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ANIMAL AND VEGETABLE
FIXED-OILS, FATS; BUTTERS,
-AND WAXES:-
THEIR PREPARATION AND PROPERTIES,
AND THE
0f
BY
C. R. ALDER BRIGHT,
D.Sc. (LOND.), B.Sc. (VicT.), F.R.S.,
LECTURER ON CHEMISTRY IN ST. MARY'S HOSPITAL MEDICAL SCHOOL, LONDON ; EXAMINER IN
"SOAP" TO THE CITY AND GUILDS OF LONDON INSTITUTE.
Witb 144 Illustrations*
OF THE
UNIVERSITY
LONDON:
CHARLES GRIFFIN & COMPANY, LIMITED;
EXETER^ STREET, STRAND.
1894.
[All Rights Reserved.]
bl
€ OF THE *" Ny
CVERSITT)
OF J
PREFACE
The complete discussion of the Sources, Production, and
General Technology of the numerous substances included in
the term Oils, and of the intimately associated Fats, Butters,
and Waxes (all of which are practically oils when melted),
would require far more space than is compatible with the
limits of the present ^or-k'; it has accordingly been found
indispensable to make a selection from this wide field, as
the result of which the subjects now dealt with are
narrowed down to the Animal and Vegetable Fixed Oils
and allied substances ; whilst Mineral Oils, Products of
Distillation, Essential Oils, and various analogous materials
are only discussed in so far as they are associated with the
Fixed Oils in their technological applications. For the
same sufficient reason minute details respecting the various
special tests employed in the practical examination of oils,
&c., for adulterations have, as a rule, been omitted ; as also
have the descriptions of the distinctive properties and
qualities of the individual oils and fats, excepting in a
comparatively small number of typical cases. In short, the
object aimed at has rather been to give general descriptions
of the methods whereby Animal and Vegetable Oils and Fat
are obtained from natural sources, of their leading practical
applications and uses, and of their chief physical and
chemical properties and reactions, than to enter into special
details, and to discuss minutely the analytical tests and
processes applicable in each separate case for the detection
of adulteration.
VI PREFACE.
The literature relating to the chemistry and technology
of fixed oils arid fats is already voluminous, and yearly
increases considerably in magnitude, being mostly dispersed
throughout the pages of numerous scientific and technical
serials. Amongst the periodicals of this description consulted
for the purpose of gathering together to some extent these
scattered results and items may be more particularly
mentioned : —
The Journal of the Society of Chemical Industry.
The Journal of the Society of Arts.
The Journal of the Chemical Society.
The Analyst.
The Chemical News.
Zeitschrift fur angewandte Chemie.
Berichte der Deutschen Chemischen Gesellschaft.
Dingler's Polytechnisches Journal.
Biedermann's Technisch-Chemisches Jahrbuch.
Moniteur Scientiftque.
Bulletin de la Societe Chimique de Paris.
Comptes rcndus.
Besides many others in which papers bearing on the matters
in hand appear from time to time. Various text-books and
technical dictionaries previously published in this country
or abroad have also been freely consulted with the object of
rendering the present work as complete as possible, with
due regard to the limits of space. In particular the author
desires to express his indebtedness to the following works: —
Schadler, Technologic der Fette und Oele* Berlin, 1883.
Allen, Commercial Organic Analysis, vol. ii., Second
edition. London, 1886.
Schadler, Untersuchungen der Fette und Oele* Leipzic,
1889.
Benedikt, Analyse der Fette und Wachsarten, Second
edition. Berlin, 1892.
* Whilst the present book was in the press the two works by Schadler
above mentioned have been incorporated into a single volume, edited by
P. Lohmann after the decease of the original author.
PREFACE. Vll
To the firm of Kose, Downs, & Thompson, of Hull, the
author is greatly indebted for numerous illustrations of the
most recent and effective forms of oil mill machinery, as
well as for valuable information concerning their use in oil
extraction generally. In similar fashion be desires to thank
Messrs. Neill & Sons, of St. Helens, for a variety of specially
made drawings of appliances used in soap manufacture;
Messrs. S. H. Johnson, of Stratford, for drawings of the
newest forms of filter presses ; and Messrs. E. Cowles & Co.,
of Hounslow, for cuts of improved candlemaldng machines.
C. R. ALDER WRIGHT.
LONDON, October, 1893.
€^E LIBR^PT^
OF THE X
;VERSITY)
OF J
TABLE OP CONTENTS
1. General Composition and Nature of Oils, Butters, Fats,
Waxes, and Allied Substances.
CHAPTER I.
THE SOURCES AND GENERAL
NATURE OF NATURAL AND
ARTIFICIAL OILS.
Meaning of the Terms "Oil,"
"Fat," "Butter," and "Wax,"
Sources and General Nature of
Oils,
Nature of Sapoiiification Changes,
Classification of Oils, Fats,
Waxes, &c. , according to Chem-
ical Composition,
CHAPTER II.
ALCOHOLIFORM SAPONIFICATION
PRODUCTS OF OILS, FATS,
WAXES, &c.
Glycerol, Glycerides, Hydrolysis
of Glycerides, .... 7
Fatty Alcohols, Ethylic Series, &c., 13
Glycols, 18
CHAPTER III.
ACID SAPONIFICATION PRODUCTS
OF OILS, FATS, WAXES, &c.
Fatty A cids- Acetic Family, . 18
Oleic Family, . . . 24
Linolic Family, . . 30
Linolenic Family, . . 36
Glycollic Family, . . 37
Ricinoleic Family, . . 39
Oxystearic Acids, . . 43
2. Physical Properties of Oils, Fats, Waxes, &e.
CHAPTER IV.
GENERAL PHYSICAL CHARACTERS.
Phy sical Texture and Consistency ;
Cohesion Figures, .
Taste, Odour, and Colour, .
Action of Polarised Light; Re-
fractive Index,
Solubility of Oils, Fats, &c., in
various Solvents,
Thermometric Scales, .
Methods used in the Determina-
tion of Fusing and Solidifying
Points, .....
Freezing and Melting Points of
Oils, &c.,
CHAPTER V.
SPECIFIC GRAVITY AND VISCOSITY.
Determination of Specific Gravity, 77
Construction of Tables of Errors
for Hydrometers and Hydro-
static Balances, . . . 82
Hydrometer Scales, . . .84
Relative Densities of the Principal
Oils, Fats, &c., . . 86
Classification of Oils, Fats, &c.,
according to their Relative
Densities, . . . .89
Variation of Density of Oils, &c.,
with Temperature, . . .92
Viscosimetry ; Mechanical Testing
Arrangements, . . . .94
Efflux Viscosimeters, . .95
Standards of Efflux Viscosity, . 101
Relative Viscosity of Oils, &c., . 102
Determination of Viscosity in
Absolute Measure, . . . 107
CONTENTS.
§ 3. Chemical Properties of Oils, Fats, Butters, and Waxes.
CHAPTER VI.
PROXIMATE CONSTITUENTS AND
THE METHODS USED FOR THEIR
EXAMINATION AND DETERMIN-
ATION.
Compound Nature of Oils, Fats,
and Waxes ; Variations in Com-
position with Circumstances of
Natural Formation,.
110
Methods Employed for Separa-
ting Constituents, . . .112
Determination of Free Fatty
Acids; Free Acid Number, . 116
Determination of Unsaponifiable
Constituents, . . . .119
Determination of Water, . . 122
Adulteration of Fats with sus-
pended Matters,
Sulphurised and
Constituents, .
Phosphorised
123
123
CHAPTER VII.
CHEMICAL REACTIONS or OILS,
FATS, £c., AND THEIR, USES AS
TESTS OF PURITY, &c.
Effect of Heat on Oils, &c. ;
Flashing Point, . . .125
Characteristic Oxidation Products, 128
Spontaneous Oxidation of Oils,
Fats, &c. ; E fleet of Light
thereon, 129
Spontaneous Combustion, . .132
Film Test; Livache's Test, . . 133
Chemical Changes occurring dur-
ing drying of Oils, . . . 134
Elaidin Reaction ; Legler's Con-
sistency Tester, . . .137
Nitric Acid Test, , . .139
Zinc Chloride Reaction and Colour
Test; Action of Zinc Chloride
on Oleic Acid, . . . .141
Action of Sulphuric Acid on Oils
and Fats ; Turkey Red Oils, . 143
Maumene's Sulphuric Acid Ther-
mal Test, . . . 147
Various Colour Reactions, . . 151
Sulphur Chloride Reaction; Vul-
canised Oils, . . . .154
CHAPTER VIII.
QUANTITATIVE REACTIONS OF
OILS.
Koettstorfer's Test— Total Acid
Number, ..... 157
Classification of Oils, &c., accord-
ing to their Saponification Equi-
valents, ..... 159
Practical Determination of Saponi-
fication Equivalents of Glycer-
ides, &c., ....
159
163
Proportion of Fatty Acids formed
by Saponification, .
Hehner's Test; Insoluble Acid
Number, . . ... . 166
Practical Determination of the
amount of Fatty Acids formed
on Saponification, . . . 167
Corrections for An hydro Deriva-
tives, Free Acids, and Unsa-
ponifiable Matters,
170
172
Mean Equivalent of Fatty Acids
contained in Soap, .
Reichert's Test and Modifica-
tions thereof, . . . .173
Bromine and Iodine Absorption ;
Bromine Process, . . . 176
Iodine Process ; Hiibl's Test, . 179
Iodine Numbers of Oils, Fats,
&c., . . . . .180
Acetylation Test ; Benedikt and
Ulzer'sTest, . . . .186
Methyl Iodide Test; Zeisel's
Test, 191
Tabulated results of the various
Quantitative Tests, . . . 194
§4. Processes Used for Extracting, Rendering, Refining,
and Bleaching Oils, Fats, &e.
CHAPTER IX.
EXTRACTION OF OILS FROM SEEDS,
&c., BY PRESSURE OR SOLVENTS.
Earlier forms of Press,
199
Elbow, Wedge, and Screw
Presses, 202
Hydraulic Press, . . . 207
Composition of Oilcake, . .213
Oil Mill Plant ; " Unit " Mill, . 214
CONTENTS.
XI
Crushing Rolls and Edge
Runners, . . . .218
Kettle ; Moulding Machine, . 221
Faring Machine ; Supplementary
Appliances, .... 223
Decortication, .... 224
Filter Presses, . ' .
Separation of Solid Stearines from
226
229
Oils, &c., .
Manufacture of Lard Oil, and
Allied Products, . . .231
Extraction of Oil from Seeds, Oil-
cake, &c., by Solvents, . . 231
Extraction of Grease from Engine
Waste, &c., . . . . 236
Determination of Fat in Seeds,
&c., 237
Proportion of Fatty Matter Con-
tained in Seeds, &c., . . 241
CHAPTER X.
A NIMAL FATTY TISSUES : EXTRAC-
TION or OILS AND FATS
THEREFROM.
Rendering of Fatty Tissues by
Dry Fusion, . . . .246
Rendering of Fatty Tissues by
Heating with Water or Steam
under ordinary Atmospheric
Pressure, .... 247
Rendering under Increased
Pressure, . . . .250
Extraction of Fat from Bones, . 251
CHAPTER XI.
REFINING ANDBLEACHING ANIMAL
AND VEGETABLE OILS, FATS,
WAXES, &c.
Suspended Matters, .
Dissolved Matters,
Sulphuric Acid Process for
Refining Oils, &c.,
Alkaline Refining Processes,
Utilisation of " Foots,"
Clarification,
Bleaching Oils and Fats,
Wax Bleaching, .
CHAPTER XII.
RECOVERY OF GREASE FROM
"SUDS," &C.
Modes of Treating Soap Suds,
Analysis of Yorkshire Grease,
Distilled Grease,
Engine Waste Grease,
254
256
259
260
261
262
263
268
270
273
277
279
§ 5. Classification and Uses of Fixed Oils, Fats, Waxes, &e. ;
Adulterations.
CHAPTER XIII.
CLASSIFICATION.
Classification according to Tex-
ture, Sources, and Essential
Chemical Nature. . . .281
CLASS I. Olive (Almond) Class;
Vegetable Expression
Oleines, . . .282
II. Rape (Colza) Class, . 284
„ III. Castor Class, . . 284
,, IV. Animal Non-Drjdng
Oils- Lard Oil Class, 285
,, V. Sesame or Cotton Seed
Class — Vegetable
Semidrying Oils, . 286
Lesser Known Vege-
table Oils, . . .287
,, VI. Drying Oils — Linseed
O'il Class, . . .290
,, VII. Train, Liver, and Fish
Oils, . . . .292
,, VIII. Vegetable Butters,
Fats, Waxes, &c., . 295
Lesser Known Vege-
table Butters, &c., . 296
„ IX. Animal Fats— Tallow,
Lard, and Butter Class, 298
,. X. Animal Oils — Sperm
Oil Class, . . .299
,, XI. Vegetable Nonglyce-
ridic Waxes, . . 301
,, XII. Beeswax and Sperma-
ceti Class, . . 301
CHAPTER XIV.
PRINCIPAL USES OF OILS AND
FATS, &c.
Classification according to Uses, . 302
Edible and Culinary Uses of Oils,
Fats, &c 303
Cotton Seed Stearine ; Vegetable
Lards, . . 305
Xll
CONTENTS.
Manufacture of Hog's Lard, . 306
Manufacture of Artificial Lard
and Batter, . . . .307
Utilisation of Fatty Matter from
an Ox, 311
Lamp Oils, 312
Drying Oils used in making Paints
and Varnishes, . . . 313
Blown Oils — Oxygen Process, . 319
Miscellaneous Uses of Oils, Fats,
&c. ; Manufacture of Lubri-
cants, 321
Analysis of Lubricating Oils and
Greases, 328
Turkey Red Oils; Analysis, . 330
Currier's Grease, Sod Oils, and
Degras, 336
Manufacture of Lanolin, . . 337
CHAPTER XV.
ADULTERATION OF OILS AND FATS.
Methods employed in Detecting
Adulterations, . . .340
Relative Values of Oils, . . 342
General Characters of Olive Oil
andTests for Adul-
terations thereof, . 342
,, Rape Seed and Colza
Oil, . . .348
Linseed Oil, . . 349
Sperm Oil, . . 353
Tallow, . . . 354
Beeswax, . . 357
Spermaceti, . . 359
6. The Candle Industry.
CHAPTER XVI.
MATERIALS USED IN CANDLE-
MAKING.
Origin of Candles ; Combustible
Materials, . • . . . 362
Manufacture of ' ' Stearine ; " the
Chevreul-Milly Process,
Composition and Analysis of
"Rock,"
Milly- Autoclave Process, .
Analysis of Red Oils, Separation
Cake, and Similar Products, .
Sulphuric Acid Process,
364
371
373
378
380
Hydrolysis of Glycerides by
Water only, . . . .385
Utilisation of Red Oils, . . 386
CHAPTER XVII.
MANUFACTURE OF CANDLES, TAPERS,
AND NIGHT LIGHTS.
Basted and Drawn Wax Candles,
Tapers, &c., . . . .388
Dip Caudles; Dipping Machinery, 390
Wicks ; Wick Pickling, . . 394
Moulded Candles ; Handmade, . 395
Continuous Moulding Machines, 398
Night Lights and Medicated
Candles, 406
§ 7. The Soap Industry.
CHAPTER XVIII. CHAPTER XIX.
MATERIALS USED IN THE MANU-
FACTURE OF SOAP.
Fatty Matters ; Alkalies, . . 408
Causticising Process, . . .411
Valuation of Alkalinity of Leys, 414
Corrections for Impurities, . .419
English, French, and German
Decrees, 420
Calculations, . . . .421
Formulae, 425
SOAPMAKING PLANT.
Heating Appliances ; Free-fired
Soap Coppers, ... 426
Morfit's Steam Twirl, . . 429
Steam-heated Soap Coppers, 432
Curb and Fan, ... 433
Soap Pumps, . . . 434
Soap Frames, . . . 434
Barring and Slabbing, . 437
Crutching, 438
CONTENTS.
Xlll
Toilet Soap Machinery ; Remelt-
ing, 441
Stamping, ..... 444
Transparent Soaps, . . . 445
Milling, 446
Plotting, 448
CHAPTER XX.
MANUFACTURE OF SOAP.
Soapmaking Processes ; Direct
Neutralisation, . . . 449
Calculations, .... 454
Processes in which the Free Gly-
cerol is retained ; Cold Process
Soaps, ..... 456
Soft, Hydrated, and Marine
Soaps, ..... 459
Calculations, .... 464
Processes in which the Glycerol
is separated ; Curd Soaps, . 466
Graining, ..... 469
Fitted and Mottled Soaps, . . 470
Special Varieties of Soap ; Rosin
Soaps, Silicated Soaps, &c., . 473
Toilet and Fancy Soaps; Milled
Soaps, 478
Transparent Soaps, &c., . . 481
Neutralised Soaps, . . .483
CHAPTER XXI.
GENERAL CHEMISTRY OF SOAP —
SOAP ANALYSIS.
General Properties of Soaps ;
Hydrolysis of Soap Solutions, 484
Reaction of Soap Solution or of
Fused Soap on Inorganic and
other Salts, . . . .488
Methods Used in the Analysis of
Soap, 492
General Scheme for Analysis, . 506
Composition of Manufacturers',
Laundry, and Toilet Soaps, &c., 508
Classification of Toilet Soaps
according to amount of Free
Alkali present, . . .512
CHAPTER XXII.
GLYCEROL EXTRACTION — MANU-
FACTURE OF GLYCERINE.
Sources of Glycerol ; Extraction, . 513
Valuation of Commercial Glycer-
ine ; Estimation of Glycerol in
Watery Solution, . . .516
Glycerol in Soap Leys, . . 522
INDEX,
525
LIST OF ILLUSTRATIONS.
FIG. PAGE
1. Cohesion Figures, ....... 48
2. Capillary Tubes used for determining Fusing Points. . . 60
3. Mode of attachment to Thermometer, . . . .61
4. Mode of heating the arrangement in Water, . . .61
5. Another Mode, ....... 62
6. Olberg's Water Bath, ...... 62
7. Bensemann's Tubes, . . . . . .63
8. Pohl's Method, ....... 64
9. Cross and Bevan's Method, ..... 63
10. Lcewe's Method, . . . . . . .65
11. Mohr's Hydrostatic Balance, ..... 78
12. Westphal's do., ..... 79
13. Lefebre's Oleometer, ...... 80
14. Hot Air Bath for use with Westphal's Hydrostatic Balance, . 81
15. Ambuhl's Arrangement, ...... 81
16. Schiibler's Viscosimeter (Efflux Method), . " . .95
17. Schmid's do., . . . . . .96
18. Redwood's do., . . . . . ,97
19. Do. do., ...... 98
20. Allen's Modification of Viscosimeter, . . . .98
"21. Engler's Viscosimeter, ...... 99
22. Hurst's do., . . . . . .100
•23. Eedwood's Chart of Viscosity of Oils, . . . .103
24. Do. do. do., .... 104
25. Lepenau's Leptometer, ...... 107
26. Traube's Apparatus, . . . . , .109
27. Chattaway's Tubes, ...... 120
28. Abel's Flashing Point Apparatus, . . . . .126
29. Pen sky's Modification of same, ..... 127
30. Legler's Consistency Tester, . . . . .139
31. Apparatus for Maumeue's Test, ..... 147
32. Jean's Thermeleometer, . . . . . .151
33. Benedikt and Griissner's Apparatus for Zeisel's Test, . . 193
34. Elbow Press, ....... 202
35. Wedge Press, Front Elevation, . ; . . | . 203
36. Do. Side do., . . . . •'" :. 203
37. Do. Longitudinal Section, . . . .204
38. Screw Press (English), ". . . . . . 205
39. Do. (German), . ... . .206
40. Hydraulic Press (German, empty), . . . 208
41. Do. (after the ram has risen), . . . 209
42. Do. (English, Handworked), .... 210
43. Do. (Anglo-American System), . . .211
LIST OF ILLUSTRATIONS. XV
FKi. PAGK
44. Hydraulic Press, Plan and Longitudinal Section of Plate, . 212
45. Do. Cross Section of Plate, .... 212
46. Oil Mill Plant; Ground Plan of 16- press Installation, . . 216
47. Crushing Rolls, . . . . . . .218
48. Edge Runners, ....... '219
49. Kettle, ........ 220
50. 51. Envelopes, ....... 221
52. Paring Machine, ....... 222
53. Decortication of Cotton Seeds, ..... 224
54. ,, of Castor Beans, . . . . .224
55. Disintegrator and Elevator, ..... 225
56. Filter Press, ....... 226
57. Do., Front Elevation of Plates, .... 226
58. Do., Sectional do., . . . . . 226
59. Do., with Pyramid Drainage Surfaces, . . . 227
60. Do., do. do., . . . 228
61. Do., Small Handworked, ..... 229
62. Apparatus for Oil Extraction by Solvents, . . . 233
63. Heyl's Distillation Apparatus, ..... 234
64. Deitz's Extraction Apparatus, ..... 235
65. Plant for Cleansing Engine Waste, .... 237
66. 67. Soxhlet's Tube (two forms), . . ... .238
68. Allihn's Reflux Condenser, . . . . .239
69. Fruhling's form of Soxhlet Tube, . . . . .239
70. Reservoir for same, ...... 240
71. Laboratory Extraction Apparatus, .... 240
72. Honig and Spitz's Apparatus, ..... 240
73. Wilson's Digester, ....... 250
74. Barrel Digester for Extracting Fat from Bones, . . . 252
75. Leuner's Apparatus, ...... 253
76. Free-fired Pan for Boiling Oil, ..... 316
77. Steam-heated Oil Kettles, . . . . .317
78. Open Pan used in manufacturing Stearine, . . . 366
79. 80. Crystallising Pans, . . . . . .367
81. Hot Press, ........ 368
82. Plant for Saponification by Open Pan Process, . . . 369
83. Plant for Hydrolysis of Fats by means of Sulphuric Acid, . 381
84. Knab's Apparatus for Distillation by Superheated Steam, . 382
85. Plant for Hydrolysis of Glycerides by Superheated Steam, . 386
86. Basting Wheel, ....... 388
87. Drawing Tapers, ....... 389
88. Knife for Cutting off Butt Ends, . . . . .390
89. Rotating Candle Dipper, ...... 390
90. Edinburgh Wheel, ....... 391
91. Wick-holder, ....... 392
92. 93. Dipper with Movable Cauldron, 393
XVI LIST OF ILLUSTRATIONS.
PAGK
FIG.
94. Candle Mould, ....... 396
95. Hand Moulding Frame, ...... 396
96. Mode of fixing Wick, .... 396
97. 98. Improved Moulding Frame, ..... 396
99. Royan's Continuous Wick Moulding Machine, . . . 397
100. Camp's Moulding Wheel, ..... 398
101. Piston of Moulding Machine, ..... 399
102. Moulding Machine and Nippers, ..... 400
103. Self -fitting Butt End, ...... 402
104. Machine for Moulding Self-fitting Butt End Candles, . . 403
105. Turnover Machine, ...... 404
106. Polishing Machine, ...... 405
107. Soap Tank for holding Ley, . . . . .412
108. Free-fired Soap Pan, ...... 427
109. Another form of do., ...... 427
110. Steam-heated Pan, ...... 428
111. Morfit's Steam Twirl, . . . . . .429
112. Soap Copper, . . . . . . . 430
113. Morfit's Steam Series, ...... 430
114. Modern form of Steam-heated Pan, .... 431
115. Plan of same, ....... 432
116. Fan, ........ 434
117. Rotary Soap Pump, ...... 434
118. Mode of building up Wooden Frames, .... 435
119. Galvanised Iron Frames, ...... 435
120. Improved form of Steel Soap Frame, .... 436
121. Cutting Soap, . ..... 437
122. Looped Wire used for cutting, ..... 437
123. Scribe, ........ 438
124. Slabbing and Barring Machine, ..... 439
125. Padded Frame, ....... 440
126. Hand Crutch, ....... 440
127. Crutching Machine, ...... 440
128. Jacketted Crutching Machine, ..... 440
129. 130. Series of Crutching Pans, . . . . .442
131, 132. Neill and Son's Remelter, . . . . . 44£
133. Hand Tablet Stamping Machine, .... 444
134, 135. Steam Stamping Machine, ..... 445
136. Rutschmann's Stripping Machine, .... 446
137. Soap Mill, ........ 447
138. Beyer's Plotting Machine, . . . . .448
139. Steam Jacketted Pan and Agitator, . . . .452
140. 141. Hawes' Boilers for Cold Process Soaps, . . .457
142. Dunn's Plant for making Hydrated Soaps under Pressure, . 463
143. Alder Wright's Chart of Hydrolysis of Soap Solutions, . 488
144. Gerlach's Vaporimeter, . . . . .' 518
1. General Composition and Nature of
Oils, Butters, Fats, Waxes, and
Allied Substances.
CHAPTER I.
THE SOURCES AND GENERAL NATURE OF NATURAL
AND ARTIFICIAL OILS, &c.
AMONGST the alchemists the term " oil " had a somewhat wider
range of application than is usual at the present day, including
various inorganic substances, such as " oil of vitriol." Similarly
" butter of antimony " and " butter of tin " were metallic deri-
vatives entirely dissimilar from cow's butter in constitution,
although resembling it in physical consistency. Even when
such wholly inorganic compounds are excluded, the term " oil "
has still an extremely elastic meaning, being employed to
designate a very large variety of liquid substances, natural
and artificial, which have but few features in common beyond
the fact that, being all organic in character, they are capable of
burning with more or less facility under suitable conditions ;
whilst with but very few exceptions they are practically in-
soluble in water, so as to be incapable of permanent solution
therein ; being as a rule lighter than water, when agitated
therewith an emulsion forms, from which the water and oil
gradually separate 011 standing, the latter usually floating as a
separate layer on the former.
The term "fatty matter," or more shortly "fat," is applied to
substances which are more or less of a soft solid character at
the ordinary temperature, but on gently heating pass to liquids
closely resembling fluid oils in general characters ; " butters "
being specially soft varieties of such fats possessing the peculiar
physical texture of cow's butter at the atmospheric temperature
of temperate climates. " Waxes," on the other hand, possess a
somewhat different and much firmer texture at the ordinary
temperature, but when heated melt to fluids which closely
resemble ordinary liquid oils and melted fats in their general
physical characters.
1
; 01 LS, FATS, WAXES, ETC.
Oils proper are derived from animal, vegetable, and mineral
sources, being mostly precontained in the tissues, seeds, or strata,
&c., from which they are obtained by simple mechanical pro-
cesses, such as pressure or pumping, or by means of solvents,
or by volatilisation ; certain products of destructive distillation,
however, are also ranked amongst oils — e.g., the "light oils,"
" creosote oils," &c., obtained during the rectification of coal tar;
and "shale oils," " bone oil " (Dippel's oil, or bone tar), "paraffin
oils," " rosin oils,5' and similar substances formed by the breaking
up of more complex organic matters under the influence of heat.
Somewhat -similar substances (fusel oils) are produced by ana-
logous decompositions occurring during fermentative changes.
Oils capable of being converted into vapour by the application
of heat wdthout suffering material decomposition (volatile oils)
are for the most part either artificial products of destructive
distillation, natural mineral oils (petroleum, very probably
formed underground by the long-continued action of intra-
terrestrial heat on subterranean organic matter), or " essential "
oils — i.e., volatile odorous matters extracted from numerous vege-
table sources, usually by distillation along with water. Fixed
oils, on the other hand, are substances not volatile without
decomposition, and are essentially of animal and vegetable
origin ; as also are butters, fats, and waxes (which practically
become fixed oils on slightly raising the temperature), with
the exception of the so-called waxes of mineral origin, paraffin
wax, ozokerite, cerasin, &c.*
From the point of view of general chemical composition, oils,
fats, butters, and waxes may be divided into two leading classes-
— viz., those consisting of carbon and hydrogen only (Jiydro-
carbons); and those containing carbon, hydrogen, and oxygen.
Oils, &c., of the former class are practically all volatile without
decomposition ; those of the second class are in some cases
volatile without change (e.g., oxidised essential oils), but, as a
rule, are " fixed," undergoing destructive distillation when heated,
so that the vapours emitted are produced in consequence of
decomposition.
Hydrocarbon oils include a large number of " essential oils "
(in which oxidised substances are often present along with hydro-
carbons) ; paraffin and petroleum oils, including the lightest and
most volatile distillates of the " benzoline " class, " burning oils "
(kerosenes, <fec.) of medium volatility, "lubricating oils" of
higher boiling point, and paraffin waxes, Arc.; coaltar oils of
* The terms " fat " and " butter " are not confined to the fatty matters
obtainable from the adipose tissues of animals and the milk of mammalia ;
thus, various vegetable fats and butters are known, e.g., Dika fat, Palm
butter, Shea butter, vegetable tallow, &c. Similarly, whilst animal waxes
are the best known products of the wax class, various forms of vegetable
wax occur in nature (e.g., Japanese wax and Carnauba wax).
THE SOURCES AND GENERAL NATURE OF OILS, ETC. 3
various kinds ; and other analogous products of destructive
distillation, from which various "closed chain" hydrocarbons,
(benzene, naphthalene, anthracene, &c.) are isolable, along with
many other kinds of hydrocarbons, some of the " saturated "
class (paraffins, indicated by the general formula CnHon + 2), some;
of the " unsaturated " classes (CmH2n, where n is not greater
than in}.
Oxidised oils (including fats, butters, and waxes), from the point
of view of chemical constitution, are divisible into two classes —
viz., those that are, and those that are not, of the nature of
" compound ethers," or substances capable of undergoing changes,
of the character of that known as " saponification." Oils of the
first class are again divisible into two groups — viz., Glycerides,
or oils, &c., developing glycerol by saponification ; and Non-
glycerides, or oils not developing glycerol by saponification, but
giving rise instead to some other alcoholiform product. As
examples of these two groups may be mentioned, olive oil,
coker* butter, mutton tallow, cow's butter, Japanese wax,
linseed oil, colza oil, cod liver oil, and whale oil, essentially
glyceridic in character ; and oil of wintergreen (chiefly methyl
salicylate), beeswax (mainly myricyl palmitate), spermaceti
(chiefly cetylic palmitate), and sperm and doegling oils, essenti-
ally non-glyceridic in character.
Oils, &c., of the second class (non-saponifiable) include various
oxidised essential oils belonging to different organic families —
e.g., aldehydes, such as oil of bitter almonds (benzoic aldehyde) ;.
ketones, like oil of rue (methyl nonyl ketone) and oil of tansy
(methyl octyl ketone) ; alcohols, such as oil of geranium
(geraniol) ; camphor analogues, such as oil of wormwood (absin-
thol) ; and resinoid constituents. Various alcoholiform sub-
stances are also contained in the free state in natural oils,
greases, &c. ; thus woolgrease contains cholesterol, and amber-
gris an allied body ambreol ; whilst similar substances are found
in small quantity in many vegetable oils. Higher alcohols (e.g.,
cetylic alcohol) are often present in the free state in marine
cetacean oils ; whilst phenol and its homologues are present in
coaltar oils and other products of destructive distillation.
SAPONIFICATION .
Originally the term " Saponification " was used to designate
the chemical changes taking place when soap is prepared by
the action of alkalies on fixed oils and fats ; but subsequently it
* Although the spelling " coker" at first sight looks inelegant, it is con-
venient to employ it instead of " cocoa," in order clearly to distinguish the
product of the cokernut palm (Cocos nucifera) from that of the cacao (choco-
late plant yielding the beverage cocoa) and the coca (yielding the alkaloid
cocaine).
4 OILS, FATS, WAXES, ETC.
has been extended to include a large number of parallel changes
occurring where various classes of " compound ethers " are broken
up under the influence of alkalies or other bases, so as to give
rise, on the one hand, to the metallic salt of an organic acid, and,
on the other, to an alcoholiform complementary product. The
following equations represent typical reactions of saponification,
according as' the alcoholiform product is an alcohol of the mono-
hydric, dihydric, trihydric, or tetrahydric class : —
Ethyl Acetate.
C2H5.O.C2H30
Potassium Potassium
Hydroxide. Acetate.
K . OH = K . 0 . C2H30
Ethylic
Alcohol.
+ C2H, . OH
Ethylene Diacetate.
Potassium
Hydroxide.
Potassium
Acetate.
2K.OH = 2K.O.C2H,0
Glycol.
r (OH
Uiyceryl Tristearate
(Stearin).
C3H5
O.C1SH350
O.C18H350
O.C18H350
Erythrol Tetrabenzoate.
O.C7H50
O.C7H50
O . C7H5O
O.C7H50
4. C4H
Sodium
Hydroxide.
Sod'um
Stearate.
SNa.OH = 3Xa. 0. C18H350
Sodium
Hydroxide.
4Na.OH
Sodium
Benzoatc.
Glycerol.
( OH
(OH
Erythrol.
( OH
4Na.O.C7H50 + C4H6 < ™
f OH
The majority of saponification changes occurring with natural
fixed oils and fats, £c., belong to the third class ; i.e., these sub-
stances are chiefly " glycerides," or compound ethers furnishing
glycerol on saponification ; some liquid fixed saponifiable oils,
however, are of non-glyceridic character, undergoing saponifica-
tion changes of the first kind ; thus sperm oil largely consists of
Cetylic pliysetoleate and homologous substances, broken up by
saponification, thus —
Cetyl Physetoleate
C]6H33.O.CiCH290
Potassium Potassium
Hydroxide. Physetoleate.
K.OH = K.O.C1GH290
Cetylic Alcohol.
C1CH33.OH
Most waxes possess an analogous constitution; thus the chief
constituents of beeswax and spermaceti are respectively myricyl
palmitate and cetyl palmitate, decomposable by saponification,
thus —
Myricyl Palmitate.
^3oH(;i . 0 . CicH3iO
Sodium
Hydroxide.
Na.OH = Na.O.C16H31O
Sodium
Palmitate.
Myricylic
Alcohol.
CsoHgi . OH
Cetyl Palmitate.
Potassium Potassium
Hydroxide. Palmitate.
K.OH = K.O.CJ6H310
Cetylic
Alcohol
C1CH33.OH
THE SOURCES AND GENERAL NATURE OF OILS, ETC. 5
Some few vegetable waxes, however, are of glyceridic char-
acter, e.g., Japanese wax, chiefly consisting of palmitic glyceride,
08H6(O.C16H810)8.
A considerable number of oxidised essential oils also consist
mainly of compound ethers of the first class ; thus oil of winter-
green (Gaultheria procumbens) mainly consists of methyl salicylate,
and oil of cow parsnep (fferacleum spondylium) ,of octyl acetate :
respectively saponified, thus —
Potassium Potassium Methylic
Methyl Salicylate. Hydroxide. Salicylate. Alcohol.
CH3.O.C7H502 + K.OH = K.O.CrH502 + CH3.OH
Sodium Sodium Octylic
Octyl Acetite. Hydroxide. Acetate. Alcohol.
C8HU.O.C2H30 + Na.OH = Na . 0 . C2H30 + C8H17.OH
Compound ethers of Class II. (furnishing dihydric alcohols on
saponification), although not absolutely unknown amongst natural
products of the oil, fat, and wax class, are very rare ; carnauba
{OTT
OH
on saponification (p. 18). Tetrahydric ethers, like those of
erythrol, have not as yet been recognised as constituents of oils
and fats, &c. ; and the same remark applies to the yet more com-
plex pentahydric and hexhydric ethers; mannitol, C6H8(OH)6r
a hexhydric alcohol, has been found as a constituent of vege-
table fruits, &c., accompanying oil — e.g., in unripe olives ; but.
neither mannitol nor any ethers thereof appear to be contained
in purified expressed olive oil.
CLASSIFICATION OF OILS, FATS, WAXES, &c.,
ACCORDING TO CHEMICAL COMPOSITION.
The following table indicates a rough classification of the
principal varieties of oils, fats, and waxes in accordance with
the general chemical character of their leading constituents : —
DIVISION I.— HYDROCARBONS.
1. Natural essential oils, mostly of vegetable origin.
2. Natural mineral oils (petroleum), including the crude oils, and the pro-
ducts thence obtained by distillation, &c. (benzoline, kerosene oils,
lubricating oils, <fcc.)
3. Artificial products of destructive distillation (paraffin oils, shale oils,
bone oils, coaltar oils, &c.)
4. Solid hydrocarbons obtainable from natural products (earthwax, &c.) or
isolated from the two previous sources — e.y., paraffin wax and allied
substances largely used in candle-making.
6 OILS, FATS, WAXES, ETC.
DIVISION II.— CONTAINING OXYGEN.
A . — Saponifiable.
1. Essentially compound ethers of monohydric alcohols.
a. Various natural essential oils mostly of vegetable origin.
6. Certain animal fixed oils, especially those of cetacean origin (some-
times termed " liquid waxes").
c. Most animal and vegetable solid waxes (waxes proper).
d. Certain artificial essential oils— t.g., various compound ethers used
for perfumery and flavouring purposes.
2. Essentially glyceride*, or compound ethers of glycerol.
a. The majority of animal and vegetable fixed oils, fats, and butters.
b. Some few vegetable waxes.
JB. — Not Saponifiable.
a. Various essential oils, consisting of aldehydes, ketones, camphora-
ceous bodies, &c.
6. Alcoholiform constituents of natural animal and vegetable oils
(cholesterol, phytosterol, cetylic alcohol, &c.)
c. Alcoholiform bodies formed by fermentation (fusel oils).
d. Phenoloid bodies formed by destructive distillation and contained
in coaltar, &c. (phenol, cresol, &c. )
e. Products formed by oxidation of hydrocarbons — e.g., " Sanitas oil'*
(formed by the atmospheric oxidation of oil of turpentine).
In the present work a large number of the various substances
thus coming into the general category of oils, fats, butters, and
waxes are necessarily excluded from minute consideration, fixed
animal and vegetable oils and fats, &c., all practically belonging
to Division II., Sections 1 and 2. Certain hydrocarbons, how-
ever, are intimately connected with the subjects dealt with,
more especially mineral oils and products of destructive distilla-
tion employed as adulterants of animal and vegetable fixed oils,
-and as ingredients in lubricating mixtures, &c. ; and mineral
waxes (paraffin wax, ozokerite, and similar substances) employed
as candle materials. Various essential oils, moreover, are in use
as ingredients in certain kinds of fancy (toilet) soaps as perfuming
agents, and in some kinds of sanitary soaps (e.g., eucalyptus oil) ;
as also are certain products of destructive distillation (e.g., car-
bolic acid and its higher homologues).
For further classifications of fixed oils, fats, waxes, &c.
(apart from other kinds of oils), based either on their physical
characters and the chemical nature of their main ingredients, or
on their leading technical uses, vide Chap. xin.
SAPONIFICATION PRODUCTS OF OILS, PATS, WAXES, ETC.
CHAPTER II.
SAPONIFICATION PRODUCTS OF OILS, FATS,
WAXES, &c.
ALCOHOLIFORM PRODUCTS.
A SAPONIFIABLE oil, &c., as above stated, gives rise to two pro-
ducts under the influence of alkalies — viz., an alcoholiform
organic substance (which in practice is either glycerol or some
kind of monohydric alcohol), and the alkali salt of an organic acid.
Under suitable conditions (more especially heating under pres-
sure in contact with water) parallel decompositions can be
brought about by means of water, the products of the " hydro-
lysis " thus effected being the alcoholiform body and a free
" fatty acid." Thus in the cases of the glyceride of oleic acid and of
cetyl palmitate the hydrolytic actions take place in accordance
with the following equations : —
Oleic Glyceride. Water. Oleic Acid. GHycerol.
O.C18H330 (OH
C3H5 O.C18H330 + 3H20 = 3C18H33O.OH + C3H5 \ OH
O.C18H330 (OH
Cetyl Palmitate. Water. Palmitic Acid. Cetylic Alcohol.
C1CH33.O.CJ6H310 + H20 = CJGH31O.OH + C16H33 . OH
Similar reactions occur in many other parallel cases, the nature
of the alcoholiform body and of the fatty acid developed only
differing in each instance.
TRIHYDRIC ALCOHOLS FORMED BY SAPONI-
FICATION (GLYCEROL).
Glycerol, the most frequently occurring alcoholiform saponi-
fication product of fixed oils and fatty matters, solidifies, when
pure, to a crystalline mass by long continued chilling,* the melting
point being about + 22° C.; its great hygroscopic character renders
it extremely difficult to obtain absolutely free from water, in
consequence of which values varying from 1*262 to 1*2653 have
* Passing a few bubbles of chlorine into concentrated glycerol will often
make it crystallise (Werner). Chilled glycerol usually crystallises when
stirred up with a few crystals of the previously solidified substance, a
method utilised in manufacture (Chap, xxn.)
8 OILS, FATS, WAXES, ETC.
been stated as its specific gravity at 15°. When heated gently
under the ordinary atmospheric pressure it volatilises without
decomposition, but at higher temperatures it splits up into water
and acrolein, thus —
Glycerol. Acrolein.
C3H803 = 2H20 + C3H40
In vacuo it boils at about 1 80° C.
By cautious oxidation with alkaline permanganate it yields
oxalic acid in sufficiently accurate proportions for quantitative
estimation. By treatment with potassium dichromate and sul-
phuric acid it similarly forms CO2 and water; by treatment with
acetic anhydride it forms triacetin, the saponification of which
furnishes another means of quantitative determination (vide
Chap, xxii.) In the absence of substances carbonised by
sulphuric acid, an excellent qualitative test is to heat cautiously
to 120° or a little higher a mixture of two drops glycerol, two of
fused phenol, and about as much sulphuric acid \ a brown solid
mass forms, which after cooling dissolves in ammonia with a
beautiful carmine red colour (Reichl) ; if substances becoming
carbonised are present they produce a dark brown colouring
matter which hides the red tint.
Polyglycerols. — Glycerol heated in contact with hydrochloric
acid or certain other dehydrating substances is capable of
undergoing reactions of dehydration and condensation, expres-
sible by the general equation : —
nC3H803 = mH,0 + C3nH8n_om03u_m.
Thus when n = 2 and m — 1, diglycerol results.
C3H
2C3H5(OH)3 = H20 + 10
C3H5
l(OH)2
And when n .= 3 and m = 2, triglycerol is produced.
(OH),
3C3H6(OH)3 = 2H20 + C3H5JOH
r°
C«H*\(OH)2
It has been supposed by some chemists that bodies of this
class are sometimes contained in commercial " glycerines," more
especially those formed under high pressure in autoclaves, or
purified by distillation; such glycerine, when slowly evaporated
at a temperature of about 160° u.,* leaves a non- volatile organic
* Lewkowitsch, Year Boole of Pharmacy, 1890, p. 380.
ALCOHOLIFORM PRODUCTS OF SAPONIFICATIOX. 9
residue, from the weight of which (after deducting ash) the
proportion of polyglycerols present may be deduced. It does
not appear, however, that the residue thus left has been definitely
proved to have the character and composition assigned to it,
although the formation of polyglycerols is, a priori, highly pro-
bable.
Natural Triglycerides. — As a very general, if not abso-
lutely invariable, rule, only one acid radicle is contained in any
given substance — i.e., substances of the types
CH2 . OR CH2 . OR CH2 . OR
CH . OR CH .OS CH . OS
CH2 . OS CH2 . OR CH2 . OT
(where K, S, and T are not the same) are only extremely rarely-
met with. Cow's butter, however, not improbably contains a
mixed glyceride of one or other of these classes ; for whilst it
forms butyric acid on saponification, no butyrin (tri glyceride of
butyric acid) can be dissolved out from it by means of alcohol ;
whereas mixtures of butyrin and other triglycerides readily
yield the former to that solvent ; hence a mixed glyceride,,
oleo palmito butyric glyceride^
CH2.O.C]8H330
CH . 0 . C1CH310
I
CH2 . 0 . C4H70
(or some analogous substance) has been supposed to be present,
breaking up on saponification into glycerol, with formation of
salts of oleic, palmitic, and butyric acids.
Some few other fats have been supposed, on similar grounds, to
contain analogous mixed glycerides ; but, as a general rule, when-
ever an oil or fat yields on saponification the salts of two or more
different fatty acids, it can be shown that the original substance
is a mixture of two or more triglycerides of the ordinary type-
(i.e., each containing only one acid radicle) ; thus, by chilling an
oil yielding palmitic and oleic acids on saponification, a solid fat
usually separates, yielding only palmitic acid on saponification ;
whilst the liquid portion is substantially olein, giving rise to
oleic acid only on similar treatment, the reaction in each case
being indicated by the general equation : —
Normal Caustic P,, _ _, Potassium
Triglyceride. Potash. Salt
CH2 . OR CHo . OH
I I
CH . OR + 3K . OH = CH .OH + 3K . OR
CH2 . OR CH3 . OH
10
OILS, FATS, WAXES, ETC.
the effect of the alkali being always the same, the only differences
in different cases being due to the variation in the nature of R.
Hydrolysis of Glycerides. — As a general rule, pure triglyce-
rides are acted upon by water only at an elevated temperature,
treatment with superheated steam blown through the mass, or
digestion with water under considerable pressure being requisite;
under such circumstances, the glycerol set free is often more or
less decomposed by secondary reactions. With crude unpurified
oils continued standing at the ordinary temperature often suffices,
the action in such cases being largely due to changes of a fermen-
tative character taking place in the mucilaginous or albuminous
extractive matters present as impurities ; in extreme cases the
action goes on to such an extent as to hydrolyse the larger
portion of the glycerides present, so that upwards of 50 per cent,
of the mass is free fatty acid. Changes of this description are
almost invariably accompanied by the production of bye-products
of unpleasant taste and smell, so that the development of " ran-
cidity " by this action greatly deteriorates the value of the oil,
<fec., for many purposes, more especially culinary and edible ones.
In all probability the formation of a free fatty acid and glycerol
from a glyceride by hydrolytic action takes place in three stages,
giving rise to two kinds of intermediate products, diglycerides
.and monoglycerides respectively ; thus, it' R be a fatty acid
radicle —
Normnl
Triglyceride.
OH2 . OR
CH . OR +
CH2 . OR
Dislyceride.
CH2 . OR
I
CH .OR +
I
CH.> . OH
Waier.
HoO =
Fatty
D'uzlyceride.
CH2.OR
CH .OR
I
CH2 . OH
Fatty Acid.
H.OR
Water. Monoglyceride. Fatty Acid.
CH2. OR
H,,0 = CH .OH + H . OR
CHo.OH
Monojjlyceride.
CH3.OR
CH .OH +
I
CHo.OH
"Water.
H20
Glycerol.
CHo . OH
Fatty Acid.
H . OR
= CH .OH
CH2 . OH
The final action may consequently be expressed by the equation-
Triglyceride.
CHo. OR
CH .OR
CHo. OR
Water.
3H20 =
Glycerol.
CH2.OH
CH .OH
CHo . OH
Fatty Acid.
3 H.OR
ALCOHOLIFORM PRODUCTS OF SAPONIFICATION. 11
which may be written somewhat more compactly —
+ 3H-OR
The formation of the intermediate substances by gradual
hydrolysis has not been much studied as yet ; in the case of
rape oil, however, it has been shown that whilst fresh oil con-
tains the triglyceride erucin,
(C22H410)3
the corresponding diglyceride dierucin,
CTT \ /~^TT /^\ r^ TT /"\
3-T15 J l_y±lo . U . v^2l>^Ml^'
(C22H410)., [ 03 = CH . 0 . Co2H410
" H I CH2 . 0 . H
is sometimes contained in old oil,* probably formed as above by
partial hydrolysis. On the other hand, the reverse reactions
leading to the successive building up from glycerol of mono-
glyceride, diglyceride, and triglyceride are well known laboratory
operations : thus —
Glycerol. Fatty Acid. Monoglycf-ride.
( OH I OR
C3TlJOH -l- H.OR = CSH5 OH + H,O
(OH (OH
Monoglycfride. Diglyceride.
( OR ( OR
C3H5 \ OH + H . OR = C3Hn { OR + H,0
(OH (OH
Diglycsride. Triglyceride.
( OR ( OR
CoH5 OR + H.OR = C3H5 OR + H20
(OH (OR
In many cases, when it is desired to obtain triglycerides in a
state of purity, it is more easy to saponify an oil, separate and
purify the resulting fatty acids, and convert them into glycerides
in this way than it is to separate the original glycerides them-
selves contained in the oil.
The following boiling and melting points are possessed by
some pure triglycerides prepared synthetically in this way : —
Melting Poiut. Boiling Point.
Butyrin, . . C3H5(0 . C4H70)3 Fluid 285°
Laurin,
Myristin, .
Palmitiii, .
Stearin,
Olein,
C3Hs(0 . Ci2H230)3 45°
C3H5(O.C14H270)3 55
C3H5(O.C1CH310)3 62
C3H5(0 . C18H350)3 71-5
C3H5(0 . C18H330)3 solidifies at - 6°
*Reimerand Will(Berichte der Deut. Chem. Ges., 1886, xix., p. 3320) found,
that a deposit which had slowly formed in a quantity of colza oil was not
the triglyceride usually obtained tinder such conditions, but the diglyceride
melting at 47°.
12 OILS, FATS, WAXES, ETC.
When oils that have become hydrolysed through rancidity are
refined by treatment with alkalies (Chap. XL), the free acids are
removed and neutral oils left ; but other kinds of refining pro-
cesses do not affect the free acids, which accordingly are apt to
be found in commercial oils to varying extents, sometimes only
inconsiderable amounts, and sometimes very large percentages
being present. According to Thum the free acids do not consist
solely of oleic acid, as is often supposed, but of a mixture in
exactly the same proportions as that in which they exist in the
undecomposed glycerides. Thus palm oil and olive kernel oil
containing much free acid yield as much solid free acids relatively
to oleic acid when the free acids are removed by agitation with
a cold alkaline ley, as are yielded by the neutral unsaponified
fats present.
Just as the glyceridic compound ethers of fatty acids are apt
to be hydrolysed under appropriate conditions, so are their
alkaline salts (soaps) split up by water with the formation of
basic substance (free alkali) and an acid salt (vide p. 23).
It is a remarkable fact that although a somewhat considerable
number of monohydric alcohols are known to be formed by the
saponification of fixed oils, essential oils, and similar sub-
stances, only one trihydric alcohol, viz., glycerol, has ever been
found to be produced from such sources.
Isoglyceride Theory. — Theoretically the existence is possible
of various substances possessing the composition of a trihy-
droxylated propane, C3H5(OH)3, but not identical with glycerol :
these substances would naturally form compound ethers isomeric
with ordinary glycerides containing the same acid radicles.
Amongst such hypothetical bodies, the compound ethers of ortho-
propionic acid, indicated by the general formula —
( OR
C ] OR (JH., . OR
| /OR |
CH, isomeric with CM . OR
! ' I
CH, CH2.01l
have been supposed by some chemists to be present in certain
fatty matters, notably cow's butter ; but the experimental proofs
of this supposition are singularly wanting in clearness and
cogency. Such compound ethers on saponification should neu-
tralise four instead of three equivalents of alkali, generating an
alkaline propionate instead of glycerol ; thus —
Hypothetical Sodium
Isogyceride. Hydroxide. Sodium Propionate. Sodium Salt. Water.
C2H5.C(OR)3 + 4NaOH = C,H3 . CO . ONa + 3NaOR + 2H2O
ALCOHOLIFORM PRODUCTS OF SAPONIFICATION. 13
MONOHYDRIC ALCOHOLS FORMED BY
SAPONIFICATION.
Numerous families of alcohols (monohydroxylated hydro-
carbons) are known to the chemist, derived successively from
saturated hydrocarbons of the series Cn H2n + 2, and from the other
series of hydrocarbons containing less hydrogen, by the replace-
ment of hydrogen by hydroxyl : thus inter alia the following
families of alcohols are known : —
Ethylic alcohol homologues ; general formula, Cu H-n+i . OH
Allylic „ ,, „ „ CaHo^.OH
Phenol ,, ,, „ CnH»n-7.0H
Cinnamic alcohol ., „ ,, CnH2n-9,OH
Although representatives of several such families of alcohols
are found amongst products of destructive distillation (coaltar
oils, £c.), and in essential oils and the allied balsams and other
aromatic bodies, and in small quantities as natural constituents
of fixed oils of various kinds (occurring there in the free state),
yet compound ethers derived from alcohols of the first and second
of the above families appear to be the only kinds naturally
occurring in fixed oils and waxes, etc. ; and of these by far the
most frequently occurring substances belong to the first class.
Ethylic Series of Alcohols. — The table on next page indicates
the leading alcohols of this family (general formula CnH2n + i . OH)
derived from fixed and essential oils and similar sources ; besides
those mentioned numerous isomeric modifications of many of
them exist, obtainable artificially by laboratory reactions.
The higher alcohols of this series, when fused with alkalies,
evolve hydrogen with formation of the alkali salt of the corre-
sponding fatty acid;* thus —
CVtylic Alcohol. Potassium Palmitate.
C15H31.CH2.OH + KOH = C15H31.CO.OK + 2H2
Myricylic Alcohol. Potassium Melissate.
C29H59.CH2.OH + KOH = C29H59 . CO . OK -f 2H2
They are readily converted into compound ethers by treatment
with organic anhydrides (e.g., acetic anhydride), and in some
cases by heating with the acids alone, water being evolved.
* C. Hell (Liebig's Annalen, pp. 223, 269) has based a method for the quan-
titative determination of higher alcohols on this reaction, the substance to
be examined being heated to 300°-310° in contact with soda lime, and the
evolved hydrogen collected and measured. At higher temperatures there
is a possibility of hydrogen being also evolved by the action of caustic
alkalies on oleic acid (p. 24). This method has been found useful in the
examination of beeswax which, when genuine, furnishes about 54 per
cent, of myricylic alcohol.
14
OILS, FATS, WAXES, ETC.
Name.
Formula.
Boil ing Point.
Melting
Point.
Sources.
Methylic alcohol,
CH3 . OH
cc°c.
...
Saponification of oil of winter-
green ; wood distillation
products.
Ethylic alcohol,
C2H5 . OH
78°
Fermentation of saccharine
matter.
Propylic alcohol, )
97°
Fermentation fusel oils.
Isopropylic alco- '
hoi, )
C3H7 . OH
84°
Isopropylic iodide from gly-
cerol and hydriodic acid.
Normal Butylic j
117°
...
Heavy oils from brandy.
alcohol,
C4H9. OH
Isobutylic alcohol )
Amylic alcohols
dHn.OH
107°
127°-13S°
...
Potato and beet fusel oils.
Fusel oils from grain spirit,
(several isomeric !
&c. Saponification of oil
modifications),
of Roman Chamomile.
Hexylic alcohols
CCH13.OH
147°-157°
Sapouification of oil of cow's
(several modi-
parsley, oil of Roman Cha-
fications),
momile, &c.
Normal Primary C 7 Hj 3 . OH
176°
Brandy fusel oils. Hydro-
Heptylic alcohol,
genation of ccnaiithol from
castor oil.
Octylic alcohols,
C8H]7.OH
180°- 192°
Saponification of oil of Hera-
deum spondylium and H.
giganteum. Action of hot
alkali on castor oil.
Nonylic alcohols,
C9H19.OH
...
.
Normal Primary
C10H21.OH,
119° at 15
7°C.
Hydrogenation of capric
Decy lie alcohol,
millims.
aldehyde.
pressure.
Secondary Hen-
CnH23.OH
220°
...
Hydrogenation of oil of rue.
decylic alcohol,
Dodecylic alcohols, C12H25.OH
143° at 15
24°
Hydrogenation of lauric
millims.
aldehyde.
Tridecylic alcohols,
C13H27.OH
pressure.
19°
Saponification of sperm oil.
Normal Primary
CJ4H29.OH
167° at 15
38°
Hydrogenation of myristic
Tetradecylic
millims.
aldehyde.
alcohol,
pressure.
Pentadecylic alco- C15HC1.OH
...
...
hols,
Normal Primary \
lS9°'5atl5
49°'5
Hydrogenation of palmitic
Hexadecylic al- '
C.^Ho* OH
millims.
aldehyde.
cohol, (
^1 6^*33 • vJi
pressure.
Cetylic alcohol, )
188°- 193°
49° '2
Saponification of spermaceti.
at 15mm.
...
pressure.
Heptadecylic al-
c]7HC;.OH
...
...
cohols,
Normal Primary
C18H37.OH
2 10° -5 at
59°
Hydrogenation of stearic
Octodecylic al-
15millims.
aldehyde. Saponification
cohol,
pressure.
of spermaceti (in small
quantity).
Cerylic alcohol, \
Isocerylic alcohol, J
C27H55.OH
... \
79°
62°
( Chinese wax.
< Carnauba wax.
( Wax of Fkus gummiflua.
Myricylic alcohol, )
,
81!0
-p
xSeeswax.
Isomyricylic alco- >
hoi ? \
CSOH61.OH
... (
oO
72°
Carnauba wax.
ALCOIIOLIFORM PRODUCTS OF SAPONIFICATIOX. 15
Acetic
Cetylic Alcohol. Anhydride. Cetyl Acetate. Acetic Acid.
C]6H33.OH + (C2H30)20 = C]0H33.O.CoH30 + C2H3O.OH
Cetylic Alcohol. Acetic Acid. Cetyl Acetate. Water.
C16H33.OH + C2H3O.OH = C1GH33.O.C2H30 + H20
The compound ethers thus produced are, in turn, readily
saponified by alcoholic potash, and from the amount of potash
neutralised during the operation the molecular weight of the
alcohol is deducible, due corrections being made for unsaponifi-
able matters, &c., if present (Chap, viu.)
Allylic Series of Alcohols. — Alcohols of the series
CnHgn.j.OH, derived from the olefine family of hydrocarbons
of formula CnH9n, are only sparsely represented amongst the
derivatives from natural products. Acrolein (acrylic aldehyde),
C2H3. CHO, by hydrogenation yields allylic alcohol, C2H3.CH2.OH
(also obtainable in various other ways), existing as a thiocyanic
ether in the oils of black mustard seed, horse radish, and garlic ;
whilst higher homologues are probably contained amongst the
alcohols of the previous series obtained on saponifying sperm
oil, since in certain cases a deficiency of hydrogen is observed
on analysis, coupled with a strongly marked tendency to com-
bine directly with iodine, indicating the presence of unsaturated
compounds. These higher alcohols, however, have not as yet
been isolated from the other bodies accompanying them in a
state of sufficient purity to admit of their formulae being exactly
determined. Borneol, C10H19 . OH, occurs in the camphor of
Dryobalanops camphora, and to a small extent in oil of valerian
and oil of rosemary.
Alcohols of the series CnH2n_3. OH, derived from the CnH2n_2.
(acetylene) series of hydrocarbons, are found to some extent in
certain essential oils — e.g., geraniol, C10Hllr .OH, in Indian gera-
nium oil. This appears to be a true analogue of ethylic and
allylic alcohols, being capable of yielding by oxidation an alde-
hyde and a monobasic acid (geranic acid) C9H15 . COH and
C9H15 . CO . OH respectively : no substances of analogous char-
acter have as yet been isolated from fixed oils and fats, tfcc.
Phenol and its Homologues. — Alcohols derived from hydro-
carbons still poorer in hydrogen are occasionally met with as
constituents of natural products of the resinous class, or as sub-
stances formed by destructive distillation; thus the hydrocar-
bons of the benzene family, CnH2n_6, give rise to two such classes
of alcohols, both indicated by the general formula CuH:n_7.OH
and derived from the same parent body, phenol, CGH5 . OH. In
the one class (phenols proper) the hydroxyl group is situated in
connection with the " benzene nucleus " of 6 carbon atoms ; and
in the other (benzylic alcohol series] the hydroxyl group is not
situated in the benzene radicle, but in one of the "side chains "
16 OILS, FATS, WAXES, ETC.
introduced by the methylation of benzene so as to develop
homologous hydrocarbons ; thus —
Phenols.
Phenol (carbolic acid), . . . C6H5 . OH
Cresol (methyl phenol), . . . CCH4/^3
( CH3
Xylenol (dimethyl phenol), . . CCH3 { CH3
OH
Phlorol (ethyl phenol), . . . CGH4 £|p
Benzylic Alcohol Series.
Benzylic alcohol, .... CGH5.CH2.OH
Xylylic alcohol, ..... C«H*{cH2 OH
Benzyl carbinol, ..... C6H5 . CH22/CH2 . OH
Alcohols of the phenol class are mostly contained in the tars
derived from the destructive distillation of coal, wood, &c. :
benzylic alcohol is contained as such in the volatile oil of cherry
laurel, and in the form of a compound ether in Balsam of Peru
and Liquid Storax ; a higher homologue, sycocerylic alcoJwl,
C18H29 . OH, is similarly found as an acetic compound ether in
the resin of Ficus rubiginosa : a-lactucerol and (3-lactucerol' are
two isomerides thereof contained as acetic ethers in lettuce juice.
Quebrachol (from Quebracho bark), and cupreol and cinchol
(from Cinchona barks) are analogous substances isomeric with
one another and indicated by the higher homologous formula,
C20H33 . OH ; whilst Pliasol (from Phaseolus vulgaris) is a lower
homologue, C]5 H23 . OH. All these substances are closely akin
to cholesterol, isocJiolesterol, phytosterol and paraphytosterol, alco-
holiform substances belonging to the family derived from the
hydrocarbons, CnH2n_8, and occurring in various fixed oils as
normal constituents dissolved in the glycerides, <fcc., constituting
the bulk of the oils. It is extremely probable that other
.analogous substances are also similarly contained in oils, <fec.,
but as yet this has not been demonstrated to be the case. In
the husks of PJiaseolus vulgaris both paraphytosterol and phasol
are present ; when such substances occur in the vicinity of oil-
containing tissues, obviously any process applicable for the ex-
traction of the oil is extremely likely to dissolve out more or
less of the accompanying alcoholiform substances, as well as any
other substances soluble in oil that may happen to be contained
in the seeds, <fcc., operated upon.
Cholesterol Series and Analogues. — Cholesterol and its
isomerides appear to be homologues of cinnamic alco/iol, C9H9.OH
(contained in storax as cinnamic ether), indicated by the formula
C9(5H43 . OH ; some (cholesterol — long known as a bile constituent
ALCOHOLIFORM PRODUCTS OF SAPONIFICATION. 17
— and isocholesterol) chiefly occur in oils, &c., of animal origin,
such as whale and fish oils and woolgrease ; others (phytosterol
and isophytosterol) are similarly found in vegetable oils, such as
olive oil. Ambergris and castoreum (from the Castor beaver)
also appear to contain related substances (ambreol and castorol
respectively). All these bodies, like the sycocerylic alcohol and
its homologues above mentioned, are of alcoholiform character
readily yielding acetic and benzoic compound ethers (often of
highly crystalline character, and readily purified in consequence),
the melting points of which are characteristic. Thus, cholesterol
heated with benzoic anhydride (preferably in a sealed tube at
200°) forms a compound ether almost insoluble in boiling alcohol,
but^ crystallisable from ether in right-angled tables, melting at
150°-151 °. The following table illustrates some of the differences
between cholesterol and its isomerides : —
Melting Point.
Action on Polarised
Light.
Melting Point of
Benzoic Ether.
Cholesterol, . .
Isocholesterol, .
Phytosterol, .
147°
137°- 138°
132°- 133°
Lsevogyrate.
Dextrogyrate.
Lsevogyrate.
150°-151°
190°-191°
Paraphytosterol,
149°- 150°
Dextrogyrate.
When dissolved in chloroform and treated with an equal
volume of sulphuric acid, cholesterol yields a blood red colora-
tion, soon becoming cherry red and purplish, permanent for
several days ; the acid underlying the chloroform solution ex-
hibits a strong green fluorescence. Phytosterol gives a similar
coloration, becoming a bluish red on standing some days ; whilst
isocholesterol gives no colour at all. On treatment with acetic
anhydride, compound ethers are produced in each case, the
"acetyl number" of which is 135-5 (parts of caustic potash,
KOH, neutralised by the acetic acid developed by the saponifica-
tion of 1,000 parts of compound ether, Chap, vin.); the corre-
sponding values for the similar compound ethers obtained
from cetylic, cerylic, and myricylic alcohols being respectively
197-5, 128-1, and 116-7.
Another substance closely akin to phytosterol has been isolated
from the seeds of Lupinus luteus, i.e., lupeol* probably indicated
by the formula C26H42O, containing less hydrogen than phyto-
sterol ; this melts at 204°, is dextrorotatory, and forms benzoic
and acetic ethers melting respectively at 250° and 230° ; dissolved
in chloroform and treated with acetic anhydride and sulphuric
acid, it gives a reddish coloration, becoming intensely violet red
on standing. Several other substances of analogous character
appear to be contained in various vegetable products — e.g., hydro-
* Likternik, Berich'.e Deut. Chem. Ge».t 1891, xxiv., pp. 183 and 187.
2
18 OILS, FATS, WAXES, ETC.
carotin (carrots), paracJwlesterol (E 'thulium septicum), &c., &c. ;
but their occurrence in oil-bearing seeds, and the oils thence
obtainable, has not yet been substantiated.
GLYCOLS.
It has been shown by Stiirke * that when carnauba wax is
saponified, and the alcoholiform constituents thus set free frac-
tionated by means of petroleum, a glycol is obtained melting at
103 '5 to 103-8, and giving numbers on analysis agreeing with
( OI-T OTT
the formula C25H52O2, or C23H46 < ^-g2 ' Q-^; this product evolves.
eight hydrogen atoms on fusion with caustic alkalies, forming
an acid of the oxalic series, thus —
(CH9.OH ~ ,TT TT fCO.ONa
H
2346 CHj. OH 2 2346 CO . ONa
just as cerylic alcohol and similar bodies evolve four hydrogen
atoms (p. 13), forming an acid of the stearic series, thus —
C26H53 . CH2 . OH + NaOH = 2H2 + C26H53 . CO . ONa.
CHAPTER III.1J
SAPONIFICATION PRODUCTS OF OILS, FATS,
WAXES, &c.
FATTY ACIDS.
IT is a remarkable fact that all known compound ethers con-
tained in natural fixed oils and fats, &c., invariably give rise on
saponification to monobasic acids only, dibasic acids (like oxalic
acid), and acids of still higher basicity being conspicuous by their
absence from the products thus formed, although in many cases
readily obtainable from these products by simple operations in
the laboratory.
At least six different families of monobasic acids are repre-
sented amongst the saponification products of fixed oils, <fcc., four
of which are included in the general formula, CmH2n +1 . CO . OH;
according as in = n, or = n + 1, n + 2, or 11 + 3, this general
formula represents the following families : —
Formula of Acid.
CmH2m + 1.CO.OH
CmH2m - j . CO . OH
CmH2m _ 3 • CO . OH
CmH2m.5.CO.OH
Family.
Acetic (or stearic) series.
Acrylic (or oleic) series.
Propiolic (or linolic) series.
Linolenic series.
* Annalen der Chemie, pp. 223-2S3 ; also in abstract, Journal Soc. Chem.
Industry, 1884, p. 448.
FATTY ACIDS.
19
Two other families are more highly oxidised, being included in
( OTT
the general formula CmII0ll -j p.. OH> accor^ing as ni = n or
— n + 1 the following two families result : —
CmH
Formula of Acid.
I OH.
CO . OH.
CmH
2m - 2
fOH.
CO . OH.
I Family.
Oxyacetic(oxystearic or glycollic)
series.
Ox3*acrylic (oxyoleic or ricinoleic)
series.
In addition to these six leading families of monobasic acids, re-
presentatives of several others are obtainable by saponification
from various essential oils and allied products ; whilst by gentle
oxidation processes or other reactions several different kinds of
more oxidised monobasic acids are readily formed from the
normal "fatty acids" derived from natural fixed oils, &c. Thus
for example : —
Formula of Acid. Family.
Examples and Sonrces.
( Benzoic and toluic acids, &c. ;
OmH2m _ 7 . CO . OH
Benzoic series
) from gum benzoin, balsam of
j Tolu, dragon's blood, storax,
( oil of bitter almonds, &c.
! Cinnamic acid ; from oil -of
CmH2m - 9 • CO . OH Cinnamic series
cinnamon, cassia, storax,
balsam of Tolu, &c.
r TT /OH
wn2m - 8 -[cO.OH
Oxybenzoic (salicylic)
series
f Salicylic acid ; from gaul-
\ theria oil, &c.
(OH
CmH2m . ! \ OH
Glyceric (dioxystearic)
( Oxidation of oleic acid and
< isomerides and homologues
(CO, OH
series
f thereof.
r H /(OH)S
L^ttsm - 2 | QQ < QH
Erythroglucic (tri-
oxystearic) series
i CigH3(505 ; from oxidation of
< ricinoleic acid and its iso-
/ merides.
c H f(OH)4
Tetroxystearic series
( CigHsgOe (sativic acid) ; from
\ oxidation of liiiolic acid.
CmH2m _ 5 | c^oH Hexoxystearic series
( CigH3608 (linusic acid) ; from
( oxidation of linolenic acid.
ACETIC FAMILY OF FATTY ACIDS.
The following table denotes the leading acids of the acetic
family (general formula CnH2nO2 - CmH2m +1 . CO . OH) derived
from fixed oils, waxes, essential oils, and similar sources : in
addition numerous isomeric modifications of many of the acids
are known, obtained artificially by synthetic and other laboratory
operations : —
20
OILS, FATS, WAXES, ETC.
Formula.
Name of Acid.
Boiling
Point.
Melting
Point.
Source •».
CH202
Formic,
ioi°c
8°C
Ants ; nettles.
C2H402
Acetic, 118°
17°
Acetous fermentation ; oil
of cow parsnep, and
various other essential
oils.
C3H602
Propionic or ; 140°
...
Oxidation of propylic
Tritylic,
alcohol from fermen-
tated fusel oil.
C4H802 Normal Butyric,
162°
— 3°
Cow's butter ; perspira-
Isobutyric,
153°
tion ; oil of cow parsnep.
Oxidation of isobutylic
alcohol from fusel oil ;
Roman chamomile oil.
CsHioOjj
Valeric or Pen-
175°- 185°
...
Several isomerides known.
toic,
Valerian root ; Isova-
leric acid from fat of
Delphinum Phoccena.
C6H12O2
Caproic or 200°
- 9° ; Isohexoic acid (isobutyl-
Hexoic,
acetic acid) from cow's
butter and cokernut
oil.
205°
- 1°'5
Normal hexoic acid, as
octylic ether in oil of
Heracleum.
C7H1402
(Enanthic or
222°
-10°'o
Normal acid by oxidation
Heptoic,
of cenanthol from castor
oil ; wine fusel oil.
CgHiflOg
Caprylic or
238°
15°
Isoprimary acid from
Octoic,
cokernut oil and butter;
Limburg cheese.
C9HJ802
Pelargonic or
254° 13° Normal acid from oil of
Ennoic,
Pelargonium roseum;
and oxidation of oil of
rue and beetroot fusel oil.
Ci0Hvo02
Capric orDecoic,
269° 30°
Butter ; cokernut oil ;
grape fusel oil.
CHH2202
Hendecoic or
Undecylic,
228° at 1 GO; 28° "5
millims. |
Hydrogenatiou of Hende-
cenoic acid from distil-
pressure.
lation of castor oil.
...
35°
Cocinic acid (?) in coker-
nut oil.
j
...
Near 23°
Umbellulic acid (?) from
chaulmoogra oil.
^12^2402 ! Laurie or Dode-
225° at 100
44°
Laurel butter (Laurux
coic,
millims.
nobilis) ; Pichurim bean
pressure.
fat ; cokernut oil ;
palm kernel oil.
Ci3H26O2
Tridecoic,
...
...
Supposed to be contained ,
in cokernut oil ; doubt-
ful.
C14H2802
Myristic,
250° at 100
54°
Nutmeg butter ; coker-
millims.
nut oil ; dika fat ; cro-
pressure.
ton oil; spermaceti.
C15H3002
Pentadecoic,
55°
(?) Oil of Jatropha curcas.
FATTY ACIDS.
21
Formula.
Name of Acid.
Boiling
Point.
Melting
Point.
Sources.
C,6H3002
Pentadecoic,
53° -5
Cetic acid(?) from sper-
^
maceti.
53°
Benomargaric acid (?)
from oil of Ben. Stilli-
stearic acid (?) from
| C16H3202 Palmitic,
271°'o
62°
Stillingia sebifera.
Palm oil. One of the
at 100
constituents of most
millims.
animal fats. Sperma-
pressure.
ceti ; beeswax ; Japan
wax.
C,7H3402
Marcraric,
...
60°
From cetyl cyanide ; for-
merly supposed to be
contained in certain
fats.
Daturic,
...
55°
From oil of Datura
Strammonium.
C18H36Oo
Stearic,
291° at 100
69° "2
Tallow, lard, and most
millims.
animal solid fats ; Shea
C,oH3802
Enneadecoic,
pressure.
66°
butter; Illipe" fat.
From stearyl cyanide (?)
obtained along with
artificial margaric acid.
C2oH4002
Arachic (or Ara-
...
75°
Earthnut oil (Arachis
chidic); Butic,
hypogcea) ; butter (?)
1
(Heintz).
C21H4o02 !
72° -5
Medullic acid (?) from
beef marrow.
C22H4402
Benic or Beni-
76°
Oil of Ben ; black mustard
stearic,
seed oil ; rape oil.
C^H^Og
Lignoceric,
8l°"
Earthnut oil ; beech-
wood tar.
Carnatibic,
72° -5
Carnauba wax.
...
46°
Paraffinic acid (?) from
paraffin wax and nitric
acid.
C25H5002
Hyaenic,
78°
Hyaena fat.
Co6H5202
Geoceric acid (?) from dis-
•
tillation of brown coal.
C27H54Oo
Cerotic,
78°
Beeswax; Carnauba wax;
C28B^02
Chinese wax.
cEnEoi
0
Melissic,
...
88;"
Oxidation of myricylic
alcohol from beeswax.
«<5,
Theobromic,
72""
Cacao butter.
The formulae ascribed to several of the acids named in the pre-
ceding table can hardly be regarded as established with perfect
22 OILS, FATS, WAXES, ETC.
certainty ; thus the cocinic acid, CUH22O2, formerly supposed to
be contained in cokernut oil, appears from later researches to
be in all probability only a mixture of other acids of the series ;
and the same remark applies to the tridecoic acid, C13H20O.2,
from the same source, which appears to be simply a mixture
of lauric and myristic acids. SimilaYly, cetic acid, C]5H30O2,
and the isomeric (?) benomaryaric and stillistearic acids are very
doubtful bodies ; the last has been stated by later observers to
be simply palmitic acid, and benomargaric acid to be a mixture
of palmitic and myristic acids. The margaric- acid, CirH34O2,
formerly regarded as present in animal fats, has been since
shown to consist of a mixture of stearic and palmitic acids
and more or less oleic acid."55" Again, the compositions ascribed
to medullic acid, C01H4.7O9 ; hycenic acid, C05H50O0 ; geoceric
acid, C26H52O2; and tkeobromic acid, C64H128O0,f require con-
firmation as regards the individual character and purity of
these substances. Of those acids where the carbon present
lies between C1(> and C2w, it is noticeable that those of most
frequent and widely-spread occurrence, and of which the com-
positions are ascertained with certainty, always contain an
even number of carbon atoms; so that it has been supposed
by some chemists that acids containing an odd number of
carbon atoms do not actually occur as glycerides amongst the
natural oils and fats, and that the bodies supposed to possess
vsuch a composition are really either mixtures of glycerides with
even numbers of carbon atoms, or substances rendered otherwise
impure. A priori, however, there seems no reason for doubting
the possibility of the existence in nature of glycerides of acids
containing an odd number of carbon atoms.
In the case of butter fat, cokernut oil, and some few other
substances, fatty acids of low molecular weight (i.e., where n in
the general formula CnHnnO2 is of low value), are present to
some notable extent ; but, as a general rule, natural oils and fats
rarely yield fatty acids of this description where n has a smaller
value than 12. Inasmuch as the lower members of the acetic
acid family are comparatively easily volatile (especially along
with water vapour), whilst the higher ones are almost non-
volatile with ordinary steam, this practically means that the
fatty acids from most fats and oils will not readily distil by the
aid of moist steam, whilst a certain proportion of more easily
volatile acids, is< contained in the mixture of acids obtained from
butter fat and cokernut oil, tfec. This distinction is utilised in
certain case& as. a. means of testing the quality of such substances
* The margarine or oleomargarine used as a butter substitute is es-
ssntially a mixture of the glycerides of stearic and palmitic acids with
sufficient olein to give it its soft texture.
t Graf was unable to find any theobromic acid in Cacao butter (Arch.
Pharm., 1888, 26, p. 820).
FATTY ACIDS. 23
as regards adulteration and admixture with cheaper forms of
fatty matter (Reichert's test, vide Chap, vin.)
The fatty acids of the acetic series diifer considerably in their
respective degrees of solubility in water ; the lowest members —
formic, acetic, propionic, and butyric acids — are miscible with
water in all proportions^ the highest members, including myristic
acid and all above it, are quite insoluble in water ; the inter-
mediate acids exhibit a degree of solubility the greater the
lower the molecular weight ; thus caprylic acid dissolves in 400
parts of boiling water, and capric acid in about 1000 parts, both
mostly separating out again on cooling; whilst lauric acid is
almost insoluble in cold water, though sparingly dissolved by
boiling water.
Alcohol, especially when warm, readily dissolves even the
highest members of the series ; inasmuch as the glycerides of
these acids are, as a rule, almost insoluble in alcohol, this pro-
perty affords a method of separating the free fatty acids con-
tained in natural oils, &c., from the glycerides, the oil being
simply agitated with alcohol and allowed to stand so as to
separate the alcoholic solution of fatty acids from the unaffected
glycerides. Alcohol containing only a minute quantity of a free
fatty acid exhibits an acid reaction to phenolphthalein, and can
accordingly be readily titrated volumetrically by means of a
weak standard alkaline solution in presence of that indicator :
on this also is based the general method of determining the
amount of fatty acid salt formed on saponifying a glyceride or
other compound ether by an alkali (Chap, vin.) The highest
acids of the series are not extremely soluble in cold alcohol, so
that they are readily crystallisable from that menstrum.
The normal salts of acids of the acetic family are indicated by
the general formula CnH2n+1 . CO . OM, where M is a monad
metal : acids salts of formula CttHgB.1O2l^ CnH0llO2 can in some
cases be produced — e.g., sodium diacetate, C2H3NaO2, C2H4O2 ;
potassium distearate, C1SH35K00, C18H3602. Salts of this kind
when dissolved in hot alcohol react acid with phenolphthalein,
and behave toward alkaline solutions on titration with that
indicator precisely as mixtures of the free acid and the neutral
salt,
In certain cases the neutral alkali salts are partly hydrolysed
by solution in water with formation of acid salt and caustic
alkali ; thus with neutral sodium stearate.
Neutral Sodium Caustic
Stearate. Water. Soda. Sodium Distearate.
2C18H35Na02 + H20 = NaOH + C18H35Na02, Ci8HS602
By adding common salt to the fluid, the latter compound and
the unaltered neutral salt are thrown out of solution ; on collec-
24 OILS, FATS, WAXES, ETC.
tion by filtration and solution in alcohol and titration an amount
of acidity is registered precisely equivalent to the alkalinity
of the watery fluid. On the occurrence of this phenomenon
depends a good deal of the cleansing properties of soaps, the
action being also observable with the alkali salts of oleic and
ricinoleic acids to approximately the same extent as with those
of palmitic and stearic acids (Chap, xxn.)"
ACRYLIC (OLEIC) FAMILY OF FATTY ACIDS.
The total number of acids of general formula CnH2n_i.CO . OH
now known is somewhat considerable ; as with the acetic
family, only a comparatively small number of them are con-
tained in natural fats, &c., and of these but few are of relatively
low molecular weight so as to be readily volatile. The table 011
page 25 exhibits the more important acids of this class.
As in the case of the acetic family of acids, the existence of
certain members mentioned in the table is not yet established
with perfect certainty ; thus damaluric acid is a substance the
existence of which requires confirmation ; and similarly with
the aldepalmitic acid recently stated by Wanklyn to be a
constituent of cow's butter.* The existence of hypogseic
acid has been denied by Schon, who found the only acid of
the acrylic series present in earthnut oil to be oleic acid.
Similarly, moringic acid has been stated by more recent ex-
perimenters to be simply impure oleic acid; and the same kind
of thing is said by Schadler to apply to doeglic acid this being
regarded by him as simply impure physetoleic acid.
The unsaturated nature of the hydrocarbons from which this
group of fatty acids are derived leads to their possession of some
peculiar features ; thus, when heated with fused alkali (caustic
potash), there is a tendency to undergo a change indicated by
the general equation : —
Cm + nH2(m + n _j,02 + 2KOH = K. CmH^-iOg + K.CuH2n..102 + H2
the potassium salts of two acids of the acetic family being formed
along with free hydrogen. In virtue of this tendency, oleic acid,
when thus treated, forms palmitic and acetic acids, a circumstance
utilised in practical manufacture.
Oleic Acid. Caustic Potash. Potassium Palmitate. Potassium Acetate.
Ci8H3402 + 2KOH = K.C,CH3102 + K.C2H302 + H2
Again, inasmuch as the unsaturated hydrocarbons have a more
or less marked tendency to combine directly with halogens (and
* Journ. Soc. Chem. Ind., Feb. 1891, p. 89.
FATTY ACIDS.
25
so pass into the series of substitution derivatives of the satu-
rated hydrocarbons), the same tendency is shared by the fatty
Formula.
Name of Acid.
Boiling Point
Melting
Point.
Sources.
C3H402
Acrylic,
140°C.
8°C.
Oxidation of acrole'in from
glycerol.
C4H602
Crotonic,
185°
72°
From cyanide of allyl (de-
rived from oil of mustard).
C5H802
Angelic,
185°
45°
Angelica root. Sumbul root
resin.
Tiglic,
196°
64°
Oil of Chamoinile. Croton
oil.
C6H1002
Pyroterebic,
210°
...
Action of heat on terebic acid
from oil of turpentine and
nitric acid.
C7H1202
...
...
53°
Damaluric acid? (from cow's
and horse's urine).
CgHi4Oo
Octenoic,
...
...
...
c9H16o;
Ennenoic,
...
liquid.
(Enanthol (from castor oil)
and acetic anhydride.
Ci0H1802
Phoronic,
Decenoic,
242°-269°
169°
10°-86°
Oxidation of sodium camphor.
Several isomeric modifica-
tions known ; all of arti-
ficial origin.
CnH2002
Hendecenoic,
275°
24° -5
Castor oil distilled under
diminished pressure.
C12H2202
Petroleumic,
Dodecenoic,
250°- 260°
liquid.
Contained in petroleum.
Artificial.
Ci3H2402
Tridecenoic,
...
...
...
Ci4H2602
Tetradecenoic,
...
Moringic,
0°
Oil of Ben.
Cimicic,
...
44°
Fcetid oil from Raphirjaster
punctipennis.
CicH3o02
Physetoleic,
30°
Sperm oil.
Hypogaeic,
...
34°
Earthnut oil(Arachis Itypo-
gcea).
50°
Aldepalmitic acid(?) from
butter.
C17H3202
Heptadecenoic,
.. .
...
Ci8H3402
Oleic,
286° at 100
millims.
14°
Contained as glyceride in
most animal fats and
pressure.
many vegetable oils.
Isoleic,
44°-45°
Distillation of oxystearic
acid.
Stearidic,
...
35°
Action of water on silver
bromostearate.
Cj9H3G02
Doeglic,
A little
Oil from dcegling (bottle-
above 0°
nose whale).
C21H4002
;.'!
'...
'.'.'. ...
C22H4202
Erucic,
254° -5 at
34°
Colza, grape seed, and
10 millims.
mustard oils.
pressure.
26 OILS, FATS, WAXES, ETC.
acids derived from them ; thus the hydrocarbon ethylene, as has
long been known, combines directly with chlorine forming an
oily fluid,* originally known as "Dutch liquid," the reaction
being
Ethylene. Chlorine. Ethylene Bichloride.
H2C = CH2 + C12 = H2C1C - CC1H2
In the same kind of way, oleic acid and its congeners, being
derivatives of ethylene of general formula K . CH = CH . S,
will directly combine with bromine or iodine in parallel fashion,
forming dibromo-, or diiodosubstitution derivatives of acids of
the acetic family of form R . CHBr - CHBr . S ; thus—
Oleic Acid. Iodine. Diiodostearic Acid.
C18H3402 + I2 = CjgHsJjOjj
This reaction is utilised as a convenient method of dis-
tinguishing from one another acids derived respectively from
saturated hydrocarbons, and from unsaturated hydrocar-
bons of the olefine series, the former not combining with
halogens, and the latter uniting therewith in the proportion of
one molecule of fatty acid to two atoms of halogen. Accord-
ingly, the measurement of the quantity of iodine or bromine
thus fixed ("iodine absorption equivalent," or "bromine ab-
sorption equivalent") often gives useful information as to the
nature of the fatty acid or acids present ; and the same remark
equally applies to the glycerides themselves, which also combine
with halogens in parallel fashion, e.g. : —
Olein. Glyceride of Glyceride of Diiodo-
Oleic Acid. Iodine. stearic Acid.
CgJU^CisH-ssO^s + 3I2 = ^3^-5(^13^53^2^2)3
In just the same kind of way certain acids of the acrylic family
can directly combine with nascent hydrogen produced under
appropriate conditions, becoming thereby converted into acids of
the acetic family, the general reaction expressing the change
being —
CnH2n.202 + Ho = CnH2n02
Thus oleic acid forms stearic acid, when heated in a sealed
tube with fuming hydriodic acid and phosphorus. By reversing
the process, an acetic acid becomes transformed into an acrylic
acid. In practice the direct removal of hydrogen after this
fashion is difficult to accomplish ; but in certain cases it may be
effected by acting on the acid of the acetic family with chlorine
or iodine or bromine, so as to produce a monochloro-, iodo-, or
bromosubstitution derivative; by treating this with alkalies, &c.,
* Whence the old name olefiant gas for ethylene, signifying " oil making"
gaa.
FATTY. ACIDS. 27
the elements of HC1, HI, or HBr are eliminated, leaving an acid
of the acrylic series.
Thus acrylic acid itself is formed from iodopropionic acid thus,
lodopropionic Acid. Acrylic Acid.
C3H5I02 - HI = C3H402
the elimination of the elements of hydriodic acid being brought
about by treatment with sodium ethylate, lead oxide, or similar
basic substances.
In other cases a dibromo- or dichlorosubstitution derivative of
an acid of the acetic family is acted upon with zinc dust, or other
substance having a strong tendency to combine with halogens ;
thus dibromopropionic acid and zinc dust form acrylic acid.
Dibromopropionic Acid. Acrylic Acid.
C-jH^BraOo — Br2 = G'sH^Og
In this way the dibrominated and diiodised products obtained
by adding Br.2 or I2 to the higher acrylic acids can be made to
reproduce the original acid. This reaction is utilised in the
examination of oils, &c., containing the glycerides of unsaturated
acids ; bromine addition products are formed and separated from
one another by crystallisation, &c., and then debrominated so as
to reproduce the original acids, which can thus be indirectly
separated from one another in a fashion usually impracticable
with the actual acids themselves.
Acrylic acids, at any rate in certain cases, combine directly
with sulphuric acid, forming saturated compound sulphuric acids
analogous to ethylsulphuric acid (sulphovinic acid) ; thus —
Oleic Acid. Sulphuric Acid. Oxystearosulphuric Acid.
C17H33.CO.OH + S02(OH)2 = CirH
By the action of water, &c., on the compounds thus formed,
hydrolysis is brought about, with the formation of sulphuric acid
and an acid of the oxyacetic (glycollic) family ; thus —
Oxystearosulphuric Acid. Water. Sulphuric Acid. Oxystearic Acid.
Ci;H34- -f H20 = S02(OH)2 + Ci7H34
These reactions, especially the first, are utilised in the pro-
duction of certain kinds of "Turkey red oils;" obviously the
sum of the two changes is equivalent to the addition to an
acrylic acid of the elements of water.
The dibromides of acids of the oleic series, when treated
with silver hydroxide, Ac., form silver bromide together with
glyceric acids — i.e., dioxy acids of the acetic series : —
+ 2AgOH = 2AgBr + CnH.n_
28 OILS, FATS, WAXES, ETC.
By the regulated action of caustic potash, they lose successively
HBr and 2HBr, forming in the one case bromoleic acid or a
homologue thereof, and in the other case a propiolic aqid—
CO. OH HBr = C" Hsn-3 1 CO. OH
£j* QH - t>HBr = Cn H,n_., . CO. OH
A remarkable property possessed by many acids of the oleic
family is that contact with certain reagents, more especially
nitrous acid, converts them into isomeric modifications of higher
fusing and boiling points, so that acids liquid at the ordinary
temperature become transferred into solids. This effect is also
produced with the natural glycerides of these acids, forming
a reaction largely utilised in testing the purity of certain oils
(Chap. vii). Oleic acid, liquid at ordinary temperatures, thus
becomes elaidic acid, melting at 45°, by contact with nitrous
acid ; and its glyceride, olein, fluid at 0°, is similarly converted
into elaidin, melting at 32°; whence the term "Elaidin reaction"
applied to this nitrous acid test. In similar fashion erucic
acid, melting at 34°, is changed into brassaidic or brassic* acid,
fusing at 60° ; whilst parallel changes are undergone by hypo-
gseic and physetoleic acids.
Elaidic acid and the similarly altered other acids of this class
call be distilled unchanged under diminished pressure, not being
thereby converted back again into the original acids ; for a given
pressure the boiling point is always slightly higher than that of
the original acid : thus Krafft and Noerdlinger f obtained the
following numbers. (See Table, p. 29.)
The nature of the chemical change ensuing during the elaidin
reaction is somewhat uncertain. By fusion with caustic potash
both oleic and elaidic acids yield acetate and palmitate ; on the
other hand, by oxidation with alkaline permanganate they form
two different dioxystearic acids, melting respectively at 136° '5
(solidifying at 119°) and 99°-100° (solidifying at S5°-86°— Saytzeff).
Similarly erucic and brassic (brassaidic) acids give rise to two
different dioxybenic acids on oxidation, as well as different
derivatives of other kinds.
* The term " brassic acid " (brasxica .mure) was originally applied to the
acid, C22H42O2, obtained from various species of Brassica, there being at
that time some doubt whether "erucic acid" obtained from other ana-
logous sources was or was not identical therewith. Later on the identity
was established, and the term " brassaidic acid " (brassidin siiure) was
applied to the product of nitrous acid on erucic acid, to indicate its analogy
with elaidic acid (Haussknecht, Annalen der Chem. and Pharm., 1867,
143, p. 55). Of late years the term " brassic acid " has been mostly substi-
tuted in English chemical literature for "brassaidic acid (c. .7., Morley and
Muir's Dictionary of Chemistry, vol. i., p. 631, article Brassic Acid}.
t Berichte der Dent. Chem. Cn<s., 1889, vol. xxii., p. 819.
FATTY ACIDS.
29
Millimetres of
Mercury.
Oleic Acid.
Elaidic Acid.
100
50
30
15
10
285-5—286
264
249-5
232-5
223
287'5—288
266
251-5
234
225
Erucic Acid.
Brassic Acid.
30
15
10
281
264
254-5
282
265
256
From Erucic Acid.
Melts at
Dioxybenic acid, . . 132°- 133°
Dibromide of erucic acid, 42°-43°
Bichloride, . . . 46°
Methylester from dichloride, 30 '5°
From Brassic Acid.
Melts at
Isodioxybenic acid, . 9S°-99°
Dibromide of brassic acid, 54°
Dichloride, . . . 65°
Methylester from dichloride, 42° -5
According to recent researches * the isomerism of erucic and
brassic acids is of the stereochemical order — i.e., the "structures"
of the two bodies, when expressed in space of three dimensions,
are not superposible ; a difference only imperfectly expressible
on a flat surface by the formulae —
CigHsj) — C — H CjgHjjg — C — H
II and ||
H - C - C02H C02H - C - H
Isomerides of Oleic Acid. — Besides elaidic acid (formed
from oleic acid by contact with nitrous acid), two other acids
isomeric with oleic acid are known, viz., isoleic and stearidic
acids ; in addition, other isomerides of the anhydride character
exist.
Isoleic acid is obtained by acting on oleic acid with sulphuric
acid ; combination takes place with the formation of oxystearo-
sulphuric acid (probably two different modifications), thus —
C17H33.CO.OH + H2S04 = C17H34
By hydrolysis the product forms oxystearic acid (again, probably
more than one modification), which on distillation under dimin-
ished pressure becomes dehydrated, furnishing a mixture of ordi-
nary oleic acid and a solid isomeride, isoleic acid.
f* TT JO. oU3U . TT f\ TT O/-V . /~< TT I OJ~I
OH
H20 = H2S04 + C,7
- H20 + CI7H33 . CO . OH
A. Holt, Berichte der Deutsch. Chem. Ges., 1891, vol. xxiv., 4120.
30 OILS, FATS, WAXES, ETC.
By converting the acids into zinc salts and heating with alcohol
a solution is obtained from which zinc isoleate separates on cool-
ing, the other zinc salt remaining in solution. The acid obtained
from the pure zinc salt by decomposition by a mineral acid,
crystallises from ether; it melts at 45°, but is not identical with
elaidic acid which fuses at nearly the same temperature : like
oleic and elaidic acids it forms acetate and palmitate on fusion
with caustic potash ; but the dibromide formed by combination
with bromine when treated with silver hydroxide forms a dioxy-
stearicacid melting at 77°-78° and solidifying at 65°-66°, the same
substance being also formed by oxidising isoleic acid with alka-
line permanganate ; whereas the dioxystearic acids obtained by
oxidising oleic and elaidic acids in the same way melt at 136° '5
and 99°-100°, and solidify at 119° and 85°-86° respectively.*
Isoleic acid combines with hydriodic acid, forming an iodo-
stearic acid reducible to ordinary stearic acid by means of nascent
hydrogen, and reconverted into isoleic acid by alcoholic potash.
The dibromide of isoleic acid similarly reproduces isoleic acid on
treatment with zinc and hydrochloric acid.
Stearidic Acid. — By the action of water on bromostearic acid
(from bromination of stearic acid) Oudemannsf obtained an acid
isomeric with oleic acid, together with silver bromide. This
product distilled unchanged : melting point 35°.
Two anhydrides of oxystearic acids are also known, isomeric
with oleic acid; viz., stearolactone, ^-oxystearic "inner" anhy-
dride (p. 39) ; and the body formed by the action of hydrochloric
acid on a-oxystearic acid, regarded as —
CO.
O. C
PROPIOLTC (LINOLIC) FAMILY OF FATTY ACIDS.
But few members of the family of acids of general formula
CUH2I, _ 3 . CO . OH have been as yet isolated from oils and fats,
&c., the best known example being linolic acid, Cl7H3j . CO . OH^
contained in various drying oils, notably linseed oil ; several
other members, however, have been produced from acids of the
oleic series by employing the method founded on the same
principle as that by means of which oleic acids are obtainable
from acids of the acetic acid series — viz., by conversion into a
chloro- or bromoderivative of an acetic acid and removal of the
elements of HC1 or HBr by the action of a base. Thus oleic
acid combined with Br2 and the product treated with alcoholic
potash furnishes stearolic acid —
* M. C. and A. Saytzeff, /. prakt. Chem., 1888, 37, p. 269.
t«/. prakt. Chemie, 89, p. 193.
FATTY ACIDS. 31
Oleic Acid. Dibromostearic Acid.
C]8H3402 + Br2 C18H34Br202
Dibromostearic Acid. Steai-olic Acid.
C18H34Br202 — 2HBr = C18H3202
In similar fashion other homologues of stearolic acid (e.g., Jiende-
colic, palmitolic, and benolic acids) are obtainable from the corre-
sponding homologues of oleic acid, the general reaction being —
CnH2ll_2Br202 - 2HBr = CuH2n_402
In certain cases propiolic acids may be directly obtained from
acids of the acetic family by treatment with chlorine or bromine,
so as to produce dichloro- or dibromoderivatives of formula
CnH2,, _ 0Br2O2, which are then acted upon with alkalies so as to-
remove the elements of 2HBr, in accordance with the above
equation ; the total change produced being therefore equivalent
to the removal of H4. In this way, for instance, myristic acid,
C14H2SO2, forms myristolic acid, C14H2402.
An analogous result is brought about with rnonochloro- or
monobromoderivatives of acids of the acrylic series by similar
treatment, the elements of HC1 or HBr being removed, thus —
- HC1 = CuH2n.402
CuHon_3Br02 - HBr = CuH2n-4O2
For instance, chlorocrotonic acid, C4H5C102, gives rise by this
treatment to tetrolic acid, C4H4O2.
The table on p. 32 includes the chief acids of this series: —
Just as one molecule of an acrylic acid will combine with I2 or
Br0, so will one of a propiolic acid unite with Br4 or I4, this action
being substantially the reverse of that above described, where a
dibromoacetic acid loses 2 HBr and becomes a propiolic acid; this;
reaction is utilised in the practical testing of oils (Chap, viu.)
Conversely, by the action of nascent hydrogen, zinc dust, and
similar dechlorinising agents, the tetrabrominated or tetra-
iodised bodies thus formed become again reduced to the original
propiolic acids ; thus linolic acid can be separated from accompany-
ing acids (obtained by saponifying the mixture of glycerides con-
tained in linseed oil, <fec.) by combining with bromine, separating
by crystallisation the tetrabrominated derivative, C18H32Br4O2
(melting at 114°-115°), and reproducing linolic acid by removing
the bromine.
Tetrabromostearic Acid. Linolic Acid.
C18H32Br402 - Br4 = C18H3202
Those propiolic acids that are formed by the bromine reaction
above described (loss of 2HBr from dibromoderivatives of acids
of the acetic family) possess the power of directly combining
with oxygen (from suitable oxidising agents), forming saturated
32
OILS, FATS, WAXES, ETC.
Formula.
Name of Acid.
Melting
Point.
Boilinc
Point.
Sources.
C3H202
Propiolic,
Chloropropiolic acid,
C3HC102, is formed
.
by the action of pot- ;
ash on dichloracrylic
acid, C3H2CL02.
C4H202
Tetrolic,
76-5°
203°
Chlorocrotonic acid and
caustic potash.
C5H602
Pentolic,
...
...
...
C6H802
Sorbic,
Liquid
221° )
at 15°
Mountain ash berries.
Parasorbic,
134-5°
... )
C7H1002
Benzoleic(Hy-
Liquid
Hydrogenation of ben-
drobenzoic),
zoic acid.
C8H1202
Diallyl acetic,
Liquid
227°
Artificial.
cM,
Camphic,
...
...
Formed together with
borneol by heating
camphor with alco-
holic soda.
Campholenic,
...
Near
Dibromcamphor and
CnHjsO,
Hendecolic
59° -5
260°
sodium amalgam.
From undecylenic
(Undecolic or
(hendecenoic) acid
Hendecinoic),
by bromine reaction.
C12H2002
...
...
...
...
CnH^Oo
Myristolic,
12°"
...
From myristic acid
by chlorination and
action of alcoholic
potash.
C^HssOj
Palmitolic,
42°"
From hypogeeic acid
by bromine reaction.
C17H3002
Elceomargaric,
48°
... /
" Wood oil " from
Eloeostearic,
71°
... \
Elceococca Vernitia.
Cj8H3<>02
Stearolic,
48°
...
From oleic acid by
bromine reaction.
Linolic,
Fluid
...
Linseed and other dry-
ing oils.
Ricilinolic,
Fluid
...
Dehydration of ricin-
oleic acid.
Tariric,
50° -5
...
Seeds of tariri (genus
Picramnia).
CgoHgeO*
... '...
Fluid
(?) Higher homologue
of linolic acid, sup-
posed to be con-
tained in some drying
oils.
c!2H4oOa
Behenolic (or
5T-5
...
From erucic acid, by
Benolic),
bromine reaction.
FATTY ACIDS. 33
compounds by the addition of two oxygen atoms instead of four
bromine atoms, thus—
Propiolic Acid. Saturated Compounds.
CnH2n-3' CO . OH + Br4 = Cii H2n -3
( =0
CnH2u_3.CO.OH + 0, = CuH2a_3 =0
( -CO. OH
In this way stearolic acid, C18H32O2, forms stearoxylic acid,
C18H32O4 ; and similarly with palmitolic and benolic acids.
The general character of the action is indicated by the equation :
R . CH-CH . S . CH=CH . T + 02=R . CH-CH . S . CH-CH . T
Linolic Acid. — The earlier researches on the acids derivable
from the chief glycerides contained in linseed and other drying
oils led to the conclusion that they were identical, and indicated
by the formula C10H28O2, and to this body the name linoleic
acid was applied ; but later experiments have shown conclusively
that a considerably higher molecular weight is possessed by the
acid obtained from linseed oil, and have rendered it not impro-
bable that different homologous acids exist (related as myristic,
palmitic, and stearic acids, for example), and that different
drying oils are not always identical as regards the leading acid
of this series present. Linolic acid was originally obtained by
Schiller by saponifying linseed oil with caustic soda, salting out,
dissolving in water, and precipitating with calcium chloride.
The precipitate was treated with ether, whereby calcium lino-
late was dissolved out, leaving other substances undissolved ;
by agitating the ethereal solution with hydrochloric acid, and
evaporating at a low temperature in an atmosphere of hydrogen,
crude linolic acid was obtained. This was purified by treat-
ment with alcoholic ammonia, precipitating as barium salt,
and regenerating the acid as before. The analysis of the acid
and its salts by Schiller, and subsequent investigators, led to
the formula C1(.(H08O2.
On the other hand, the Koettstorfer values (Chap, viu.) for lin-
seed oil and other drying oils obtained by most of the later experi-
menters lead to the conclusion that the mean molecular weight of
the fatty acids contained therein, is sensibly higher than 252,
the value corresponding with C16H28O2 ; the saponification
equivalents for linseed, poppy, and hemp oils thus deduced
mostly lie between 285 and 300, giving an average of 293 or
thereabouts for the glycerides, and consequently of about 280
for the fatty acids thence derivable (C1SH32O2 = 280). Further,
various later analyses of linolates and other derivatives corro-
3
34 OILS, FATS, WAXES, ETC.
borate this formula; whilst Peters* obtained stearic acid (of
melting point 69°) by acting on linolic acid with strong hydriodic
acid and phosphorus, so as to hydrogenise it.
Still higher molecular weights result from the observations of
some chemists. Thus A. H. Allen f found that whilst the linolic
acids isolated from several different samples of linseed oil pos-
sessed mean equivalent weights varying between 282 and 295,
another specimen, prepared with great care in an atmosphere of
coal-gas, gave 307 -2 (C2pH3602 = 308). Norton and Eichardson %
found that linolic acid from linseed oil, when distilled at
about 290° under a pressure of 89 mm., gave a colourless
distillate, constituting about three-quarters of the whole ; this
was capable of being redistilled unchanged. It consisted of
15°
an acid of specific gravity -9108 at -— giving numbers on
analysis corresponding with the formula C20H36O2 ; the vapour
density was found to be 153, this formula representing 154.
Moreover, on heating with hydriodic acid it did not form stearic
acid, melting at 69°, as in the case of Peter's product, but an
acid of considerably higher melting point — 83° (arachic acid,
C20H40O2, melts at 75°).
Reformatsky§ on repeating the experiments of Schuler, obtained
from linseed oil freshly expressed in the laboratory a crude
linolic acid that did not distil unchanged at 292° under 100 mm.
pressure. It contained a considerable amount of oleic acid,
yielding dioxystearic acid on oxidation with permanganate ; by
heating with alcohol and gaseous hydrochloric acid, ethyl linolate
was ultimately obtained, distilling at 270-275 under 180 mm.
pressure ; from this by saponification linolic acid was regener-
ated in a state of comparative purity ; e.g., giving the iodine
number 172-65 to 180-3, that calculated being 181-4. When
dissolved in glacial acetic acid the product thus prepared formed
two compounds on addition of bromine — viz., a tetrabromide
(addition product), C18H3200Br4, as a viscid oil ; and a crystallis-
able hexabrominated substance, regarded by him as a bromosub-
stitution derivative of the tetrabromide, C18H30O2Br6, melting at
177°-178° and solidifying at 175°. Oxidation with alkaline per-
manganate yielded tetroxystearic (sativic) acid and a little azelaic
acid.
Whilst it appears exceedingly probable from the preceding re-
sults that more than one homologous acid of the series CnH2n_ 4O^
exists in ordinary drying oils, it is more than doubtful whether
any single substance in a state of purity was examined by
* Monatsh. f. Chemie, 1886, 7, p. 552.
t Commercial Organic Analysis, vol. ii., 1886, p. 117.
J Berichte (L Deut. Chem. Ges., 1887, xx., p. 2735.
§Journ. Soc. Chem. Industry, 1890, p. 744 : from /. prakt. Chem., 1890,
41, p. 529.
FATTY ACIDS. 35
any of the various observers, inasmuch as purification by
recrystallisatioii of a well marked crystalline derivative was
not found readily practicable. On the other hand, Hazura and
Griissner obtained from hemp seed oil* a mixture of fatty
acids which on solution in acetic acid and treatment with
bromine gave more than one brominated product of crystal-
lisable character, as well as iioncrystalline ones. One of the
crystallisable products was found to melt at 177°-178°, and
to have the composition 018H30O2Br6 ; another melted at
114°-115°, and had the composition C18H32O2Br4; from this latter
by the action of zinc and alcoholic hydrochloric acid the bromine
was removed, producing linolic acid, C18H.>9O.7, free from ad-
mixture with other acids. It was found impracticable to bromi-
nate the bromine compound, C18H3.2O2Br4, so as to obtain from it
any substitution derivative, C3 8H30O2Br(3 ; whence it appears that
the hexabrominated body, melting at 177°-178°, was not formed
by the further substitutive action of bromine on the tetrabromi-
nated addition product (as supposed by Reformatsky), but must
have been produced by the direct combination of Br6 with an
acid, C18H<]0O0, contained along with linolic acid, &c., in the
original mixture ; this acid, linolenic acid, is in fact easily repro-
duced from the hexabromicle by treatment with zinc and alco-
holic hydrochloric acid so as to remove the bromine (p. 27) ;
conversely, it is again converted into the original hexabromide
by direct combination with Br6.
The linolic acid thus obtained from the tetrabromide of fusing
point 114°-115°, C18H32O2Br4, reproduced that substance by
combination with bromine ; and similarly combined with I4,
but did not form a hexabrominated derivative ; on oxida-
tion with alkaline permanganate it formed a tetroxystearic
acid, sativic acid, 018H3G0G == CirH'31 I £,Q ^jj , together with
a little azelaic acid and other secondary products, but no linusic
acid (p. 37). Sativic acid fuses at 170° ;f on heating with
hydriodic acid and phosphorus, it forms an iodised acid, reduced
to stearic acid by means of zinc and hydrochloric acid ; it dis-
solves in 1000 parts of boiling water, and is readily soluble in
alcohol, but is insoluble in cold water and in ether; by acety-
lation it forms a tetracetyl derivative, C17H31 < £,Q j^j| '4;
hence it obviously possesses the constitution of a quadruply
hydroxylated stearic acid. On further oxidation it does not form
linusic acid, but produces azelaic acid, C*-H14(CO . OH)2.
Isomerides of Linolic Acid. — Stea/rolic acid, obtained by
combination of oleic acid with Br2, and removing the elements of
* Journal Soc. Clie.m. Industry, 1888, p. 506 : from MonatsJi. d. Chemie>
ix..p. 180.
t According to earlier observations, at 160°-162°.
36 OILS, FATS, WAXES, ETC.
2HBr from the product, fuses at 48°. By oxidation with alka-
line permanganate, this forms stearoxylic acid, C18H82O4> melting
at 84°-86°, together with some suberic acid, C6H"12(CO.OH)2,
produced by the further oxidation of the stearoxylic acid first
formed (Hazura). Nitric acid also directly oxidises it to stear-
oxylic acid, with formation also of azelaic acid, C7H14(CO.OH)2
(Overbeck), and of pelargonic (ennoic) acid (Limpach).
Tariric Acid. — A. Arnaud has recently described* an acid
isomeric with linolic acid contained as triglyceride in the
seeds of " tariri," a shrub common in Guatemala ; it melts at
50° '5 C., and unites with bromine, forming a tetrabromide,
C18H32Br4O2, melting at 125°.
Ricilinolic Acid. — This name may be conveniently applied to
the acid obtained by Krafft,f by heating ricinoleic acid under
diminished pressure (15 mm.), when an acid distilled, liquid at
ordinary temperature, but solidifying on chilling ; this boiled at
230° at 15 mm. ; and gave numbers indicating that it was an
isomeride of linolic acid,! produced by the dehydration of
ricinoleic acid, which might be expected a priori to take
place, thus —
Ricinoleic Acid. Dehydrated Derivative.
C1'H^ H2° + C17HSi.CO.OH
LINOLENIC FAMILY OF FATTY ACIDS.
The existence in drying oils of two isomeric acids of formula
CnH.2n_5.CO.OH (where n= 17) in the form of glycerides has been
rendered extremely probable, if not conclusively substantiated,
by Hazura and various collaborateurs. When the fatty acids
isolated from such oils — e.g., hempseed or linseed oil — are dis-
solved in acetic acid, at least three different brominated
compounds are obtainable by the addition of bromine — viz.,
crystallisable linolic acid tetrabromide, C18H32O2Br4, melting
at 114°-115°, and the crystallisable hexabromide, C18H30OoBr6,
melting at 177°-178° above described (p. 35), together with a non-
crystallisable liquid bromide, apparently containing an isomeric
hexabromide, 018H80O2Br6. As already stated, the crystallisable
hexabromide loses Br6 by the action of zinc and alcoholic hydro-
chloric acid, forming linolenic acid, C18H30O9, from which the
same hexabromide can be reproduced by bromination ; by
oxidation with alkaline permanganate no sativic acid is pro-
* Comptes rendus, 114, p. 79.
t Eerichte d. Deut. Chcm. Ges., 1888, p. 2730.
+ By heating ricinoleic acid in vacno, Norton and Richardson obtained an
acid closely resembling linolic acid, regarded by them as C2oH3C02 (Bcrichte
d. Deut. Chem. Ges., 1887, xx. p. 2735).
FATTY ACIDS. 37
duced, but, instead, linusic acid, a hexoxystearic acid,
C17H29 | (^Q1^. This last melts at 203°-205°, and furnishes a
hexacetyl derivative, C17H29 j '^Q ^j| '6. Hence the pre- exist-
ence of linolenic acid in the original mixture of acids, as
the source of the crystallisable hexabromide, would seem to be
pretty clearly demonstrated.
The existence of an isomeric modification of linolenic acid,
isolinolenic acid, is inferred from the fact of a noncrystalline hexa-
bromide being apparently produced by the addition of bromine
to the original mixed acids, together with the circumstance
that on oxidising the mixture by alkaline permanganate there
are formed (in various relative proportions, according to the
kind of drying oil operated on) not only dioxystearic acid (due
to oleic acid contained), sativic acid (tetroxystearic acid, due
to linolic acid, C18H32O9), and linusic acid (due to linolenic acid),
but also another hexahydroxylated stearic acid, isolinusic acid,
isomeric with linusic acid; this melts at 173°-175°, and furnishes
a hexacetyl derivative, C17H.,9 < ^pA jL,4 , resembling that
obtained from linusic acid, but less soluble in ether.
OXYACETIC (GLYCOLLIC) FAMILY OF FATTY
ACIDS.
The members of this family (general formula, CmH2in < QQ OH/
hitherto recognised as normal constituents of fats, oils, waxes,
£c., are but few in number. Carnauba wax has been found by
Stiircke * to contain a small quantity of a substance simultane-
ously possessing the properties of an alcohol and an acid, indi-
f OTT OTT
cated by the formula C19H38 ] QQ 2 j) JT ; when this is heated
with soda lime, it forms an acid of the oxalic family with evolu-
tion of hydrogen.
CHo.OH , ov ^TT n TT fCO.ONa . OTT TT n
- ^
The essential oil of Angelica Arcliangelica contains (probably
as some form of compound ether) an acid which appears to be
( OTT
oxymyristic acid,\ C13H26 \ ^ OH, fusing at 51°, and yielding
( O f TT O
a benzoyl oxymyristic acid C13H26 < ^A 5^j| , fusing at near
* Annahn der Chemie., 223, p. 283; also Journal Soc. Chem. Industry,
1884, p. 448.
t R. Muller, JBerichte Deut. Chem. Ges., 1881, vol. xiv., p. 2476.
38 OILS, FATS, WAXES, ETC.
68°. An oxymyristic acid apparently identical with this is
obtainable from myristic acid by brominating and treating the
resulting monobromomyristic acid with caustic soda.
By similar processes palmitic acid yields oxypalmitic acid and
stearic acid, oxystearic acid. Of this latter body, moreover, more
than one isomeric modification is known ; thus M. C. & A. Say-
tzeff found * that a-oxy stearic acid is obtained when isoleic acid
(m.p. 45°) is combined with hydriodic acid so as to form an
iodostearic acid, and the product treated with silver hydroxide ;
while fi-oxystearic acid is similarly obtained from ordinary oleic
acid ; the reaction in each case being expressed by the equations
Oleic Acid. Iodostearic Acid.
Ci8H3402 + HI CI8H35IOo
Iodostearic Acid. Oxysteavic Acid.
C18H35I02 + AgOH = Agl + C18H3a(OH)02
a-oxystearic acid melts at 80°-82° and distils unchanged ;
Avhilst /3-oxystearic acid breaks up on heating into water and
ordinary oleic acid —
Oxystearic Acid. Oleic Acid.
C1SH35(OH)02 = H2O + CJ8H3402
The same two acids are also obtainable by treating isoleic acid
with sulphuric acid, when combination takes place as the forma-
tion of two isomeric oxystearosulphuric acids, which by the
hydrolytic action of water are decomposed into sulphuric acid
and oxystearic acids, thus —
Sulphuric Oxystearo-
Isoleic Acid. Acid. sulphuric Acid.
C17HS3.CO.OH + H2S04 = GirH
Oxystearo- Oxystearic Sulphuric
sulphuric Acid. Water. Acid. Acid.
Ci7H34k 3 + H20 = Ci7H34 + H2S04
the two reactions jointly are consequently tantamount to the
addition of water 611 to isoleic acid —
Isoleic Acid. Oxystearic Acid.
r TI PIT PIT rr» ryprj-TT f\\ = Ci5H31 -CH2~CH.OH -CO. OH
C15M31-CH lioUj _Cl5H31-CH.OH-CH2-CO.OH
The a or the (3 acid thus results according as the hydroxyl group
becomes added to the penultimate or antepenultimate carbon.
Geitel finds t that when ordinary oleic acid is thus treated
* Jahresbericht, 1888, p. 1916 : from Journal pr. Chemie, [2] 37, p. 269.
t Journal Soc. C/iem. Industry, 1888, p. 218 ; from Journal f. prakt.
Chemie, [2] 37, p. 53.
FATTY ACIDS. 39
with sulphuric acid, besides the a-oxystearic acids above described
a y-oxystearic acid, C14H2g - . CH . OH - CH2 - CH2 - CO . OH,
is produced, which readily forms an " inner " anhydride, stearo-
lactone, CUH29 - CH - CH2 - CH2 - CO. This anhydride is
produced whenever a salt of y-oxystearic acid is decomposed by
.a mineral acid ; if the acid solution be cautiously neutralised in
the cold by an alkali, the stearolactone remains unaltered, and
may be obtained by dissolving out with ether or benzoline,
and thus separated from any other accompanying fatty acids
set free by the mineral acid, but retained by the subsequent
addition of alkali. When boiled with alcoholic potash, however,
potassium /-oxystearate is produced.
Stearolactone. Potassium Oxystearate.
C17H34J~ I + HOK + C17H34|°**
Processes for detecting and estimating stearolactone in mix-
ture with free fatty acids, &c., are founded on these reactions.
Stearolactone is readily soluble in alcohol, ether, and light
petroleum spirit; it crystallises in needles melting at 51°; it
is formed in somewhat large quantity when oleic acid is heated
with zinc chloride and the product treated with water (Benedikt),
probably by reactions analogous to those taking place under the
influence of sulphuric acid (vide Chap, vn.)
An anhydride isomeric with stearolactone is derived from
a-oxystearic acid by the action of hydrochloric acid thereon (C.
and A. Saytzeff) in accordance with the equation —
OP TT f OH OTJ n r< TT f CO • 0 1 /-i TT
2C17H34 | CQ QH 2H20 + C17H34 | Q co | C17H34
This substance is fluid at the ordinary temperature and does not
solidify 011 chilling ; it combines with neither bromine nor iodine
(Hiibl's reagent), but on heating with caustic potash becomes
wholly converted into potassium oxystearate ; on acidifying the
product a-oxystearic acid is set free, and not. an anhydride, as
in the case of stearolactone.
OXYACRYLIC (KICINOLEIC) FAMILY OF
FATTY ACIDS.
f
The acids of general formula CmH2m_2-! QQ QJJ obtained by
the sapoiiification of fixed oils, &c., are not very numerous,
{ OH
ricinoleic acid, CirH32 \ ^Q OH , being the only one as yet known
40 OILS, FATS, WAXES, ETC.
with certainty ; castor oil, and to a lesser extent some other oils,
contain ricinolein, the glyceride of ricinoleic acid. To isolate
the acid, castor oil is saponified with concentrated caustic potash
solution, and the resulting soap decomposed by heating for a
short time with hydrochloric acid ; the separated acids are
washed with water several times, and then cooled to 0°, or some-
what lower ; the mass solidifies and is subjected to pressure,
first gentle then stronger, so as to squeeze out liquid matters,
the temperature being gradually raised to 10°- 12°. If any con-
siderable quantity of unsaponified oil is mixed with the free fatty
acids, their solidification by chilling is greatly hindered, a result
also brought about by the presence of bye -products formed by the
action of the air on the free fatty acids ; wherefore the saponify-
ing and decomposing operations, <kc., should be conducted as
rapidly as possible. Thus purified ricinoleic acid fuses at
16°-17°, the phenomenon of superfusion being strongly shown
by the liquid acid, which usually does not solidify again until
considerably chilled.
When castor oil is heated, the ricinoleic acid present therein
as glyceride breaks up into oenanthol and hendecenoic acid,
thus —
iiicinoleic Acid. (Enanthol. Hendecenoic Acid.
<-1i8H3403 = C7H]40 + CnH2002
Free ricinoleic acid, however, when heated does not split up in
this way at all, neither does it distil unchanged even under
greatly diminished pressure — below 15° rnm. An acid distillate
passes over at about 250°, which on rectification furnishes aiiacid
boiling at about 230° at 15 mm. ; and giving numbers correspond-
ing with the formula C]8H32O2 (p. 36), whence it would seem that
water is thus split off from ricinoleic acid yielding a linolic acid
isomeride. Hydriodic acid and phosphorus convert ricinoleic acid
into stearic acid ; heating with caustic potash forms a secondary
decylic alcohol, C10H21 (OH), and sebacic acid, C8H16 (CO.OH)2,
from which reactions the structure would seem probable
CH3 - (OH2)5 - CH . OH - CH = OH - (CH2)S - CO . OH. Alka-
line permanganate oxidises ricinoleic acid to trioxystearic acid
(Dieff and Reformatsky).
By the action of nitrous acid ricinoleic acid is converted into
ricinelaidic acid melting at 52°-53° ; on heating under diminished
pressure, this is decomposed much more slowly than ricinoleic
acid. Oxidation by means of nitric acid readily converts it
into normal heptoic acid, whilst alkaline permanganate forms
trioxystearic acid. According to Hazura and Griissner,
two different trioxystearic acids are formed when ricin-
oleic acid is thus oxidised, respectively melting at 140°-142°
(trioxystearic acid), and at 110°-111° (isotrioxy stearic acid); from
which they infer the presence in castor oil of two isomeric acids
FATTY ACIDS. 41
(ricinoleic and isorlcinoleic acids respectively). Both of these
trioxy acids form triacetyl derivatives, ClTH.j:, S QQ ()H3 >
and both are reducible to ordinary stearic acid by means of
hydriodic acid ; the latter is present to the extent of about twice
as much as the former.
Isomerid.es of Ricinoleic Acid. — On heating barium ricin-
oleate Krafft obtained a residue from which an acid termed by him
ricinic acid was isolated,* apparently isomeric with ricinoleic
acid; this melted at 81°, and distilled unchanged at 250°-252°
under 15 mm. pressure ; by oxidation it yielded normal heptok?
acid.
Rapic Acid. — Reimer and Will have obtained from colza oil a
liquid acid, C1SH34O3, differing considerably from ricinoleic acidr
especially in not forming a solid elaidic acid with nitrous acidf
and in not yielding sebacic acid on fusion with potash. This is
isolated by means of the zinc salt which is soluble in ether,
whereas zinc erucate is insoluble therein. ; by decomposing the
recrystallised salt (melting at 78°) by tartaric acid, and well
Avashing with water, rapic acid is obtained as a fluid mass, not
solidifying even when considerably chilled.
Oxyoleic Acid. — When the dibromide of oleicacid (dibromo-
stearic acid) is treated with silver hydroxide it forms oxyoleie
acid, apparently in consequence of the removal of the elements of
HBr, forming bromoleic acid, and the action thereon of silver
hydroxide, thus —
Eromoleic Acid. Oxyoleic Acid.
C17H,2Br.CO.OH + AgOH = AgBr + C17H
The same product results by first converting the dibromide
into bromoleic acid by means of potash and then acting upon
this with silver hydroxide (Overbeck). Oxyoleic acid is a thick
liquid at ordinary temperatures but solidifies on chilling ; by
boiling with caustic potash it takes up water, forming a dioxy-
stearic acid, melting at 126°. J
r TT /OH p „ /(OH)2
Li7M32|co OH Ll7H33lCO.OH
{OH
C1O OH ' *S
formed when the dibromide of hypogaeic acid is treated with
silver hydroxide (Schroder) ; as with oleic dibromide, the action
probably takes place in two stages, the elements of HBr being
* Berichte d. Deut. Chem. Ges., 1888, vol. xxi., p. 2730.
t Berkhte d. Deul. Chem. Ges., 1887, vol. xx., p. 2385.
l^ Later experiments by Saytzeff indicate that this acid is identical with
the dioxystearic acid melting at 136'5, obtained by him by oxidation of
oleic acid by alkaline permanganate (p. 30).
42 OILS, FATS, WAXES, ETC.
first removed, forming bromohypogseic acid, C1GH20Br02, and this
being then converted into the oxyacid, thus —
Cl5H28Br . CO . OH + AgOH = AgBr + ClfiH28{cO.OH
It melts at 34°, and by boiling with caustic potash solution
takes up the elements of water forming dioxypalmitic acid,
usin at 115°'
When oleic acid is heated to 200° and a stream of air blown
through (as in the preparation of " blown oils," it absorbs
oxygen and becomes largely converted into an oxyoleic acid
(Benedikt and Ulzer). The relationships of the oxidised oleins
and similar substances contained in blown oils to ricinoleic
glyceride (castor oil) have not been fully studied, but appa-
rently there is a considerable degree of similarity between
them. The same remark applies to the oxidised acids formed
when oils and fats are kept for long periods of time, so as to
.absorb oxygen largely from the air spontaneously. On the
other hand, when drying oils are exposed to the air in thin
films, so as to " dry " up to solid varnishes, they absorb oxygen ;
when the absorption attains its maximum, the increment in
weight is tolerably close to that corresponding with the weight
of iodine capable of being taken up by the original oil,
whilst the capacity for absorbing iodine decreases pari passu
with the oxidation. It would, therefore, seem that the tendency
of atmospheric oxidation of drying oils is to produce less " un-
saturated " oxidation products than the original substances ;
whence by analogy in the case of oleic glyceride, it would
seem probable that saturated acids are formed thus, rather
than uiisaturated acids like oxyoleic acid. A product has been
recently introduced into the market under the name of " oxy-
oleate," for use as a " Turkey red oil," obtained by the action
•of sulphuric acid on certain oils, and decomposition of the
•compound sulphuric acid formed by heat (vide Chap, vn.) The
precise chemical nature of this substance does not seem to
have been closely investigated as yet; presumably it chiefly
consists of an oxystearic, rather than an oxyoleic acid, since
by hydrolysis the former and not the latter results from the
sulphuric acid compound of oleic acid (supra, p. 38).
AnUydrodioxystearic Acid. — When dioxystearic acid (melting
point 136°-5) is distilled under diminished pressure (100 to
180 mm.) it breaks up into water, and a monobasic acid, isomeric
with ricinoleic acid, melting at 77°-79°, and solidifying at
66°-69°.* From its mode of formation this product is obviously
f -= O
indicated by the formula, C^Hgg •! _ /-JQ QJT > being a saturated
-compound, not containing alcoholiform hydroxyl like ricinoleic acid.
* A. Saytzeff, /. prakt. Chem. [2], vol. xxxiii., p. 300.
FATTY ACIDS.
43
It is not improbable that the rapic acid above mentioned
has an analogous constitution, since the low acetyl number pos-
sessed by colza oil renders it unlikely that any large quantity
of a glyceride of a hydroxylated acid is present therein (Chap, vin.)
POLYHYDEOXYLATED STEAKIO ACIDS.
A number of acids are known, related to stearic acid in that
they are derived therefrom by the replacement of two or more
hydrogen atoms by hydroxyl groups — i.e., by a further continu-
ance of the action by means of which oxystearic acids may be
regarded as derived from stearic acid. These polyhydroxylated
derivatives are all expressed by the general formula,
CirE35_n(OH)n.CO.OH
When 11 = 1, some modification of oxystearic acid results ; when
n = 2, a dioxystearic acid (higher homologue of glyceric acid) ;
similarly, when n = 3, 4, or 6, trioxy-, tetroxy, and hexoxy-
stearic acids respectively result.
The following table gives the principal sources and melting
points of these acids, the usual mode of production being gentle
oxidation of the acid serving as source with alkaline perman-
ganate : — *
Name.
Formula.
Source.
Melting
Point.
Solidifying
Point.
Dioxystearic acid,
Ci7H33(OH)2.CO.OH,
Oleic acid,
136° -5
119°- 122°
Isodioxy stearic acid,
Do.,
Elaidic acid,
99°- 100°
85°-86°
Do.,
Do.,
Isoleic acid,
77°-78°
64°-66°
Trioxystearic acid,
C17H32(OH)3.CO.OH,
Castor oil,
140°- 142°
...
Isotrioxystearic \
acid, J
Do.,
Do.,
110°-1110
...
/3-isotrioxysteario 1
acid, J
Do., {
Eicinelaidic
acid,
114°- 115°
...
Sativic acid )
(Tetroxystearic >
Cl7H3l(OH)4.CO.OH,
Linolic acid,
173°
...
acid), )
Linusic acid j
(Hexoxystearic >
C17H2o(OH)4.CO.OH,
Linolenic acid,
203°-205°
...
acid), . . )
Hemp seed »
Isolinusic acid i
oil, &c., J
(Isohexoxy-
stearic acid), )
Do.,
(supposed
isolinolenic \
acid),
173°-17C°
...
i
* A dioxystearic acid (melting point 136°) is also obtainable in small
quantity by the action of silver hydroxide on the dibromide of oleic acid
(p. 30); also by the hydration of oxyoleic acid (p. 41). Oxyhypog;eic acid
44 OILS, FATS, WAXES, ETC.
A remarkable rule is uniformly followed in all cases where
unsaturated fatty acids are thus oxidised — viz., that a number
of hydroxyl groups is always taken up sufficient to form a satu-
rated polyoxy acid.* Thus in the case of the oxystearic acids,
unsaturated acids of form C17H33.CO:OH (oleic, isoleic, and
elaidic acids), take up two hydroxyl groups forming three dif-
ferent dioxystearic acids, C17Ho3 < /s/-^ OTT '> similarly ricinoleic
( OTT
and riciiielaidic acids of form C17H.J2 < ^^ ~TT take up 2 hy-
droxyl groups, producing two trioxystearic acids, C17H32 < LQ Q\T.
In the same wray hendecenoic, hypogseic, and erucic acids take up
2 hydroxyl groups giving rise to dioxyhendecoic, dioxypalmitic,
and dioxybenic acids respectively. On the other hand, linolic
acid, C-l7H31 . CO . OH, takes up 4 hydroxyl groups, producing
sativic (tetroxystearic) acid, C17H.U < X/-\ ATT ', whilst linolenic
acid, Cl7H09 . CO . OH, takes up 6 groups, producing liimsic
(hexoxystearic) acid, C17IL0 <
The above rule appears to be only a particular case of a con-
siderably wider principle applying also to hydrocarbons and
alcohols, etc., of unsaturated character, which may be put in the
form of the following theorem : — -
With substances containing the group — CH = CH — (or cer-
tain groups thence derived, - OR = CH, - and — CR = CS — ,
where R and S are monad alkyl radicles), the effect of oxidising
agents of not too energetic a character is to cause the addition of tico
hydroxyl radicles so as to form the group - CH. OH - CH. OH -
(or the derived group - CR.OH - CS.OH - ), this action
occurring twice over if two groups — CH = CH — are present,
thrice over if three groups are present, and so on.
Thus Wagner has found * that olefmes are readily transformed
into glycols by means of potassium permanganate in virtue of
this reaction; alcohols of unsaturated character (allylic series)
similarly become glycerols ; hydrocarbons containing the group
— CH = CH - twice (e.g., diallyl) become erythrols, and so on.
Glycerol itself is thus obtainable from allylic alcohol.
(from dibromide of hypogseic acid) behaves similarly, forming a dioxy-
palmitic acid, melting point 115°. A dioxypalmitic acid was obtained by
Groger (inter alia) by the direct oxidation of palmitic acid with alkaline
permanganate. Two dioxybenic odds are known, respectively derived
from the dibromides of erucic and brassic acids (p. 29), and melting at
132°- 133° and 9S°-99°.
* Hazura & Griissner, Journal Soc. Chem. Industry, 1888, p. 506; from
Monatsh. Chem., vol. ix., p. 180.
t Berichte. d. Dent. Chem. Ges., 1888, 21, pp. 1230 and 3343.
FATTY ACIDS. 45
111 all probability the first action taking place is the direct com-
bination of oxygen in the same way as the combination of bro-
mine or iodine, thereby forming a substance containing the group
— CH — CE — CRX
O, or the derived groups | j>O or I/O;
— CH — CH/ — C8
this product then assimilating water whilst nascent.
Tims, for example, oleic acid, C17H.,., . CO . OH, may be supposed
to combine with oxygen, forming C17H33 % ~ ~Q QTT ; by tak-
ing up water this immediately produces dioxystearic acid,
(OH
CrH33 lOH ; whilst linolic acid, C.-H.^ . CO . OH, simi-
(CO.OH
i =0
larly first forms CrH,r =O , which by taking up 2H0O
( -CO. OH
OH
OH
forms tetroxystearic acid (sativic acid), Cl5.Hgl^ OH
OH
^CO.OH
Tn the case of the stearolic acid and its homologues obtained
from acrylic acids by the bromine reaction (addition of Br.7 and
removal of 2HBr, p. 31), the effect of oxidation stops short at
the first stage, 2 atoms of oxygen being added on forming a satu-
rated compound which does not take up water. Thus stearolic
( =°
acid, CrH.n . CO . OH, forms stearoxylic acid, ^-H^ - = O
( - CO . OH
melting at 84°-86°, by the direct action of nitric acid (Overbeck),^
or by means of alkaline permanganate (Hazura & Griissner).
Similarly palmitolic acid (from hvpogseic dibromide), gives the
* I = °
analogous pal mito.icyl ic acid, CirH.>-< =O , melting at 67°
" ( - CO . OH
(Schroeder) ; and benolic acid (from erucic dibromide) gives ben-
f = 0
oxylic acidj melting at 90°-91°, C91H80^=O (Hauss-
(-CO. OH
knecht).
•;- Overbeck (Annakn. Chem. P/iarm., 1866, 140, p.39) found that the stear-
oxylic acid thus prepared would not combine with bromine, and concluded
that the 4 affinity units which in stearolic acid are capable of combining
with Br4, are saturated by oxygen when stearolic acid is converted into
stearoxylic acid.
t Termed " dioxybenolic acid" by its discoverer.
46 OILS, FATS, WAXES, ETC.
By the action of heat (distillation in vacuo) dioxystearic acid
(melting at 136°), loses water forming an anhydro derivative still
possessing the characters of a monobasic acid (Saytzeff); obviously
thus —
(OH ( = O
C17HS8 OH = H20 + C17HoJ
( CO . OH ( - CO . OH
the reaction being the converse of the second stage in the
hydroxylation of unsaturated acids as above.
GENERAL PHYSICAL CHARACTERS. 47
§ 2. Physical Properties of Oils, Fats,
Waxes, &c.
CHAPTER IV.
GENERAL PHYSICAL CHARACTERS.
PHYSICAL TEXTURE AND CONSISTENCY.
THE physical consistency of a fixed oil — butter, fat, or wax —
depends entirely upon the temperature ; when this is sufficiently
raised all are fluid oils ; but at lower temperatures, according to-
the nature of the substance, more or less complete solidification
is brought about. In many cases, natural fixed oils, &c., are
mixtures of different glycerides, &c., the melting points of which
are different ; accordingly, at temperatures somewhat below the
melting point of the least fusible constituent, this more or less
completely solidifies, whilst the other constituents remain liquid,
thus giving rise to pastiness or buttery texture. Substances of
practically uniform composition (i.e., consisting essentially of only
one kind of compound) generally exhibit a fairly sharply defined
melting point when the temperature is sufficiently raised; but this
is not the case with mixtures ; accordingly, considerably different
temperatures will be registered as the fusing points of such sub-
stances if different methods be employed, depending, for instance,
in one case, upon the production of a considerable degree of
softness only ; in another, upon the complete liquefaction of all
the constituents ; and so 011 (vide p. 61, 63).
Even the most fluid oils possess to a greater or lesser extent
the property of viscosity, or resistance to flow, due to the greater
or lesser degree of cohesion between the constituent particles of
the liquid. When the smooth surfaces of two solids are smeared
or wetted with a viscous fluid and applied to one another, a,
varying degree of force will be requisite, according to circum-
stances, in order to enable one surface to glide over the other.
The amount of force requisite in any given case largely depends on
the viscosity of the fluid employed; to diminish this force is the
4-S OILS, FATS, WAXES, ETC.
main object of lubrication in the case of machinery, and in conse-
quence the determination of the relative lubricating powers of
different materials (lubricating oils, &c.) is an important point in
the valuation for such purposes of different fixed oils, mixtures
of these and mineral oils, and such like substances employed for
the purpose. It is found that the rate at which a given fluid
flows through an orifice of standard dimensions is in many cases
& fair measure of its lubricative powers ; whence the determina-
tion is frequently made of the rate of efflux of lubricating oils,
«foc., as compared with that of a standard fluid (such as rape oil),
similarly examined in the same apparatus at the same tempera-
ture, the value deduced being generally (but by no means cor-
rectly) spoken of as the relative viscosity of the fluid examined
(vide Chap, v.)
Cohesion Figures. — When a drop of oil is allowed to fall
gently on the surface of water in a basin or large plate, it often
Fig. 1.
behaves in a characteristic way, usually first spreading out into
ii thin film and then retracting again. It has been suggested
that the particular forms assumed by films of various kinds
(cohesion figures) are sufficiently well defined and characteristic
to be of service in the examination of oils with a view to
GENERAL PHYSICAL CHARACTERS. 4$
detecting adulteration ; but as yet little success has attended
experiments in this direction. Olive oil thus treated gives a fairly
characteristic result, which is more or less modified by various
admixtures, especially sesame oil. Fig. 1 (Schadler) represents
the different cohesion figures exhibited by colza oil (A, Brassica
rapa ; B, Brassica napus) ; poppy seed oil (C and D) ; sesame
oil (E) ; arachis oil (F) ; and olive oil (G-).
Taste and Odour. — When in a state of absolute purity,
fixed oils have usually little or no odour or taste ; but as met
with in commerce, in most cases traces of sapid or odorous
matters accompany the oil, so as give a more or less characteristic
flavour or smell thereto. Essential oils of the oxidised class, on
the other hand, are frequently possessed of most powerful scent,
although the hydrocarbons therein contained, when completely
separated from all traces of oxidised matter (by heating with
sodium or other similar means), are generally odourless or practi-
cally so. As regards the edible oils and fats, a considerable
amount of their value depends on the delicacy and purity of the
flavour ; thus genuine olive oil is esteemed far more highly by
connoisseurs than refined cotton seed oil, groundnut oil, and
similar substances with which the ordinary commercial article is
often largely intermixed, although, from the nutritive point of
view, these latter are probably quite equal in value to the pure
product of the olive. Similarly, the commercial value of butter
is largely affected by its flavour and freedom from all trace of
rancidity or rankness ; and analogous remarks apply to lard.
The difficulty of removing all matters communicating unpleasant
odour or taste to many varieties of fatty or oily matter often
prevents these being used for dietetic purposes to any consider-
able extent, at any rate by civilised nations ; in the case of
some materials — e.g., cod liver oil — such removal is practically
impossible without more or less interfering with the special
characters and qualities of the substance. Palm oil has generally
a peculiar smell, recalling that of violets, and for certain purposes
the possession of this odour is valuable — e.g., in the prepara-
tion of certain kinds of scented soaps. The development of
" rancidity " in fixed oils on keeping is in most cases due to
the presence in small quantity of mucilaginous or albuminous
matters which undergo chemical changes (oxidation, or decom-
position, &c.) in the course of time ; accordingly, the purification
and refining of crude oils, &c., for the purpose of removing these
ingredients is often a highly important operation.
Colour.— Expressed vegetable fixed oils sometimes possess a
greenish shade, due to the presence of chlorophyll ; as a general
rule, coldpressed oils of all kinds, prepared from fresh substances,
are almost white ; whilst oils subsequently expressed by the
aid of heat, especially from materials that have been stored some
time, are generally darker in tint, the hue varying from a
4
50
OILS, FATS, WAXES, ETC.
light straw yellow to a light or even dark brown. Palm butter
usually contains a dark orange red colouring matter, different
from chlorophyll ; similar substances appear to be present in
smaller quantity in many other oils, leading to the necessity for
bleaching them for certain purposes. The refining processes,
whereby mucilaginous extractive matters, &c., are removed,
usually serve to lighten the colour also.
The addition of coloured vegetable expressed oils (containing
chlorophyll, &c.) to animal oils, such as sperm oil, may sometimes
be detected by means of the absorption spectroscope * when such
adulteration has been practised.
The phenomenon of fluorescence does not appear to be. exhibited
by refined vegetable or animal oils free from substances possessed
of fluorescent properties (such as aesculin, occasionally found in
horse-chestnut oil); on the other hand, products of destructive
distillation (coaltar and rosin oils, tfec.) often exhibit this peculi-
arity, so that admixtures of such hydrocarbons with more expen-
sive vegetable and animal oils may sometimes be thus detected.
Action of Polarised Light. — The majority of the oils and
fats in common use have so little action of a marked character
on polarised light that little, if any, definite information of prac-
tical value is, as a rule, obtainable by means of such light; on
the other hand, adulteration with strongly active hydrocarbons
(such as some kinds of rosin oils) may sometimes be detected by
means of the polariscope.
Bishop has obtained the following values for a length of
200 mm. of various oils in a Laurent polarimeter; the other
figures annexed are from Schadler : —
Bishop.
Scbadler.
Degrees.
Degrees.
{Linseed oil,
- 0-3
- 0-2
Nut oil, .
- 0:3
La&vogyrate, •
Apricot oil,
Arachis oil,
- 'o-4
- 0-2
-o-i
Sweet almond oil,
- 0-7
- 0-2
Colza oil, .
- 1-6 to - 2-1
- 0-3
Neutral, or
nearly so,
{Cotton seed oil,
Poppy seed oil,
Seal oil, .
0
0
+ o-i
0
1' Olive oil, .
+ 0-6
+ 0'2
Cod liver oil,
+ O'o to +
0:7
Dextrogyrate,
Cold pressed sesame oil,
+ '3-1
I + 1-0 to +
1-1
Hot
-r 7 "2
\
Castor oil,
+ 9-8
* A special form of absorption spectrum colorimeter for this sort of
examination has been devised by T. L. Paterson ; vide Journ. ticc. Chem.
Industry, 1890, p. 36.
GENERAL PHYSICAL CHARACTERS.
51
Peter finds most vegetable oils to be slightly laevogyrate, olive
oil being an exception, so that admixtures of other oils may some-
times be detected by the rotation being left handed instead of
right handed. Croton oil and castor oil, however, are compara-
tively powerfully dextrogyrate, giving values exceeding + 40°.
Refractive Index. — The differences in refractive power
exhibited by different oils are in most cases hardly sufficiently
marked to render this property of much value in discriminating
one from the other, or in detecting admixtures, excepting in the
case of a few oils and fats, such as olive oil and cow's butter;
thus Strohmer gives the following values for the I) line at 15°,
and Abbe the annexed values at 20°, water being taken as
1-3330:—
.
Strohmer.
Abbe.
Olive oil,
1-4698 to 1-4703
1 -4690
1-4810
Sesame oil (new),
1 -4748
,, nine years old,
1-4762
Walnut oil, ....
...
1-491
Cotton seed oil, ...
1-4732 to 1-4752
\Crude, 1-4732
) Refined, 1-4748
Rape and colza oil,
1-47-20 to 1-4757
1-472 to 1-475
Beechnut oil, ....
1 -5000
Cold drawn castor oil,
1 -4795
\ i -/too
Hot pressed ,, .
1-4803
Cold drawn linseed oil,
1-4835
•4780
Poppy seed oil, ....
Cod liver oil, ....
1-4783
1-4800 to 1-4852
•4670
•4800
Whale oil
•483 .
Sperm oil, .
•470
From which it appears that olive oil has a sensibly lower re-
fractive index than the others, whilst drying oils and castor oil
exhibit the highest values. For the direct determination of the
refractive index of oils and other substances, Abbe and Pulfrich
have devised special " reiractometers."
Amagat and Jean * have also constructed an " oleorefracto-
meter," whereby the refractive power of a given oil is determined
by differential comparison with a sample of genuine oil taken as
standard', a positive reading denoting increased refractive index
and vice versd ; the following comparative differential values have
been obtained by de Bruijn and von Leent and by Jean in this
way, from which results they infer that the refractive powers of
* Comptex rendu*, 1889, 109, p. 616 ; see also Journ. Soc. Cliem. Industry,
1890, pp. 113 and 218.
52
OILS, FATS, WAXES, ETC.
oils, when thus tested, are capable of giving more information as
to admixture than is usually supposed. The oil to be examined
should be previously shaken with alcohol to dissolve out free
fatty acids ; the standard of comparison was a sample of the
purest olive oil obtainable : —
de Bruijn and v.
Leent.
Degrees.
Degrees.
Horse foot oil,
- 12
Sperm oil, .
Neat's foot oil, ....
- 12
3
Sheep's trotter oil,
0
Olive oil, .....
0 to + 2
+ 1 -5 to + 2
Almond oil, ....
+ 7
+ 6
Arachis oil, ....
+ 3 to -«- 4
+ 4 to -f 5
Colza oil, .....
+ 15 to H- 18
+ 16-5 to + 17'5
Sesame oil, .....
+ 45
+ 17
Cotton seed oil, .
+ 20
Maize oil, .....
+ 27
Poppy seed oil, ....
Whale oil,
...
+ 30
+ 30-5
Hemp seed oil,
+ 33
Castor oil, .....
+ 37 to + 46
+ 40
Linseed oil, ....
+ 49 to + 54
+ 53
Cod liver oil,
+ 42
Whale oil,
+ 30-5
Holde has obtained the following average results with this
instrument,* the temperature of the testing-room being close to
20° throughout : —
Limits of Index of Refraction.
Mean Index.
Refined rape oil,
Crude rape oil,
Olive oil, .....
1-4722 to 1-4736
1-4735 ,, 1-4760
1-4670 ,. 1-4705
1-4776 ,, 1-4980
1-4735
1 -4744
1 '4698
1 -4923-
Resiu oil, ....
1-5274 „ 1-5415
1 -5344
The presence of rape oil in olive oil can thus be detected when
any considerable amount of adulteration has been made.
In the case of butter, Jean claims that the oleorefractometer
is capable of rendering useful service in the laboratory. Even if
butter is not sufficiently constant in refractive power to enable a
decision to be always arrived at as to the genuineness or other-
Journ. Soc. Chem. Industry, 1891, p. 166.
SOLUBILITY IN SOLVENTS. 53
wise of a given sample without further tests, still the oleo-
refractometer indications at least enable a rough classification of
a variety of samples to be made, viz., those undoubtedly spurious,
those doubtful, and those probably genuine. The normal butter
deviation is regarded by him as - 29° to — 31°, averaging — 30° ;
if higher values (32°— 36°) are observed, admixture with palm or
cokernut oil is probable; slightly lower ones (25°-29°) correspond
with doubtful qualities; margarine and oleomargarine give much
lower figures, 13°- 17°.* Genuine butters have been found that
give values materially below the normal deviation, but the cause
of this is considered by Jean to be that the cows have been fed
on oilcake, unaltered oil from which finds its way into the
secreted milk in quantity large enough to affect the refraction,
though too small to produce any marked effect either on the
saponification equivalent, or the Reichert-Meissl-Wollny figure
for volatile acids (Chap, vui.)
Various British analysts also regard the oleorefractometer as
useful in preliminary butter examination, but other chemists
consider its value in this respect to be overrated ; thus de Bruijn
and von Leent obtained very discordant results with Dutch
butters, whilst H. O. G. Ellinger found f that genuine Danish
butters gave deflections varying between 23° and 35°, according
to the season of the year.
Electrical Conductivity. — In general, but little information
is obtainable by examining the relative electrical conductivities of
different oils. Olive oil, however, has a much lower conducting
power than most other oils of ordinary occurrence, and hence,
attempts to utilise this property as a means of detecting adultera-
tion of olive oil have been made, notably by Palmieri, who has
constructed a special instrument, or diagometer, for the purpose ;
as yet, however, this method does not seem to have come into
practical use to any considerable extent.
SOLUBILITY OF OILS, FATS, &c., IN VARIOUS
SOLVENTS.
The immiscibility of " oil and water " is proverbial ; but some
few oils are known where the solubility in water, although far
from perfect, is not entirely inconsiderable ; thus the fusel oils of
fermentation, and certain oxidised volatile essential oils, and
products of distillation (e.g., phenol), dissolve in water to the
* Journ. Soc. Ghent. Industry, 1892, p. 945; from Monit. Sclent., 1892, 6,
p. 91.
•\-The Analyst, 1891, p. 197; from Journ. f. prakt. Chemie,,[2] 44, p.
54 OILS, FATS, WAXES, ETC.
extent of a few per cents, by weight at ordinary temperatures.
As a general rule, however, fixed oils and hydrocarbons are, for
practical purposes, entirely insoluble in pure water ; in some few
cases dilute alkaline solutions dissolve them somewhat more freely
than pure water; in others the presence of acids slightly promotes
solubility ; but, as a rule, when neutral salts are present to any
extent, their presence prevents the solution of the oil, &c. ; so
that on agitating an aqueous solution with solid common salt or
with sodium sulphate, as the mineral matter goes into solution,
the dissolved oil is more or less thrown out of solution. The
same phenomenon is observed with the potash and soda salts of
most of the fatty acids, so that when an aqueous solution of such
salts (soaps) are treated with neutral saline matters, the organic
salts are thrown out of solution ; this property is largely utilised
in the ordinary process of soap boiling.
Strong alcohol does not exert any great degree of solvent action
in the cold on most fixed oils, solid fats, or waxes ; whereas,
many essential oils, whether hydrocarbons or of oxidised nature,
are extremely freely soluble therein. Similarly, resins and free
fatty acids are, generally speaking, moderately soluble in alcohol,
especially when almost anhydrous and warm. Some few fixed
oils, too, are exceptional as regards solubility in alcohol, more
especially castor oil and croton oil, and to a lesser extent coker-
nut oil, cow's butter, and linseed oil.
Girard finds that absolute alcohol at 15° dissolves the following
proportions of various oils : —
RaPeoil'| 1-5 to 2-0 per cent.
Colza oil, J
Mustard seed oil, .... 2'7 ,,
Hazelnut oil, . . . . . 3 '3 ,,
Olive oil, 3-6
Almond oil, 3 '9
Sesame oil, ..... 4*1 ,,
Apricot kernel oil, . . . . 4 '3 ,,
Nut oil, 4-4
Beechnut oil, . . . . . 4*4 ,,
Poppy seed oil, . . . . 4 '7 ,,
Hemp seed oil 5 '3 „
Cotton seed oil, . . . 6*4 „
Aracliis oil, ..... 6'6 „
Linseed oil, . . . . . 7'0 ,,
Camelina oil, ..... 7'H „
Schadler gives the following Table representing the quantities
of alcohol, of specific gravity '800, required to dissolve 1 part of
oil or fat : —
SOLUBILITY IN SOLVENTS.
55
Cold.
Boiling.
Parts.
Parts.
Almond oil, . . .
60
15
Cacao butter, .
4
Cotton seed oil, . .
75
...
Croton oil,
36
...
Camelina oil, .
68
t
Cod liver oil, .
45
"G
Hemp oil,
30
Soluble in all proportions.
Japan wax,
3
Linseed oil, .
40
5
Lard' (hog's),
27
Madia oil, . .
30
6
Nut oil (walnut),
100
60 alcohol to 100 of oil.
Nutzneg oil, .
4
Poppy seed,
25
6
Tallow (sheep),
45
Suet (ox tallow),
40
Whale oil (bottlenose),
...
1
As a general rule, fixed oils are very freely soluble in carbon
disulphide, chloroform, carbon tetrachloride, ether, benzene, light
petroleum distillate (mostly consisting of pentane and hexane
with their homologues), and oil of turpentine; and on this
property are based various methods of extracting oleaginous
matters from natural and other sources. Castor oil, however,
is almost insoluble in light petroleum spirit • whilst drying
oils, when oxidised to some considerable extent, generally be-
come either quite insoluble in these various solvents, or nearly
so, the decrease in solubility usually being the more marked the
greater the degree of oxidation. The action of nitrous acid on
an oil (conversion into elaidin, Chap, vn.) usually diminishes
the solubility of the oil thus affected.
Glacial acetic acid has been found by Yalenta to be a con-
venient solvent for certain oils, &c., as a means of separation
from one another. Thus, when equal volumes of acid and oil are
intermixed, the oil being previously warmed, complete solution,
even when cold, occurs with castor oil, rosin oil, and olive kernel
oil, whilst rape oil, mustard seed oil, and wild radish seed oil are
not completely dissolved even at the boiling point of the mixture.
Most other oils give a clear fluid whilst hot, which on cooling
becomes turbid, owing to the lesser solubility of the oil in the
acetic acid at lower temperatures. It has been proposed * to
make use of the temperature at which turbidity is thus brought
about as a distinguishing test for oils of various kinds ; but the
figures obtained by different authorities who have repeated
1 * Valenta, Dinyler's Poly tech. Journal, 252, p. 296 ; also, Journal of the
Chemical Society, *W, p. 1078.
56.
OILS, FATS, WAXES, ETC.
Yalenta's experiments, exhibit so much discrepancy as to render
it very doubtful whether the results can be relied upon at all, as
affording indications of adulteration or otherwise. Thus, the
following values, amongst others, have been obtained by A. H.
Allen * and G. H. Hurst :— f
Oil.
Valenta.
Allen.
Hurst.
Olive (green),
„ (yellow), .
85
111
•c.
| 28-76
Almond, ....
110
...
Arachis, ....
112
87
72-92
Apricot kernel,
114
Neat's foot, ....
...
102
G5-85
Sesame, ....
107
87
...
Melon seed,
108
...
...
Cotton seed,
110
90
53-63
Niger seed, ....
49
Linseed, ....
...
57-74
36-41
Cod liver, ....
101
79
65
Menhaden, . ...
...
64
Shark liver,
105
95
Porpoise, ....
...
40
98
85
Bottlenose, ....
...
102
74-84
Whale, ....
38-86
48-71
Palm,
23
83
Not turbid at 13
Laurelberry,
26-27
40
...
Nutmeg butter, .
27
39
Cokernut, .
40
7'5
M turbid at 13
Palm kernel,
48
32
Bassia fat (Illipe),
64'5
...
Cacao butter,
105
...
Beef tallow,
95
Pressed tallow (M.P., 55 '8),
114
...
Tallow oil (cold pressed),
...
47
Hog's lard, ....
...
96-5
...
Lard oil,
...
...
69-76
Butter fat, ....
61 '5
Oleomargarine,
...
. 96-5
The practical value of the test, as shown by the above numbers,
is obviously not very great ; it is still further diminished by the
circumstance that comparatively slight differences in the strength
of the glacial acetic acid considerably influence the temperature
of turbidity, as also does the presence or otherwise of free fatty
acids ; after an extended examination, Allen concludes that the
results are too variable and indefinite to be of service in
* Commercial Organic A naly&is, vol. ii. , p. 2C.
t Journ. Soc. Ckem. Industry, 1887, p. 22.
FUSING AND SOLIDIFYING POINTS.
57
discriminating the quality of oils ; an opinion also arrived at by
G. H. Hurst, by Ell wood,* and by Thomson and Ballantyne,t
the latter of whom obtained the following numbers, inter alia,
with glacial acids of different strengths : —
1
Percentage of
Free Acid
Temperature of Turbidity with Glacial
Acetic Acid of
Name of Oil.
present
(calculated as
Oleic Acid).
Sp. gr. 1054-2
Sp. gr. 1055-2.
Sp.gr. 1056-2.
°C.
•G.
°C.
Olive (Syrian),
23-88
42
...
,, (Gioja),
9-42
65
80
91
Same sample freed from \
free acid, . . . J
None.
87
...
...
Arachis oil (commercial),
6-20
76
96
112
,, (French )
refined), {
•62
96
m i
Not completely
dissolved.
Eape oil,
4-54
2-43
105 \
110 /
Hot completely
dissolved.
,,
Linseed oil (Baltic),
3-74
42
59
71
(River Plate),
1-21
56 -
...
,, (East India),
•79
57
In some few cases, however, the comparatively solubility in
glacial acetic acid may afford a useful indication — e.g., in de-
tecting the presence of rape seed oil in linseed oil, and more
especially of hydrocarbons in animal and vegetable saponifiable
oils ; thus, mineral oils are but sparingly soluble in glacial acetic
acid, so that on agitating with that solvent a mixture of mineral
oil and other substances freely soluble in acetic acid, the latter
are dissolved, leaving the former undissolved ; in this way the
presence of rosin oil is easily detected in paraffin and petroleum
distillates.
FUSING AND SOLIDIFYING POINTS.
It most unfortunately happens that several different thermo-
metric scales are in use in different countries ; of these the
Celsius or Centigrade scale is by far the most convenient, and
is accordingly used almost exclusively for scientific purposes.
In England, however, the highly inconvenient Fahrenheit scale
is still largely in use for technical and general purposes ; whilst
in some parts of the Continent the Reaumur scale is similarly
employed. The following formula gives the means of translating
the temperature expressed on any one of these systems to the
* Pharmaceutical Journal, 3, xvii., p. 519.
t Journ. Soc. Chem. Industry, 1991, x., p. 233.
58 OILS, FATS, WAXES, ETC.
corresponding value expressed on either of the others, F being
the value on the Fahrenheit scale, C that on the Centigrade scale,
and R that on the Reaumur scale : —
F_-_32 _ C _ R
9 ~ 5 ~ 4*
This formula is based on the system of construction of the
three scales respectively ; the distance between the " ice melting
point " (sometimes termed the " freezing point ") and the " steam
point" (or "boiling point" — under normal atmospheric pressure)
being divided into 180 degrees on the Fahrenheit scale,* 100 on
the Centigrade, and 80 on the Reaumur scale ; so that the rela-
tive values of the degree in each scale respectively are — T-J-F :
TUIT • 8"V > or v • i • T' The Reaumur and Centigrade scales,
however, begin with the ice melting point as 0, so that the
steam point is at 80° and 100° on the two scales respectively ;
wrhilst the Fahrenheit zero is 32° F. below the ice melting point ; f
whence that point is 32°, and the steam point 32 + 180 = 212°,
on the Fahrenheit scale.
From the above formula are derived the following equations,
whereby, when requisite, a Centigrade temperature may be trans-
lated into the corresponding Fahrenheit value, and so on : —
C - (F - 32).
F = C + 32.
o
= (F - 32).
* This particular number is said to have been selected on account of some
hazy idea on the part of the inventor that the temperature-range between
freezing and boiling of water had some connection with the number of
degrees in a semicircle, or two right angles !
-f Presumably because M. Fahrenheit noticed that the temperature of a
mixture of snow and salt was 32 of his degrees below the freezing point of
water, and concluded, for some unknown reason, that this must be the
initial temperature, or absolute zero.
FUSING AND SOLIDIFYING POINTS.
The following table affords a yet simpler means of effecting
the translation : —
Centigrade.
i
Reaumur.
Fahrenheit,
•
Centigrade.
Rdaumur.
Fahrenheit.
|
i Centigrade.
•jiunnrpjj
j
Fahrenheit.
- 40
- 32
- 40
+ 7
+ 5-6
+ 44-6
+ 54
+ 43-2
+ 129-2
- 39
- 31-2
- 38-2
+ 8
+ 6-4
+ 46-4
+ 55
+ 44
+ 131
- 38
- 30-4
- 36-4
+ 9
+ 7-2
+ 48-2
+ 56
+ 44-8
+ 132-8
- 37
- 29-6
- 34-6
+ 10
t 8
+ 50
+ 57
+ 45-6
+ 134-6
- 36
- 28-8
- 32-8
+ 11
+ 8-8
+ 51-8
+ 58
+ 46-4
+ 136-4
- 35
- 2S
- 31
+ 12
+ 9-6
+ 53-6
+ 59
+ 47'2
+ 138-2
- 34
- 27-2
- 29-2
+ 13
+ 10-4
+ 55-4
+ 60
+ 48
+ 140
- 33
- 26-4
- 27-4
+ 14
+ 11-2
+ 57-2
+ 61
+ 48-8
+ 141-8
- 32
- 25-6
- 25-6
+ 15
i- 12
+ 59
+ 62
+ 49-6
+ 143-6
- 31
- 24-8
- 23-8
+ 16
+ 12:8
+ 60-8
+ 63
+ 50-4
+ 145-4
- 30
- 24
- 22
+ 17
+ 13 6
+ 62-6
+ 64
+ 51-2
+ 147-2
- 29
- 23-2
- 20-2
4- 18
+ 14-4
+ 64-4 + 65
+ 52
+ 149
- 28
- 22-4
- 18-4
+ 19
+ 15-2
+ 66-2 ! + 66
+ 52-8
+ 150-8
- 27
- 21-6
- 16-6
+ 20
+ 16
+ 68
+ 67
+ 53-6
+ 152-6
- 26
- 20-8
- 14-8
+ 21
+ 16-8
+ 69-8
+ 68
+ 54-4
+ 154-4
- 25
- 20
- 13
+ 22
+ 17-6
+ 71-6
+ 69
+ 55-2
+ 156-2
- 24
- 19-2
- 11-2
+ 23
+ 18-4
+ 73-4
+ 70
+ 56
+ 158
- 23
- 18-4
9-4
+ 24
+ 19-2
+ 75-2
+ 71
+ 56-8
+ 159-8
- 22
- 17-6
- 7-6
+ 25
+ 20
+ 77
+ 72
+ 57-6
+ 161-6
- 21
- 16-8
- 5-8
+ 26
+ 20-8
+ 78-8
+ 73
+ 58-4
+ 163-4
- 20
- 16
4
+ 27
+ 21-6
+ 80-6
+ 74
+ 59-2
+ 165-2
- 19
- 15-2
- 2-2
+ 28
+ 22-4
+ 82-4
+ 75
+ 60
+ 167
- 18
- 14-4
0-4
+ 29
+ 23-2
+ 84-2
+ 76
+ 60-8
+ 168-8
- 17
- 13-6
+ 1-4
-r 30
+ 24
+ 86
+ 77
+ 61-6
+ 170-6
- 16
- 12-8
+ 3-2
+ 31
+ 24-8
+ 87-8
+ 78
+ 62-4
+ 172-4
- 15
- 12
+ 5
+ 32
+ 25-6
+ 89-6
+ 79
+ 63-2
+ 174-2
- 14
- 11-2
+ 6-8
+ 33
+ 26-4
+ 91-4
+ 80
+ 64
+ 176
- 13
- 10-4
+ 8-6
+ 34
+ 27-2
+ 93-2
+ 81
+ 64-8
+ 177-8
- 12
9-6
+ 10-4
+ 35
+ 28
+ 95
+ 82
+ 65-6
+ 179-6
- 11
- 8-8
+ 12-2
+ 36
+ 2S'8
+ 96-8
+ 83
+ 66-4
+ 181-4
- 10
— 8
+ 14
+ 37
+ 29-6
+ 98-6
+ 84
+ 67-2
+ 183-2
- 9
- 7-2
+ 15-8
+ 38
+ 30-4
+ 100-4
+ 85
+ 68
+ 185
- 8
- 6-4
+ 17-6
+ 39
+ 31-2
+ 102-2
+ 86
+ 68-8
+ 186-8
_ IT
5-6
+ 19-4
+ 40
+ 32
+ 104
+ 87
+ 69-6
+ 188-6
6
- 4-8
+ 21-2
+ 41
+ 32-8
+ 105-8
+ 88
+ 70-4
+ 190-4
5
— 4
+ 23
+ 42
+ 33-6 + 107 -G
+ 89
+ 71-2
+ 192-2
4
- 3-2
+ 24-8
+ 43
+ 34-4 + 109-4
+ 90
+ 72
+ 194
3
- 2-4
+ 26-6
+ 44
+ 35-2 +111-2
+ 91
+ 72-8
+ 195-8
_ 2
- 1-6
+ 28-4
+ 45
+36 ; + 113
+ 92
+ 73-6
+ 197-6
— 1
- 0-8
+ 30-2
+ 46
+ 36-8
+ 114-8
+ 93
+ 74-4
+ 199-4
0
0
+ 32
i + 47
+ 37-6
+ 116-6
+ 94
+ 75-2
+ 201-2
+ 1
+ 0-8
+ 33-8
+ 48
+ 38-4
+ 118-4
+ 95
+ 76
+ 203
+ 2
+ 1-6
+ 35-6
+ 49
+ 39-2
+ 120-2
+ 96
+ 76-8
+ 204-8
+ 3
+ 2-4
+ 37-4
+ 50
+ 40
+ 122
+ 97
+ 77-6
+ 206-6
+ 4
+ 3-2
+ 39-2
+ 51
+ 40-8
+ 123-8
+ 98
+ 78-4
+ 208-4
+ 5
+ 4
+ 41
+ 52
+ 41-6
+ 125-6
+ 99
+ 79-2
+ 210-2
+ 6
+ 4-8
+ 42-8
+ 53
+ 42-4
+ 127-4
+ 100
+ 80
+ 212
!
60 OILS, FATS, WAXES, ETC.
Iii the following pages, whenever a temperature is expressed
as a number without the scale used being mentioned, it is always
to be understood that the Centigrade value is intended.
Determination of Fusing and Solidifying Points. — Inas-
much as most natural oils and fats, itc., are not chemically pure
single substances, but generally consist of one or more main
ingredients with smaller quantities of other allied bodies, as a
general rule no sharply defined temperature exists characteristic
of the fusing or solidifying point of any given variety, although
in many cases pure unadulterated specimens, even though of
widely various origin, do not differ largely in these respects.
For the same reason, the point at which incipient solidification
on chilling first becomes manifest, often differs considerably from
the temperature at which the mass, when once rendered solid by
cold, exhibits incipient fusion on gradual heating. Further, a
given substance, if heated considerably above its melting point
and then cooled quickly so as to solidify it again, will often melt
for the second tyne at a temperature materially different from
that at which it first fused, although the normal melting point is
more or less regained on standing for some time ; accordingly, if
the fusing point of a solid fat that has been once melted is to be
determined, a sufficient time must be allowed to elapse to enable
the normal physical structure to be re-assumed. In practice, it
is generally necessary first to melt the substance and then clarify
it by subsidence, or, better, by filtration through dry paper, in
order to remove suspended matters and, more particularly, water;
so that the purified material, after cooling and solidification, must
be allowed to stand some time (at least an hour or two, but
preferably a much longer period, say till the next day) before
further "examination.
In order to determine the fusing point of a
solidified specimen, several different methods are
in use, the results of which are not always com-
parable with one another; so that, if an accurate
comparison of two substances is requisite, it is
indispensable that both must be examined by the
same process, side by side. One of the most fre-
quently used methods consists in preparing a
capillary tube by drawing out in a flame a short
piece of quill tubing (Fig. 2); the fine end is
sealed up, and when cool, the solid to be ex-
amined is cut into very fine fragments or pul-
verised, and a little dropped in and shaken down
into the capillary tube. This is then bound by
Fig. 2. wire, string, or an india-rubber ring to the stem
of a thermometer (Fig. 3), so that the centre of
the bulb is about level with the substance ; the whole is then
placed in a small vessel of water (or, for higher temperatures,
FUSING AND SOLIDIFYING POINTS. 01
melted paraffin wax) which is very slowly raised in temperature,
either by means of a small flame underneath (Fig. 4), or, pre-
ferably, by placing it inside a much larger similar vessel ; a large
flask with the neck cut off and a small beaker answer well (-Fig.
5). Olberg employs for this purpose the circulatory arrange-
ment shown in Fig. 6 ; this is filled with water or oil, the heat
being applied at the base of A.
If circumstances permit, two such capillary tubes (or more)
should be provided, one being used to obtain a first rough
Fig. 3. Fig. 4.
approximation to the melting point, and the others used sub-
sequently to obtain a nearer result, the bath being previously
slightly cooled below the first approximate value, and then very
slowly heated again, so that several minutes are requisite to
produce a rise in temperature of 2° or 3° C. The thermometer
and attached tube are used as a stirrer during this heating, and
the temperature noted when the fragments first show signs of
melting. Frequently this temperature (softening point) is
measurably below that requisite to cause the fragments to liquefy
entirely, and run down to the bottom of the capillary tube as a
clear fluid (temperature of complete fusion).
G2
OILS, FATS, WAXES, ETC.
Instead of a capillary tube sealed up at the end, one bent into
a U or V shape may be employed, the solid particles being
shaken down to the bend or angle. Bensemann * modifies the
tube by drawing it out as represented in Fig. 7. A drop or two
Fig. 5. Fig. 0.
of melted substance is introduced into the bulbed portion of the
tube, A, and fused as indicated by a. After standing for a
sufficient time, the tube is placed in water, the temperature of
which is very slowly raised ; the temperature of incipient lique-
faction is readily observed when the material softens and begins
to run ; at a little higher temperature it all runs down as-
indicated by b ; when the turbid liquid becomes completely clear,
the temperature of complete fusion is attained.
Another method of operating consists in drawing out the
capillary tube as before, but without sealing up the narrow end ;
this end is then dipped into the molten substance to be
examined and withdrawn, so that half an inch or so of the
capillary tube is filled up with the material. After standing at
least an hour, but preferably till next day, the capillary tube is
attached to the thermometer and placed in the bath as before ;
when the temperature rises to the softening point so as to produce
incipient fusion, the plug of solid matter in the capillary tube
becomes softened where it touches the glass, and is consequently
* Journ. Soc. Chem. Industry, 1885, iv., p. 5.35 ; from Rep. Anal. Chem.,
11, p. 165.
FUSING AND SOLIDIFYING POINTS.
63
forced upwards by the hydrostatic pressure of the fluid in the
bath ; when this occurs the temperature is noted. The former
process, as a rule, is to be preferred, not only because it gives
both the softening point and the temperature of complete lique-
faction, but also, because by withdrawing the source of heat and
allowing the completely fluid mass to cool slowly, the temperature
at which re-solidification occurs can be more or less accurately
determined. With some kinds of mixed substances, the sealed-
up capillary tube process enables three different temperatures to
be ascertained, viz. : — First, the temperature of incipient fusion
when the most fusible constituent commences to melt ; second, a
temperature when this constituent has become so far melted that
the solid fragments run down visibly; and third, a still higher
temperature when the whole mass becomes' clear and limpid,
showing that the whole of the less fusible constituents have also
become completely melted. With certain mixtures of free fatty
acids, &c., the difference between the lowest and highest fusion
temperatures thus determined may amount to upwards of 5° C.
A convenient method of determining the softening point in
certain cases consists in dipping the bulb of the thermometer into
the melted material to be examined, and causing a small light
OILS, FATS, WAXES, ETC.
glass bulb or float to adhere to the thermometer, cemented
thereto by the substance as it solidifies. After waiting a sufficient
time to enable the mass to attain its normal physical structure,
the thermometer and bulb are placed in a bath, which is
gradually heated ; when the temperature attains the softening
point, the float becomes detached and rises up in the fluid.
Instead of a float, a thick coating of the substance itself may be
ap'plied to the thermometer by dipping the latter in the just-
melted substance for an instant, taking out again until the
adherent film has solidified, and repeating the operation two or
three times so as finally to obtain a sufficiently thick coating.
Fig. 8 represents Pohl's form of bath for the purpose, consisting
of a wide test-tube, C, through the cork in the mouth of which
passes the thermometer, T, the heat being applied by means of a
small flame impinging on a flat metal disc, supported a little
distance below the test-tube, so as to furnish an ascending
current of warm air. Obviously a vessel of warm water may be
substituted for the disc and flame. A modification of this plan
has been suggested by Messrs. Cross and Be van,* where a thin
piece of sheet iron (ferrotype
plate) is cut into the shape
shown in Fig. 9, about ;f inch
long and f or J inch across ;
at A the plate is hammered so
as to form a minute saucer or
depression, and at B a hole is
cut of such size as to allow the
plate to fit on to the bulb (coni-
cal) of a thermometer. The
float is made by blowing a bulb
on the end of a thin piece of
tubing, and fixing a bit of pla-
tinum wire therein, bent into
an L shape. A drop of melted
substance is put in the saucer,
and the end of the wire dipped
therein, the stem being sup-
ported in a vertical position
until the substance solidifies,
and so holds it firmly. The
thermometer and float are
placed in a bath of water, &c. (preferably mercury), and when
the temperature rises to the softening point, the float becomes
detached and rises to the surface.
In many cases the temperatures of incipient fusion and of
complete liquefaction may be easily determined by placing small
fragments or pinches of powder of the substance examined on the
* Journal of the Chemical Society, vol. xli. (1882), p. 111.
Fi. 9.
FUSING AND SOLIDIFYING POINTS.
65
surface of a bowl of perfectly clean mercury, the temperature of
which is gradually raised, a thermometer being placed therein.
When complete fusion is effected, the substance becomes a minute
drop of clear fluid, which usually spreads out film-wise over the
surface of the mercury. A n ingenious modification of this method
has been proposed by J. Loewe,* where the substance is first applied
to the end of a platinum wire (by dipping into the just-fused
substance), so as to cover it completely ; the coated wire is then
supported by means of an insulating holder of glass, just below
the surface of the mercury, and connected with one pole of a
small galvanic cell, whilst the mercury is connected with the
other pole. As long as the substance is unmelted no contact
takes place between the platinum wire and mercury ; but as soon
as fusion takes place contact is brought about, and an electric
bell included in the circuit is made to ring. Fig. 10 represents
Fig. 10.
the general arrangement employed, the mercury being placed in
a capsule heated over a small water bath, and the temperature
ascertained by means of a thermometer plunged therein. Instead
of a platinum wire coated with the substance examined, Christo-
manosf employs a drawn-out capillary tube into which the melted
substance is sucked or poured, a platinum wire being imbedded
in the material. After solidifying and standing sufficiently long
to attain the normal texture of the substance examined, the
capillary tube is heated in a mercury bath, electrical connections
being applied to the bath and platinum wire, so that when the
substance fuses contact is made and a bell rung. A. similar
arrangement is in. use in the Paris Municipal Laboratory, the
substance tested being placed in the bend of a U-shaped tube
with a platinum wire in each limb, together with some mercury,
which runs down and makes contact when fusion occurs.
* Dingier 's Polytechnisches Journal, 201, p. 250.
t Journal Soc. Chem. Industry, 1890, p. 894 ; from Berichte d. Deut.
Chem. Gcs., 1890. p. 1093.
5
66 OILS, FATS, WAXES, ETC.
If the fusing point of a fluid oil that has been solidified by
chilling is to be determined, the bath used must be itself cooled
down below the fusing point, and gradually allowed to rise in
temperature. Strong brine, giycerol diluted Avith a little water,
or calcium chloride solution may be conveniently used for tem-
peratures below 0°. When the solidification point of a fluid oil
or melted fat is to be determined, a rough approximation may
often be obtained by placing some in a small narrow test-tube,
or dipping into the fluid a loop of platinum wire so as to cause a
small drop to adhere, and immersing in a bath of water, brine,
&c., which is being cooled down by an external application of
broken ice or snow and salt, &c., noting the temperatures when
transparency first ceases, and when visible solidification of the
whole mass has ensued. In most cases, however, the temperatures
thus ascertained are too low, because superfusion is extremely
apt to occur with oils and fats. If, however, a moderately large
quantity of substance be used (15 to 20 grammes at least),
it frequently occurs that as soon as solidification begins a more
or less considerable rise in temperature of the mass takes place,
just as when water cooled down below 0° in a dustless still
atmosphere rises to 0° whenever freezing actually commences ; or
just as the temperature of a supersaturated solution of Glauber's
salt (sodium sulphate) rises when the fluid sets to a crystalline
mass. The higher temperature thus indicated is permanent for
a time as solidification goes on, and is usually much more nearly
exact than the lower one attained before solidification com-
menced ; but even this higher one is often several degrees below
the temperature of incipient fusion (and a fortiori below that of
complete fusion) indicated when the mass has been solidified
completely, allowed to stand some time, and then re-melted in
a sealed-up capillary tube.
Differences of this description are more usually observed when
the substances in question are mixtures of different constituents
melting at different temperatures ; on the other hand, a single
substance in a state of moderate purity (e.g., a well purified
sample of a given fatty acid, such as stearic acid) usually shows
but little difference between the temperatures of incipient fusion
and of complete fusion in a closed capillary tube, and those
where the limpid fused mass first shows signs of turbidity, and
where visible complete solidification occurs, on slightly cooling
the melted substance.
With some kinds of oils, time is an important factor in the
determination of the temperature at which solidification takes
place on chilling, inasmuch as frequently no solidification at all
is visible on cooling for a short time to a given temperature
(e.g., — 15° C.), whereas more or less complete solidification takes
place on keeping for several hours at a temperature not so low
by several degrees (e.g., — 5°). In most cases, if a fragment of
FUSING AND SOLIDIFYING POINTS.
67
oil, previously solidified by chilling, be dropped into a specimen
of cooled oil, solidification is brought about much sooner, the
particle introduced acting as a "nucleus " and facilitating crystal-
lisation in the well-known way observed with other bodies (e.g.,
supersaturated solution of sodium sulphate • superfused metals ;
glycerol ; monohydrated sulphuric acid ; water chilled down
whilst at rest below 0°, &<?.). For determinations of this kind,
baths of fairly constant low temperatures, capable of being main-
tained for considerable periods, are requisite ; Hoffmeister uses
for this purpose various saline solutions cooled externally by a
freezing mixture ; by suitably choosing the saline substance and
the strength of its solution, baths of constant temperature are
obtainable so long as any liquid remains unsolidified or any solid
unmelted. Thus the following temperatures correspond with
solutions of the respective strengths : —
Temperature.
Solution.
Degrees C.
0
- 2-85 to - 3-0
- 5-0
- 8 '7 to - <)•()
- 15-4 to - 15-0
Distilled Water.
Potassium nitrate, .
\ Potassium nitrate, .
I Sodium chloride.
Barium chloride,
Ammonium chloride,
13 parts per
13
3-3
35-8
25
100 of water.
55
3 5
55
Chilling baths of this description are more especially of use in
the examination of lubricating oils with respect to their congeal-
ing temperatures.
The following table, mostly derived from Schadler's Technologic
der Fette und Oele, exhibits the average melting and solidifying
points of many of the more commonly occurring fats and oils : —
FREEZING AND MELTING POINTS OF OILS, &c.
Name.
Arachis oil,
Almond oil,
Bassia fat (Galam butter),
Beechnut oil,
Ben oil,
Belladonna seed oil, .
Butter,
Bone grease,
Cacao butter,
Castor oil,
Cokernut oil,
Colza oil, .
Cotton seed oil, .
Cress seed oil,
Melting Point
after
Solidification.
Solidifying Point
•when Cooled
(after Fusion, if
Solid).
Degrees.
Degrees.
,
- 3 to - 4
- 20
28 to 29
21 to 22
...
-16-5 to -17-5
m
About 0
...
- 16
29 to 35
20 to 30
44 to 45
35
33 to 34
20-5
...
- 18
24*5
20 to 20-5
- 6
- 2
...
- 15
68
OILS, FATS, WAXES, ETC.
FREEZING AND MELTING POINTS OF OILS, &c. — Continued.
Name.
Melting Poiut
Hfter
Solidification.
Solidif
whe
(after
5
Degrees.
D(
Goa butter (Brindonia indica), .
Goose grease, .....
40
26
Gourd seed oil, .....
Hazelnut oil,
Hemp seed oil, .....
Japanese wax, .....
Laurel berry fat, ....
Linseed oil, .....
Madia oil, .....
Nut oil,
53 to 54
38
43'5 to 44
- 17
- 27
40
Oleic acid, ......
Olive oil ....
2
- 16
Palm oil, ......
Pine oil, ......
Rape seed oil (Brassica napus oleifera),
Radish seed oil,
30 to 41
21
Spindel oil (Euonymus europseus),
Sunflower seed oil, ....
Tallow,
Tobacco oil,
Train oil, ......
Virola fat (Virola sebifera),
Wax,
Whale oil ...
46 to 50
45
62 to 64
36
01
Al
0 t
Weld oil.
•
Beloi
Solid).
Degrees.
- 16
32
18
- 16
- 15
- 18
27 to - 28
40 to 41
30
- 19
- 15
- 28
33
- 6
2 to 4
16 to - 18
21 to 37
- 18
- 3
- 4
- 5
- 10
- 16
36 to 40
- 25
to - 2
40
About 60
0 to - 2
WlMMEL.
Melts at
Becomes
Turbid at
Temperature
rises during
Solidification to
Sheep's tallow (fresh), .
(old), . .
Ox tallow (fresh),
(old), .
Hog's lard, ....
Butter (fresh),
Degrees.
47
50-5
43
42-5
41 -5 to 42
31 to 31 -5
Degrees.
36
39-5
33
34
30
19 to 20
Degrees.
40 to 41
44 to 45
36 to 37
38
32
19 -5 to 20 -5
Cacao butter,
Coker butter,
Palm butter (fresh), .
(old),
Nutmeg butter, .
34 to 35-5
24-5
30 to 36
42
43 -5 to 44
62 to 62-5
20-5
20 to 20-5
21 to 24
38
33
27 to 29 5
22 to 23
21 -5 to 35
39-5
41 -5 to 42
Spermaceti, ....
44 to 44 5
...
FUSING AND SOLIDIFYING POINTS.
RiJDORFF.
Melts at
Solidifies at
Degress.
Degrees.
Yellow wax,
63-4
6 1 -5 to 62 -6
\Vhite wax,
61-8
61-6
Spermaceti,
43 -5 to 44 -3
43-4 to 44-2
Japanese wax,
50-4 to 51
...
Cacao butter,
33-5
...
Nutmeg butter,
70 to SO
...
Sheep's tallow,
4G-5 to 47 '4
32 to 36
Ox tallow, .
43-5 to 45-0
27 to 35
The foregoing fusing and solidifying points of various solid
fats are given by Wimmel and Eiidorff respectively.
The fusion point of a pure glyceride, or mixture of glycerides,
is often materially altered if, as is often the case, any considerable
amount of hydrolysis has taken place, either through develop-
ment of " rancidity" through fermentative changes taking place
on account of the presence of mucilaginous or albuminous
matters, or by the agency of acids during refining, or otherwise.
Hence, the numbers obtained with various samples of otherwise
pure oils (i.e., unadulterated with cheaper ones) are apt to vary.
More nearly concordant figures are obtained if the whole of
the glyceride is saponified by means of alkalies (e.g., alcoholic
potash), and the fatty acids separated from the resulting soap
by evaporating off alcohol, dissolving the residue in hot water,
acidulating with a mineral acid in excess, thoroughly agitating
till all the soap is decomposed, and finally allowing to cool, and
removing the cake of solidified fatty acids that separates and
forms on standing.
By determining the fusing point of the fatty acid cake thus
produced side by side with that similarly prepared from a sample
of oil of known purity, or from a mixture of known character,
useful indications as to purity or otherwise are often attainable ;
for example, the fatty acids from genuine olive oil usually fuse
at from 22° to 26° C., and those from refined cotton seed oil at
35° to 40°, so that any considerable admixture of cotton seed oil
with olive oil will usually result in yielding a cake of notably
raised fusing point. The amount of rise, however, does not give
any very clear indication of the amount of admixture, because, as
a general rule, mixtures of different substances fuse at a tempera-
ture lower than that calculable arithmetically from the relative
amounts and fusing points of the ingredients (vide p. 73).
The following table represents the melting and solidifying
points of the mixed fatty acids obtained from various oils and
fats, as given by Schadler : — •
70
OILS, FATS, WAXES, ETC.
Name of Oil. &c.
Melting Point.
Solidifying Point.
Degrees C.
Degrees C.
Apricot kernel,
4-5
0
Almond,
14
5
Arachis,
32 to 33
29 to 30
Butter,
37
33
Cacao butter,
49-5
46 '5 to 47
Castor,
13
3
Charlock, .
18 to 19
13
Chinese tallow,
57
52
Cotton seed,
37 to 38
32-5
Cokernut,
24 to 25
20 to 20-5
Colza, ....
20 to 21
14 to 14-5
Galam butter,
35-5
30
Hemp, ....
19
15
Lard, ....
38 to 39
35
Linseed,
17
13-5
Lallemantia (Gundschit),
11 to 12
Malabar tallow,
56-5
54-8
Margarine, .
42
39-4
Nutmeg,
42-5
40
Nut (Walnut),
20
16
. Olive, ....
26 "5 to 28
21 -5 to 22
Poppy,
20-5
16-5
Palm, ....
45 to 46
42 to 43
Rape, ....
21
16
Suet (Ox), .
45-5
43
Sesame,
35 to 36
31-5 to 32
Spermaceti, .
13-5
Sunflower,
23
17
Tacamahac, .
36-5
31
Tallow (Sheep), .
49
46
Unguadia,
19
10
Wool grease,
41-8
40
Slightly different values have been given by other observers,
the variations arising partly from differences between the par-
ticular specimens examined and partly from differences in the
mode of observation. Thus the figures below given by Hiibl
are respectively the temperatures of complete liquefaction (as
noticed by melting in a narrow test-tube, stirring with a ther-
mometer, and noting the temperature when turbidity disap-
peared), and of incipient solidification (as noticed by cooling
down after complete melting, and noticing when cloudiness com-
menced) ; whilst those of Beiisemann are (A) the temperature of
complete liquefaction, when all turbidity disappears, as deter-
mined in the above described form of capillary tube, and (B)
the somewhat lower temperature when the substance was suffi-
ciently liquefied to run down in the capillary tube, but was not
thoroughly fused to a limpid fluid : —
FUSING AND SOLIDIFYING POINTS.
71
Fusing Point.
Solidifying Point.
Hiibl.
Bensemann.
Allen.
HUbl.
Bach.
Allen.
A B.
Dees.
C.
Degs.
Degs.
Degs.
Degs.
Degs.
Degs.
Olive oil, . . .
26-0
26 to 27
23 to 24
26 -Q
21-2
22-0
21-0
Almond oil, . . i 14*0*
...
...
5-0
Arachis oil, . . 27*7
34 to 35
31 to 32
29-5
23 -8
31-0
28-0
Rape oil, . . .
20-1
21 to 22
18 to 19
19-5
12-2
15-0
18-5
Cotton seed oil,.
377
42 to 43
39 to 40
35-0
30-5
35-0
32-0
Sesame oil, . . ! 26 '0
29 to 30
25 to 26
23-0
22-3
32-5
18-5
Linseed oil, . . 17;0
...
24-0
13-3
...
17-5
Poppy oil, . .
20-5
.. .
16-5
Hemp seed oil. .
19-0
...
15-0
...
Walnut oil, . ' .
20-0
...
16-5
...
...
Castor oil,
13-0
3-0
2-0
...
Palm oil, ...
47-8
50 :0
42-7
...
45-5
Cokernut oil,
24-6
24-0
204
...
20-5
Japan wax, . .
...
56-0
...
53-0
Myrtle wax, . .
...
47-5
...
46-0
Lard, ....
...
...
44-0
...
42
39-0
Tallow, . . .
45-0
...
...
43 to 50
44 to 49
...
Shea butter, . .
395
...
38-0
...
...
The following tables by Heintz * represent the melting points
of various definite mixtures of fatty acids : — •
MIXTURES OF MYRISTIC AND LAURIC ACIDS.
Percentage of
Melting Point.
Solidification Point.
Myristic Acid.
Laurie Acid.
Degrees C.
Degrees C.
58-8
100
0
51-8
47-3
90
10
49-6
44-5
80
20
46-7
39-0
70
30
43-0
39-0
60
40
37-4
35-7
50
50
36-7
33-5
40
60
35-1
32-3
30
70
38-5
33-0
20
80
41-3
36-0
10
90
43-6
...
0
100
* Poggendorff Annalen, 92, p. 588.
72
OILS, FATS, WAXES, ETC.
MIXTURES OF PALMITIC AND MYRISTIC ACIDS.
Melting Point.
Solidification Point.
Percentage of
Palmitic Acid.
Myristic Acid.
Degrees C.
Degrees C.
62-0
...
100
0
61-1
58-0
95
5
60-1
55-7
90
10
58-0
53-5
80
20
54-9
51-3
70
30
51-5
49-5
60
40
47-8
45-3
50
50
47-0
43-7
40
60
46-5
43-7
35
65
46-2
44-0
32-5
67-5
46-2
43-7
30
70
49-5
41-3
20
SO
51-8
45-3
10
90
53'8
0
100
MIXTURES OF STEARIC AND PALMITIC ACIDS.
Percentage of
Melting Point.
Solidification Point.
Stearic Acid.
Palmitic Acid.
Degrees C.
Degrees C.
69-2
100
0
67-2
62-5
90
10
65-3
60-3
80
20
62-9
59-3
70
30
60-3
56-5
60
40
56-6
55-0
50
50
56-3
54-5
40
60
55-6
54-3
35
65
55-2
54-0
32-5
67'5
55-1
54-0
30
70
57-5
53-8
20
80
60-1
54-5
10
90
62-0
...
0
100
FUSING AND SOLIDIFYING POINTS.
MIXTURES OF STEARIC AND MYRISTIC ACIDS.
73
Percentage of
Melting Point.
Stearic Acid.
Myristic Acid.
69-2
100
0
67-1
90
10
65-0
80
20
62\S
70
30
59-8
60
40
54-5
50
50
50-4
40
60
48-2
30
70
47-8
20
80
51-7
10
90
53-8
0
100
1
MIXTURES OF STEARIC AND LAURIC ACIDS.
Melting Point
Perc
Stearic Acid.
69-2
100
67-0
90
64-7
80
62-0
70
59-0
60
55-8
50
50-8
40
43-4
30
38-5
20
41-5
10
43-6
0
Myristic Acid.
0
10
20
30
40
50
60
70
SO
90
100
These tables amply illustrate the peculiarity above referred to
in cases where mixtures are heated — viz., that the melting point
of the mixture is almost invariably lower than that calculated
from the relative proportions and fusing points of the ingredients,
and in certain cases falls below the melting point of the most
OILS, FATS, WAXES, ETC.
MIXTURES OF PALMITIC AND LAURIC ACIDS.
Percentage of
Melting Point.
Palmitic Acid.
Laurie Acid.
|
62-0
100
0
59 -8
90
10
57-4
80
20
54-5
70
30
51-2
60
40
47-0
50
50
40-1
40
60
38-3
30
70
37-1
20
80
41-5
10
90
"?*
0
100
fusible of the ingredients. Thus, in the case of a mixture of
myristic and lauric acids containing equal quantities (50 per
cent.) of each, since the ingredients melt respectively at 58°-8
a-nd 43° -6 C., the melting point of the mixture would a priori be
.. . 58*8 + 43*6 „,„ „ , .. n • o»-o t
expected to be- — T) — = 51 •'!; whereas it actually is 61 *4,
or 13° -8 lower than the calculated temperature, and 6°*2 lower
than the fusing point of the most fusible ingredient.
Dalican's Method. — The following table by Dalican* repre-
sents the solidifying points of various mixtures of pure free
stearic and oleic acids, analogous to those obtained by saponify-
ing tallow completely and separating the fatty acids from the
soaps formed ; these were deduced by determining the tempera-
ture to which the thermometer rose when some 20 grammes of
mixed pure fatty acids were placed in a test-tube at a tempera-
ture a little above the solidifying point, and allowed to cool
slowly ; when incipient solidification became visible the contents
of the tube were stirred with the thermometer immersed therein,
giving a rotary movement three times from right to left, and
three times in the opposite direction ; during this stirring the
thermometer usually slightly fell just at first, but in every case
rose again to a point where the temperature remained stationary
for about two minutes, the disengagement of latent heat during
solidification balancing the loss of heat by radiation and convec-
tion, &c. The temperatures quoted are the stationary ones thus
observed with the various mixtures examined. The joint per-
centages given in the table only add up to 95, the average yield
of total fatty acids from tallow being taken as 95 per cent., after
* Moniteur Scientifique, Paris, 1868.
FUSING AND SOLIDIFYING POINTS.
allowing for small quantities of water present and loss of weight
by elimination of glycerol (vide Chap, vin.) : —
Tf-mporature
Centigrade.
Stearic Acid.
Oleic Acid.
Temperature
Centigrade.
Stearic Acid.
Oleic Acid.
40
35-15
59-85
45-5
52-25
4275
40%")
36-10
58-90
46
53-20
41-80
41
38-00
57-00
46-5
55-10
39-90
41-5
38-95
56-05
47
57-95
37-05
42
40-90
54-10
47-5
58-90
36-10
42-5
4275
52-25
48
61-75
33-25
43
43-70
51-30
48-5
66-50
28-50
43-5
44-65
50-35
49
71-25
23-75
44
47-50
47-50
49-5
72-20
22-80
44-5
49-40
45-60
50
75-05
19-95
43
51-30
43-70
The method of manipulation thus employed by Dalican is
applicable in the case of most other substances the solidifying
point of which is required ; but the amount of rise indicated by
the thermometer above the temperature of incipient solidification
varies considerably in different cases, a constant temperature for
two minutes or more not being always attained. Finkener* finds
that more concordant valuations are obtainable if the vessel
containing the fused fatty matter is enclosed in an envelope of
wadding, or jacketted with a wooden envelope, so as to diminish
the rate of cooling.
Solidifying Point
of Tallow Fatty
Percentage of " Stearine " (Solid Fatty Acids) of Solidification Point
Acids.
'
Degrees C.
48 Degrees C.
50 Degrees C.
52 Degrees C.
54 S Degrees C.
10
3-2
2-7
2-3
2-1
15
7-5
6-6
5-7
4-8
20
13-0
11-4
9-7
8-2
25
19-2
17-0
148
12-6
30
27-9
23-2
21-4
18-3
35
39-5
34-5
30-2
25-8
40
57'8
49-6
43-5
37-0
42 66-6
57-6
50-5
429
44 77-0
66-2
58-4
49-8
46 87-5
75-8
67-0
56-8
48 100-0
87-2
76-6
65-0
50
100-0
87-0
74-5
52
100-0
84-8
54
...
95-3
54-8
100-0
* Journal Soc. Chem. Industry, 18S9, p. 423, and 1890, p. 1071.
OILS, FATS, WAXES, ETC.
De Schepper and Geitel give the foregoing table representing
the amounts of mixed solid fatty acids of different solidification
points practically obtainable from tallow, when these acids are
separated from oleic acid to such an extent as to possess the
solidification points named.
The same authors give the following analogous table for the
relative amounts of mixed solid fatty acids practically obtainable
from palm oil : —
Solidifying Point
of Palm Oil Fatty
Percentage of "
Stearine " (Solid Fatty Acid?) of Solidification Point
Acids.
Degrees C.
48 Degrees C.
50 Degrees C.
52 Degrees C.
55-4 Degrees C.
10
4-2
3-6
3-2
2-6
15
10-2
9-8
7-8
6-6
20
17-4
150
14-4
11-0
'25
26-2
22-4
19-3 16-2
30
34-0
30-5
26-6 22-3
35
45-6
40-8 35-8 29-8
40
63-0
55-2 48-6 40-6
42 70-5
02-2 552 45-5
44 79-2
70-2
62-0 51-4
46
89-4
78-8
69-8
57-8
48
100-0
88-0 78-6 65-0
50
100-0 89-6
73-4
52
100-0 82-8
54
...
92-2
55-4
ibo-o
CHAPTER V.
SPECIFIC GRAVITY AND VISCOSITY.
SPECIFIC GRAVITY OF OILS, FATS, &c.
INASMUCH as the majority of natural oils, fats, and similar sub-
stances are mixtures of more than one constituent, the relative
proportions, and even the nature of the ingredients being subject
to some degree of variation, it results that the general physical
characters of any given oil, £c., are liable to fluctuation within
certain limits. This is particularly the case with the specific
gravity of such materials, differences in the climate and soil
in which seed-bearing plants are grown, in the degree of culti-
vation and the maturity of the crop, and such like causes
SPECIFIC GRAVITY. 77
often producing measurable differences in the relative density of
the oil extracted ; as also, to some extent, does the method
of extraction adopted, the first runnings obtained by pres-
sure in the cold being often perceptibly lighter bulk for bulk
than those obtained later by hot pressure. In similar fashion,
variations in the particular breed of animal (e.g., in the case of
oxen and sheep), the part of the body from which the fat is
extracted, the mode of feeding, &c., often correspond with ana-
logous fluctuations in the case of animal fats ; added to which,
the method of refinement adopted and the degree of purification
effected, cause variations in proportion to the amount of residual
mucilaginous or albuminous matters left unremoved ; whilst the
age of the sample is often a material point, many kinds of oil
having a tendency to absorb oxygen from the air, thereby
becoming more dense.
Notwithstanding these sources of variation, however, it is
often possible to obtain useful information as to the freedom or
otherwise of oils, tfcc., from admixture with adulterating sub-
stances by examining their specific gravity ; or, in many cases,
preferably, the specific gravity of the free fatty acids obtainable
from them by saponification. This determination is most accur-
ately effected by means of the pyknometer* (specific gravity
bottle); but since, excepting in comparatively few special cases
(e.g., butter analysis), a very high degree of accuracy is unneces-
sary on account of the possible natural fluctuations in density,
simpler instruments are in most cases sufficient for the purpose
in view, more especially when checked or "calibrated,"' as de-
scribed below. Thus for most fluid oils the indications of a
fairly well made areometer (hydrometer), used at a standard
temperature, are sufficiently accurate ; whilst either for ordinary
temperatures or for more elevated ones, the hydrostatic balance
is extremely convenient. In using this latter instrument at
higher temperatures (e.g., near that of boiling water V it should
not be forgotten that if the plummet immersed in the liquid to
be examined (as shown in Figs. 11 and 12) be made of glass, it
will displace more than 0'2 per cent, (or upwards of 2 per mille)
more fluid at near the boiling point of water than at 15° f ; so
that if originally constructed to give accurate indications at 15°,
the values indicated at near 100° will be more than 2 per mille
too high on account of the greater displacement ; whence, in the
* For a description of some highly accurate forms of this instrument and
their moie of use, together with a discussion of the corrections indispens-
able when results are required to be accurate to a unit in the fourth
decimal place (± O'OOOl), and a fortiori to one in the fifth place (± O'OOOOl),
vide a paper by the author, Journ. Soc. C/iem. Industry, 1892, p. 297.
t The cubical coefficient of expansion of glass is near '000025 = — - ;
'rL/jUiJiJ
so that a rise of temperature of 85° represents an increment in volume of
o~
= 2-125 per mille.
78 OILS, FATS, WAXES, ETC.
Cease of fluid oils, the specific gravity of which is usually from
•9 to -95, the indications at near 100° will be close to -002 too
high. Analogous errors of excess apply to all glass araeometers
and pyknometers when graduated at one temperature and used
at a higher one.
Another matter to be remembered is that the numerical value
arrived at expresses different things, according as the water with
which the instrument is graduated is at one temperature or
another ; this applies equally to the indications of the pyk-
Fig. 11.
nometer, the araeometer, and the hydrostatic balance. When
the indications represent the ratio between the weight of a given
volume of substance and that of the same weight of water, both
at the same temperature t°, the value is the specific gravity at t° ;
thus the specific gravity at 100° of a given oil or melted wax is
the weight of a given volume of substance compared with that of
the same weight of water also at 100°. If, however, the oil be
at t°, and the water at a different temperature, T, the value is
neither the specific gravity at t° nor that at T. If T = 4° C., the
value is the weight in grammes att°of\ c.c. of oil, since at 4° C.
1 c.c. of water weighs 1 gramme ; this value is often considerably
different from the specific gravity of the oil at £°, the more so
the higher the value of t ; thus if t = 100° 0, since 1 c.c. of water
at 100° weighs 0-9586 gramme, the weight of 1 c.c. of oil at 100°
will be only 0-9586 times the specific gravity of the oil at 100° ;
i.e., the latter value is more than 4 per cent, in excess of the
SPECIFIC GRAVITY. 79
former one. Unfortunately, most observers have recorded their
results in neither of these two forms, but have used a mode of
expression where T is not 4°, and is not = t. Tne result thus
expressed is the relative density of water at t referred to water
at T, sometimes expressed as the relative density at - - ; when
T = 15° -5 C., a temperature frequently chosen, this value' repre-
sents 1-0009 times the weight of 1 gramme of oil at ^ since
1 c.c. of water at 15*5 weighs '9991 gramme.
Fig. 12.
Lefebre's Oleometer. — Fig. 13 represents Lefebre's araeo-
meter, especially intended for oils the specific gravity of which
at 15° -5 ranges from 0*9 to 0*95 ; the instrument is so graduated
that the specific gravity is directly read off when immersed in a
fluid at the standard temperature of 15° -5 ; at various points the
average specific gravities of normal oils of different kinds are
marked off (linseed oil, olive oil, (fee.); usually, to save figures,
only the second and third decimal places are given — i.e., 35
indicates '935, 8 represents -908, and so on. If the tempera-
ture differ slightly from the normal one of 15° -5, a correction is
2
made by adding (or subtracting) - x -001 for every degree of
o
temperature above (or below) the standard, this correction being
based on the fact that most oils expand on heating to nearly the
same extent, so that the specific gravity becomes lowered by
about -00068 per 1° C. (vide p. 93).
80
OILS, FATS, WAXES, ETC.
Fig. 13.
When it is required to deter-
mine the specific gravity of an oil,
&c.j at a temperature somewhat
elevated (say at near 100°), some
form of heating arrangement must
be employed, whereby the vessel
containing the oil, <fcc., can be
constantly maintained at the re-
quired temperature for some time.
Fig. 12 illustrates a form of hot
waterbath thus used for a West-
phal hydrostatic balance.
When temperatures other than
100°, but higher than the ordi-
nary atmospheric temperatures
are required, the hot air arrange-
ment indicated by Fig. 1 4 may be
employed ; in this case the vessel,
C, containing the oil, tfec., to be
examined, is heated by a hot air
bath, B, the ascending hot gases
from a ring burner being made to
circulate as indicated by the
arrows. The temperature of the
inner hot air space is shown by
the thermometer, D, and should
not differ much from that of the
oil itself, as indicated by a ther-
mometer immersed therein (in
the figure, as also in Fig. 12, this
is enclosed inside the plummet*).
A thermostat, or heat regulator
where the gas supply is auto-
matically regulated, should be
employed in addition.
Fig. 15 represents Ambuhl's
arrangement where the vessel
containing the oil is heated in a
current of vapour (steam from
boiling water, or other vapour
emitted by a fluid of convenient
boiling point).
* Fletcher has recently constructed a
thermohydrometer, consisting of an ordi-
nary arteometer with enclosed thermo-
meter, so as to read off the temperature
of the fluid examined simultaneously
with the indicated relative density.
SPECIFIC GRAVITY.
81
Fig. 14.
Fig. 15.
82
OILS, FATS, WAXES, ETC.
In the Paris Municipal Laboratory, a peculiar kind of
" thermal araeometer," constructed by Langlet, is in use for the
examination of olive oil. This is an araeometer with an internal
thermometer, so adjusted that when the instrument is placed in
pure olive oil, the level of the fluid indicated on the stem and
the thermometer reading are practically the same ; if the oil be
warmed so as to become lighter, the hydrometer sinks to an in-
creased depth, and the thermometer column rises through the
same length, so that the two readings always correspond. If,
however, the oil be not genuine olive oil, but contain an admixture
of other oil of different density, the readings will not agree. Thus,
the following pairs of readings correspond with certain oils other
than olive oil and various mixtures (Muntz) : —
Thermometer
Reading.
Reading on
Stem.
Degrees C.
Degrees C.
18-9
11-0
Cotton seed oil, .
, , . * *
18-9
10-5
3 Parts olive oil to
1 of cotton seed oil,
18-1
16-1
2
1
18-6
15-8
3
1 of sesame oil,
18-3
16-5
2
1
18-6
16-1
3
1 of colza oil,
18-3
18-5
3
1 of earthnut oil,
18-1
17-2
2
1
18-7
17-5
52 4
8 ,,
187
17-4
CONSTRUCTION OF TABLES OF ERRORS FOR
HYDROMETERS AND HYDROSTATIC
BALANCES.
Hydrometers, as usually sold, are not infrequently affected by
errors of construction and graduation, sufficiently great to render
their indications inexact to at least ± one unit in the third
decimal place, and sometimes much more, quite apart from any
error arising from the difficulty of reading off the exact level.
To do this with as little error as possible, the hydrometer should
be floated in a jar with a white strip of enamel at its back, or a
strong light so placed that the lowest point of the meniscus
formed by the upper part of the fluid can be read off on the
hydrometer scale. Unless the fluid examined be excessively
dark coloured, this can generally be done pretty readily, the eye
being level with the bottom of the meniscus (as in reading a,
burette).
To eliminate, as far as possible, errors of graduation, it is
SPECIFIC GRAVITY.
83
necessary to construct for each instrument a table of errors,
deduced by directly comparing at the same temperature the
values obtained with different fluids simultaneously examined
by means of an accurate pyknometer, and with the hydrometer.
The following illustration will suffice to indicate the mode of
construction of such a table of errors for a hydrometer intended
to show at 15° '5 C. values ranging between '900 and "950 ; when
such a table is carefully prepared, the corrected reading of a
tolerably sensitive hydrometer should be exact within ± two,
or even ± one unit in the fourth decimal place. The figures are
expressed on the thousandfold scale,* three comparisons being
made respectively near the top, middle, and bottom of the hydro-
meter scale.
True Specific Gravity
at 15° -5 by Pyknometer.
Hydrometer Reading
at 15° 5.
Difference.
948-4
• 924-7
901-1
947-5
925-0
902-5
+ 0-9
- 0-3
- 1-4
From these comparisons the following table of errors is
deduced by interpolation : —
Hydrometer Reading
at ii>0-5.
Correction to be added
to obtain the True
Specific Gravity.
Corrected Specific
Gravity at 15°-t;.
900-0
- 1-50
898-5
905-0
- 1-25
903-75
910-0
- TOO
909-0
915-0
- 0-75
914-25
920-0
- 0-50
919-5
925-0
- 0-30
924-7
930-0
- 0-05
929-95
935-0
+ 0-20
935-2
940-0
+ 0-45
940-45
945-0
+ 0-75
945-75
950-0
+ i-oo
951-0
In similar fashion, a table of errors may be constructed for a
hydrostatic balance ; thus, the following numbers were obtained
with such an instrument of fairly good construction, the values
being here expressed on the ordinary scale, and not multiplied
by 1,000, the temperature throughout being 15°-5: —
* To save decimals, specific gravity values are often quoted after multi-
plication by 1,000 : thus, an oil of specific gravity 0'967 is said " to have
the gravity 967," and so on.
OILS, FATS, WAXES, ETC.
True Specific Gravity
by Pyknometer.
Value indicated by
Hydrostatic Balance.
Difference.
0-9976
0-9517
0-9098
0-8524
0-9995
0-9530
0-9100
0-8520
- 0-0019
- 0-0013
- 0-0002
+ 0-0004
From these determinations the following table of errors is
calculated by interpolation : —
Speciflc Gravity
indicated by
Hydrostatic Balance.
Correction to be added
to obtain the True
Speciflc Gravity.
Corrected Speciflc
Gravity.
0-85
+ -0004
•8504
0-86
+ -0003
•8603
0'S7
+ -0002
•8702
0-88
+ -oooi
•8801
0-89
0
•8900
0-90
- -oooi
•8999
0-91
- -0002
•9098
0-92
- -0005
•9195
093
- -ooos
•9292
0-94
- -0010
•9390
0-95
- -0013
•9487
0-96
- -0014
•9586
0-97
- -0015
•9685
0-98
- -0017
•9783
0-99
- -0018
•9882
1-00
- -0019
•9981
Considerably larger corrections than most of those indicated in
this table have sometimes to be applied to instruments as
purchased, in order to deduce the true specific gravities from the
direct results of observation.
Hydrometer Scales. — A considerable number of more or
less arbitrary scales for araeometers are in use, a circumstance
often leading to much practical inconvenience. The simplest or
"gravity" scale is that where the specific gravity of the fluid
is directly indicated by the level to which the instrument sinks
in the fluid (at the normal temperature) — e.g., in Lefebre's
oleometer (p. 80). Twaddell's scale is not much inferior in
simplicity, each degree on that scale representing an alteration
of 5 units in gravity on the thousandfold scale (p. 83), and the
valuation being given by the formula
S = 1000 + 5n,
where S is the specific gravity on the thousandfold scale, and n
the hydrometer reading ; thus 10° T represents specific gravity
SPECIFIC GRAVITY.
85
1-050; 100° T, specific gravity 1-500; 150° T, specific gravity
1*750 ; and so on. The same rule applies in the case of a fluid
having a density less than that of water, the value of n being
then negative, so that if n = — 10° T, the specific gravity would
be '950, and so on ; the negative-scale Twaddell hydrometer,
however, is but rarely used. A variety of other scales are also
in use, more especially in different parts of the Continent ; the
following table of formulae is given by Benedikt, expressing the
relative values of their degrees, S and n having the same mean-
ings as above : —
Araeometer of
Temperature.
Fluids Heavier than
Water.
Fluids Lighter than
Water.
Balling, .
Beaume,
Beaume,*
Beaume, t
Beck, .
Brix,
Cartier, .
Fischer, .
Gay Lussac,+ .
E. G. Greiner,
Stoppani,§
Degrees.
17 '5 C.
12 -5 C.
15-0 C.
17 "5 C.
12 -5 C.
/12-5R.
\15-625C.
12 -5 C.
/12-5R.
\15-625C.
4C.
/12-5R.
\15-625C.
/12-5R.
\15-625C.
« 200
200
200 - n
144
" 200 + M
144
144 - n
144-3
134 + n
144-3
144-3 - n
146-78
134-3 + n
s 146-78
- 146-78 - n
170
= l70"^i
400
136-78 + n
o 170
170 + n
c 400
~ 400 - n
400
400 - n
100
o =
n
400
400 + n
Q 136-8
126-1 + n
400
400 + n
s = ioo
n
400
400 - n
166
400 + n
166
166 - n
166 + n
*S= -.70 :— for lighter fluids (Schadler).
-1 44 «"> T" ?/•
f S = ul*7S+ n for Hghter fluids (SchUdler).
re for heavier fluids, and = jggqp- for lighter ones (Schadler)
S = j
§ S = ,-7.7, -- - for heavier fluids, and = j^- — for lighter ones (Schadler).
160 — n
160 + n
A)
o
and Hurter (Alkali Maker's Pocket-book) regard the
144-3
36 OILS, FATS, WAXES, ETC.
Lunge
series of values got by means of the formula S = .
144-3 - n
as the only " rational " one of the various Beaume scales in
use; taking the formula at 15° C., the specific gravity of
water at 15° = 0° B. ; whilst 66° B. represents specific gravity
144-3
= 1-8426.
The following table exhibits the relation-
144-3 - 66
ships between the values of " rational " Beaume degrees, Twaddell
degrees, and true specific gravity : —
Beaume.
Twaddell.
Specific Gravity.
Beaumd.
Twaddell.
Specific Gravity.
0
0
1-000
36 -Q
66-4
•332
0-7
1-0
1-005
38
71-4
•357
1-0
1-4
1-007
40
76-6
•383
1-4
2-0
1-010
42
82-0
•410
2-0
2-8
1-014
44
87-6
•438
2-7
4-0
1-020
46
936
•468
4-0
5-8
1-029
48
99-6
•498
5-0
7'4
1-037
50
106-0
•530
6-7
10-0
1-050
52
112-6
•563
80
12-0
1-U60
54
119-4
•597
10-0
15-0
1-075
56
127-0
•635
14-0
21-6
1-108
58
134-2
•671
16-0
25-0
1-125
60
142-0
•710
18-8
30-0
1-150
61
146-4
•732
20-0
32-4
1-362
62
150-6
•753
23-0
38-0
1-190
63
155-0
•775
25-0
42-0
1-210
64
159-0
•795
27-0
46-2
1-231
65
164-0
1-820
30-0
52-6
1-263
66
J68-4
1-842
33'0
59-4
1-297
67
173-0
1-865
RELATIVE DENSITIES OF THE PRINCIPAL
OILS, FATS, <fec.
Many experimenters have published the results of their deter-
minations of the specific gravities of genuine oils, &c. ; in most
instances the observed limits of variation in this respect are not
very wide, being mainly dependent on the freedom from rancidity
and free fatty acids ; the degree of refinement (or freedom from
mucilaginous matter, &c.) ; the age of the sample (whether
oxygen has been absorbed or not), and so on. In many cases a
measurable difference is observable between the density of the
oil first expressed, especially when cold drawn, and that of the
later portions obtained by the aid of heat, the latter being
generally heavier. The following figures are given by Schadler
SPECIFIC GRAVITY.
87
as expressing the average values of the specific gravities at 15°
of a large number of the more commonly occurring vegetable and
other oils : —
Name of Oil.
Oil from Seed of
Specific
Gravity
at 15°.
Almond oil,
Amygdalus communis,
•9190
Arachis oil (earthnut oil), .
Arachis hypogsea,
•9202
Bassia fat (Illipe butter), .
Bassia longifolia, Roxb.,
•9580
Ben oil, ....
Moringa oleifera,
•9120
Belladonna seed oil, .
Atropa belladonna,
•9250
Beechnut oil,
Fagus sylvatica,
•9225
Camelina oil (gold of pleasure),
Camelina sativa,
•9328
Cacao butter,
Theobroma cacao,
•9000
Castor oil, ....
Ricinus communis,
•9667
Cokernut oil,
Cocos nucifera,
•9250
Colza oil, .
Brassica campestris,
•9150
Cotton seed oil (raw),
Gossypium herbaceum,
•9224
,, (refined), .
» »
•9230
Cro^on oil,
Croton tiglium,
•9550
Euonymus oil (spindel oil),
Euonymus europseus,
•9380
Grape seed oil, .
Vitis vinifera,
•9202
Hemp seed oil, .
Cannabis sativa,
•9276
Gourd seed oil, .
Cucurbita pepo,
•9251
Hazelnut oil,
Corylus avellana,
•9154
Linseed oil (raw),
Linum usitatissimum,
•9299
(boiled), .
99 99
•9411
Melon seed oil, .
Cucurbita pepo,
•9251
Madia oil, ....
Madia sativa,
•9350
Mustard oil,
Sinapis nigra,
•9182
Maize oil, ....
Zea mais,
•9210
Nut oil (walnut oil), .
Juglans regia,
•9260
Nutmeg oil,
Myristica moschata,
•9480
Olive oil (greenish yellow),
Olea europsea,
•9144
„ (best quality),
,, (Galipoli), .
>» »«
»> >»
•9177
•9196
Pine oil (red pine seed oil ; "1
pinaster seed oil), . . /
Pinus picea,
•9285
Palm oil, ....
Elais guinensis, &c.,
•9046
Poppy seed oil, .
Yellowhorn poppy oil,
Papaver somniferum,
Papaver glaucium,
•9245
•9250
Plum kernel oil, . . Prunus domestica,
•9127
Radish seed oil, . .
Raphanus sativus,
•9162
Rape oil, ....
Red rape oil,
Winter rape oil,
Brassica napus oleifera,
Hesperis matronalis,
Brassica rapa olifera biennis,
•9157
•9282
•9154
,, (refined), .
» 5 >
•9177
Sesame" oil,
Sesamum orient/ale,
•9235
Sunflower seed oil,
Helianthus annuus,
•9262
Tobacco seed oil,
Nicotiana tabacum,
•9232
Weld seed oil, .
Reseda luteola,
•9358
88
OILS, FATS, WAXES, ETC.
ANIMAL OILS, &c.
Name of Oil.
Source.
Specific
Gravity
at 15°.
Bone fat, ....
Cod liver oil,
(purified),
,, (Labrador),
Mutton tallow, .
Seal oil, ....
Bones,
Gadus morrhua, &c.,
»> > »
Sheep,
Phoca vitulina, &c.,
•9185
•9200
•9270
•9237
•9147
•9246
,, (purified),
Sperm oil, ....
Whale oil (train oil), .
,, (white),
Physeter macrocephalus,
Balsena mysticetus,
•9261
•9115
•9250
•9258
The following determinations of the specific gravity at 15° of
various solid fats, &c., are given by Hager and Dieterich : —
Hager.
Dieterich.
Beef tallow,
•925 to -929
•952 to -953
Sheep's tallow, .
•937 to -940
•961
Hog's lard, .
•931 to -932
Stearine,
...
•971 to -972
Stearic acid (fused), .
•964
,, (crystallised),
•967 to -969
m
Butter fat (clarified), .
•938 to -940
„ (several months old),
•936 to -937
Artificial butter,
•924 to -930
Cacao butter (fresh), .
•950 to -952
•980 to -9S1
, , (very old),
•945 to -946
Beeswax (yellow),
•959 to -962
•963 to -964
„ (white),
•919 to -925
•973
Japanese wax,
•977 to -978
•975
,, (very old),
•963 to -964
...
Spermaceti,
...
•960
Colophony (American),
1-100
1-108
,, (French), .
1-104 to 1-105
Galipot resin (purified),
1-045
Crude ozokerite, .
•952
Ceresin (yellow),
•925 to -928
•922
„ (half white), .
•923 to -924
•920
,, (pure white), .
•905 to -908
•918
The following valuations of specific gravity at 37° '8 C. = 100° F.
are given by Muter * : —
* Spon's Encyclopaedia of Arts and Manufactures, ii., p. 1,469. The
values quoted are the numbers expressing the weights of given volumes of
SPECIFIC GRAVITY.
89
Oil.
Limits of Specific Gravity.
Average.
•8980 to
•9073
•9550
•9103
•9170
•9130
•9114
•9173
•9190
•9076
•9232
•9320
•9052
•9080
•9052
•9150
•9060
•9053
•9136
•8672
•9056
•9109
•9020
•9576
•9152
•9197
•9140
•9220
•9180
•9 i95
•9082
•9300
9440
•9079
•9090
•9079
•9155
•9077
•9065
9195
•8963
•9066
•9056
•9085
•9558
•9176
•9136
•9176
•9179
•9193
•9078
•9252
•9380
•9070
•9085
•9070
•9154
•9067
•9067
•9179
•8724
•9060
Arachis (groundnut) oil,
Castor,
Cotton seed (brown), .
,, (refined — salad oil), .
Cod fish oil,
Lard oil, .....
» (boiled)
Neat's foot,
Nut,
Olive,
Rape,
,, refined (Colza), .
Seal,
Sperm,
Whale,
Since 1 c.c. of water weighs 1-0000 grm. at 4°, -99908 at
l5°-5, and -9933 at 37°'8, these values, when reduced to the
standard of "specific gravity at 37'8 referred to water at 15°'5"
. . . ., .. -9933
be ^ess m the proportion -7^onQ —
*
/ .fl .37°-8\
I specific gravity at -f K'^E ) >
\ lo "O/
i.e., less by 0'58 per cent. ; that is, less by from -0051 to -0056.
If reduced to the standard of " weight at 37°'S in grins.
*9933
per c.c.," tney will be less in the proportion y^/^ — *'•«•» by -67
per cent. ; that is, less by from -0058 to -0064.
Classification of Oils and Fats, &c., according to their
Relative Densities.— The following tables are given by A. H.
Allen,* exhibiting the general classification of oils and fats, &c.,
according to their respective densities ; the relative density at
99°
15° '5 being taken in the case of liquid oils and that at pnr~ in
the case of fats, &c., solid or nearly so at ordinary tempera-
tures : —
oil at 37°'8, referred to the weight of the same volume of water at the same
temperature as unity, and consequently are the true specific gravities at
37 "8 (p. 78). Muter, however, prefers to call them " actual densities ;" an
unfortunate term, as the figures are very different from the true densities.
* Commercial Organic Analysis, vol. ii., p. 89, ct seq.
90
OILS, FATS, WAXES, ETC.
OILS LIQUID AT 15° C.
Specific Gravity at 15°-5 C. = G0° F.
Class of Oil.
•875 to -884.
•884 to -912.
•912 to '920.
•920 to -937.
•937 to '970.
Vegetable
oils.
None.
None.
Olive.
Almond.
Cotton
seed.
Japanese
wood.
Ben.
Sesame.
Croton.
Arachis.
Sunflower.
Castor.
Rape.
Hazelnut.
Linseed
Colza.
Mustard.
Poppy seed.
Hemp seed.
(boiled).
Blown oils
Linseed
(manufac-
(raw).
tured).
Walnut.
Cokernut
oleine
(manufac-
tured).
Essentially
More or less
non-drying
drying oils.
oils.
Terrestrial
None.
None.
Neat's foot.
None.
None.
Animal
Bone.
oils.
Lard and
tallow
oils (manu-
factured).
Marine
Sperm.
None.
Shark
Whale.
None.
Animal
Bottlenose.
liver.
Porpoise.
oils.
Seal.
Menhaden.
Cod liver.
Shark
liver.
Free fatty
None.
Oleic acid.
Linolic
Ricinoleic
acids.
acid.
acid.
Hydro-
carbon
Shale pro-
ducts.
Shale pro-
ducts.
Heavy
Petroleum
None.
None.
oils.
Petroleum
Petroleum
products.
products.
products.
SPECIFIC GRAVITY.
91
OILS, &c., PASTY OR SOLID AT 15°*5C. = GOT.
Arranged according to their Specific Gravity when Melted.
Relative Density at ^~d*
Class of Oil, Ac.
•750 to -800.
•800 to -855.
•8-55 to '863. •{ G3 to '867.
Vegetable
fats.
None.
None.
Palm oil.
Cacao butter.
Palmnut oil.
Cokernut oil.
Japan wax.
Myrtle wax.
Cokernut and
Cotton seed
steariiie
(manufac-
tured).
Animal fats.
None.
None.
Tallow.
Butter fat.
Lard.
Suet.
Dripping.
Bone fat.
Oleomar-
garine
and Butterine
(manufac-
tured).
Vegetable
and Animal
None.
Spermaceti.
Beeswax.
None.
None.
waxes.
Chinese wax.
Carnauba
wax.
Free fatty
None.
Stearic acid.
None.
None.
acids.
Palmitic acid.
Oleic acid.
Hydro-
Paraffin wax.
Shale pro-
Vaseline.
None.
carbons.
Ozokerite.
ducts.
Petroleum
products.
* These relative density values were mostly taken with the plummet
apparatus (Westphal's hydrostatic balance) and not corrected for the
expansion of the glass plummet used ; many of the values are, therefore,
about 0'2 per cent, too high — ».e., too high by nearly *002 (p. 77).
92
OILS, FATS, WAXES, ETC.
Rosin oils and rosin are not included in these tables, these
substances having specific gravities mostly higher than. any
therein mentioned — viz., from '97 to upwards of I'O; similar
remarks apply to some of the highest-boiling petroleum and shale
hydrocarbons.
Variation of Density of Oils, &c., with Temperature.—
Like most other substances, oils and melted fats, ttc., expand
i
Ratio of Weight of a given Volume
of Substance at t°, to that of the i Mean
same Volume of Water at 15° 5
Variation
Name of Oil or Fat, &c.
considered as 1000.
perl0
Alteration in
Tempera-
ture.
J=15-5.
* = 40°-80°.
/=98°-99°.
Arachis oil (groundnut oil), .
Beeswax, ....
922
835-6 at 80°
867-3
822-1
•66
•75
Butter fat, ....
904-1 at 40s
867-7
•62
Castor oil, ....
965-5
...
909-6
•65
Cod liver oil, "...
927-5
...
874-2
•65
Cokernut oleine, . . .
926-2
...
871-0
•67
Cokernut stearine,
...
895 -9 at 60°
869-6
•67
Cokernut butter, .
911 '5 at 40°
873-6
•64
Cotton seed oil,
925
872-5
•63
Doegling oil (bottlenose whale),
880-8
827-4
•64
Japanese wax,
901 -8 at 60°
875-5
•69
Lard,
898-5 at 40°
8608
•65
Linseed oil, ....
935
880-9
•65
Menhaden oil,
932
877-4
•65
Neat's foot oil,
914
861-9
•63
Niger seed oil,
927
...
873-8
•64
Palm butter, ....
893-0 at 50°
858-6
•72
Porpoise oil, ....
926
...
871-4
•65
915
863-2
•62
Seal oil, ....
924
873-3
•62
Sesame oil, ....
921
...
867-9
•62
Spermaceti, ....
835 -Sat 60°
808-6
•72
Sperm oil, ....
883-7
830-3
•65
Tallow,
895'0 at 50°
862-6
•67
Whale oil, ....
930-7
872-5
•70
Paraffin wax,
780-5 at 60°
753-0
•72
Commercial "stearine" \
(crude stearic acid), . . j
...
859-0 at 60°
8305
•75
Commercial "oleine" ( im- \
pure oleic acid), . . /
903-2
848-4
•66
on heating ; it is somewhat remarkable that nearly all bodies of
this description expand at about the same rate (within not very
wide limits of departure from the average), so that 1 c.c. of
substance always increases to about 1*00075 c.c. by rise of tem-
perature of 1° C. The effect of this on the density is to diminish
it in the inverse proportion; so that an oil, &c., the specific
SPECIFIC GRAVITY. 93
gravity of which at 15° is from '9 to '95, will become diminished
•9 *95
in specific gravity to i<0uU75 to 1.QQ()75 by rise of 1° in tempera-
ture— i.e., the diminution in the specific gravity is -00067 to
•00071. Thus the preceding values were obtained by A. H.
Allen ; * for the sake of convenience, and to avoid decimals,
all the figures are multiplied by 1,000.
From these values it results that whilst glyceridic oils fluid
at the ordinary temperature diminish in specific gravity between
15° and 98° C. at close to the average rate of -64 per 1° (uncor-
rected for plummet expansion ; somewhat more when corrected),
glycerides of higher melting point (like Japanese wax and palm
butter) and waxes (beeswax, spermaceti, paraffin wax) diminish
in specific gravity at a slightly higher rate, averaging about 0*7
per 1°. In all cases, however, the rate is sensibly near to
2
^ x -001 per 1° C., reckoned on the usual specific gravity scale
(water =1) and not multiplied by 1,000.
Figures closely concording with these have been subsequently
obtained by other experimenters ; thus 0. A. Crampton f found
for various samples of lard, lard stearine, beef fat, oleostearine,
cotton seed oil, and olive oil, coefficients of expansion between
15° and 100° lying between -000715 and '000797, averaging close
15°
to -00075. Since the relative density at — of these substances
was found to lie between -9065 and -9220, the average decrement
in density per 1° C. rise in temperature was close to 0-69 on the
thousandfold scale. W. T. Wenzell found J that olive oil,
mustard seed oil, castor oil, sperm oil, and cod liver oil expanded
to almost exactly the same extent in each case between 16°*7 and
44° -4 C. (62° and 112° F.) ; the increment in bulk being 2 per
cent., all the substances being examined in the same dilatometer.
This represents an apparent coefficient of expansion per 1° C.
of -00072, which, when corrected for the expansion of the glass,
becomes -00075, or practically the same figure as that found by
Crampton ; and indicating an average decrement in density
per 1° C. rise in temperature of 0-68 to 0-69. On the other
hand, Lohmann states § that 1,000 volumes of olive oil increase
* Commercial Organic Analysis, vol. ii., p. 17, et seq. The values at
the higher temperatures were mostly obtained by a plummet apparatus
(Westphal's hydrostatic balance), and not corrected for the expansion of the
glass plummet used, the object being simply to make comparative estima-
tions ; hence many of the figures in the last column are somewhat too low
by about -01 to -02 (vide p. 77).
•^Journ. Soc. Chem. Ind., 1889, p. 550 ; from Amer. Chem. J., 11., p. 232.
J Analyst, 1890, p. 14.
§Schadler's Technologic der Fette und Oele, 2nd edition, edited by
Lohmaun, p. 91.
94 OILS, FATS, WAXES, ETC.
by 0'83 volumes for 1° C. rise of temperature ; whilst the
analogous increment for rape oil is 0*89, and for train oil, I'OO;
figures perceptibly higher than those found by the other observers
above mentioned.
YISCOSIMETRY.
In order to obtain valuations of the so-called " viscosity " of
oils, &c., as approximate measurements of their relative lubricat-
ing powers, two classes of methods are in use — viz., those where
the measurements are made by observing the mechanical effects
produced by applying the oil, &c., between two conveniently
arranged surfaces in motion with respect to one another; and
those where the oil to be examined is made to pass through a
given tube or orifice, and the time of passage of a known quan-
tity is noted. From the practical point of view, obviously the
most valuable measurements of the kind are those obtainable by
imitating as nearly as possible the conditions under which the
lubricant is to be used — i.e., the power of overcoming friction is
best measured by a testing machine precisely similar to that for
which the lubricant is required ; quick moving spindles, rapidly
revolving axles in journal boxes, or heavy slow moving shaft-
ing, &c., being employed as occasion requires. Such measure-
ments, however, can only be properly carried out in compara-
tively large establishments, and are not at all adapted for use in
laboratories where the chemical nature of the oils is investigated
and their general characters tested ; accordingly, in these cases,
methods of the second kind are now usually employed, since ex-
perience has shown that the comparatively small sized mechanical
testing machines of various kinds that have been invented for
the purpose are apt to give results more discordant amongst
themselves, and less faithfully representing the actual lubricating
values of the substances examined, than those obtained by
apparatus for the determination of " efflux velocity " (incorrectly
designated " viscosity ").
Of the numerous simpler forms of mechanical testing arrange-
ments that have been proposed, one of the earliest (M 'Naught's
pendulum machine) is also one of the least unsatisfactory ; this
consists of two discs, the lower one provided with a raised edge
and attached to a vertical spindle revolving in bearings, the
upper one resting on a pivot. The space between the two discs
is filled with ' the oil to be tested, and the lower one made to
revolve at a given speed. The friction due to the oil would in
time cause the upper disc to revolve too ; but this motion is
prevented by means of a projecting pin in contact with a
pendulum. In consequence, more or less pressure on the pen-
dulum is produced, diverting it from a vertical position; the
degree of displacement affords a measure of the resistance of
the oil.
VISCOSIMETRY.
95
Efflux Method. — The simplest arrangement for making com-
parisons between different oils, &c., as regards their efflux
velocities, consists of an ordinary pipette
filled up to a given mark on the stem
with the oil to be tested, the time being
noted requisite for the oil to run out
either completely, or down to some
lower mark. Fig. 16 represents an in-
strument on this principle devised by
Schiibler, the upper part of the pipette
being expanded into a reservoir, with a
scale attached indicating the level to
which the fluid sinks ; for comparative
observations, the reservoir is filled to a
given level, and the time determined
during which the level sinks to a given
extent, (a) in the case of the substance
tested, (b) in the case of some other
substance taken as standard.
The time ratio thus deduced does not
represent the relative time for equal
weights, but that for equal volumes ; so that
ratio for equal weights the value
16.
to deduce the
must be multiplied
by -j?, where d± is the relative density of the substance examined,.
al
and d.j that of the standard substance. Thus if the substances
contrasted were sperm and rape oils, and the respective time&
requisite for the same volume to flow out were 40 and 120
seconds, whilst the relative densities were -880 and -915 re-
spectively, the relative efflux rate for. equal weights would
be
h d,_ J0_xj915 _
t2 ~dl 120 x -880
As the time of efflux varies markedly with the temperature
(usually diminishing as the temperature rises), such comparisons.
must necessarily be made under constant conditions as to tem-
perature.
In order to ensure uniformity of temperature in different
experiments the results of which are to be compared together,
the vessel containing the oil may be conveniently surrounded
with a jacket containing water or melted paraffin wax. Fig. 17
represents an arrangement of the kind described by E. Schmidr
also containing a device for maintaining a constant pressure
during the outflow, instead of having a continually varying
" head," as in Schiibler's instrument. The vessel containing the
oil, A, is a sort of pipette, excepting that the upper end consists
96
OILS, FATS, WAXES, ETC.
of a tube, B, passing down inwards to a point, F, near the base
of the expanded part. The upper end of B is closed by a stopper,
R
Fig. 17.
D, so that when the stopper is in, no air can enter, and, con-
sequently, no oil runs out at G ; but on removing the stopper the
VISCOSIMETRY.
97
oil flows out. The pipette is filled by removing the stopper,
inverting it with the end BD immersed in the oil, and sucking
up at the other end, G, until full, when it contains some 50 c.cs.
The stopper being replaced, the pipette is fixed in position inside
the water jacket, heated to the required temperature in the
ordinary way by means of the projecting tube ; a stirrer, R, with
an annular plate at the end is provided ; by moving this up and
down the temperature is equalised. When the required tem-
perature is attained the stopper is withdrawn and the time
ascertained requisite for a given volume of oil to run out; as
long as the level of the oil in the pipette does not fall below F,
the pressure or " head " under which the oil issues at G is mani-
festly constant, being that due to a column of oil of length, GF.
By employing high-boiling paraffin oils, <fec., in the water jacket,
the relative efflux times at high temperatures can thus be readily
determined for various oils.
7
98
OILS, FATS, WAXES, ETC.
With all instruments of this description a variable amount of
friction is brought into play as the oil passes through the efflux
pipe, especially when this is conical ; so that varying results are
often obtained with different instruments. This source of error
is best avoided by doing away with the efflux tube altogether,,
substituting for it a hole drilled in a plate of glass or agate.
Redwood's Efflux Viscosimeter. — Figs. 18 and 19 repre-
sent Boverton Redwood's form of viscosimeter, consisting of an
interior silvered copper cylinder, about 1^ ins. diameter and
3^ ins. deep> containing the oil to be examined ; the bottom
of this is furnished with an orifice, consisting of a hole bored
through an agate plate, the top of which is excavated into a
hemispherical cavity, so that a small brass sphere attached to a
rod and dropped in forms a sufficiently tight valve. An outer
Fig. 19,
jacket is provided with a closed copper tube projecting therefrom
downwards at an angle of 45°, so that by heating this "tail" in a
Bunsen or spirit lamp flame, the temperature of the liquid (water,
oil, melted paraffin wax, &c.) in the jacket can be raised as
required. A revolving agitator to equalise temperature in the
jacket is provided, with a thermometer attached, a second ther-
mometer being supported in the oil by a clamp fixed to the
cylinder. The whole rests on a tripod stand furnished with
levelling screws. The constancy of initial level of oil inside the
VISCOSIMETRY.
99
cylinder is assured by means of a gauge consisting of a small
internal bracket with upturned point.
When an observation is to be made the bath is filled with
water, or heavy mineral oil, etc., and heated to the required tem-
perature. The oil to be tested is also heated to this temperature
and poured in until the level of the liquid just reaches the point
of the gauge. A narrow-necked flask, holding 50 c.cs., is placed
beneath the jet immersed in a liquid at the same temperature
as the oil. When all is ready the ball-valve is raised and a
stop-watch started, and the number of seconds requisite to fill
Fig. 21.
the 50-c.c. flask noted, care being taken that the temperature
does not fluctuate during the time, and that the oil is per-
fectly free from suspended matter, such as dirt or globules of
water.
In order to obviate the necessity of always using the same
volume of oil (indispensable in order to end with the same
difference of level, and consequently maintain the same average
head or pressure throughout), A. H. Allen makes an addition
100
OILS, FATS, WAXES, ETC.
consisting of an airtight cover, Fig. 20, perforated by two holes,
one of which, A, is furnished with a tap, B, while the other has
another tube screwing airtight into it. This tube, C, is pro-
longed on two sides in contact with the agate orifice, whilst the
angles of the inverted V-shaped slits cut on each side terminate
at D, exactly 1} inches higher. The cylinder is completely
filled with oil before commencing an observation, the tap, B,
closed, and the orifice opened till the oil sinks to the level of D
Fig. 2>2.
in the inner tube. Air then bubbles regularly in at D ; when
this happens, the temperature is noted and the oil collected in a
graduated receiver. Any volume from 10 to 50 c.c. can thus be
run out, as the oil falls in the upper part of the cylinder, but is
maintained constantly at the level, D, in the inner tube. Five
consecutive valuations of 10 c.c. each may thus be made, whilst
50 c.c. run out.
VISCOSIMETRY. 101
Several other forms of viscosimeter have been constructed by
other experimenters, based on the efflux principle. Fig. 21
represents in section Engler's instrument ; a slightly modified
form of this by Engler and Kiinkler* is largely used on the
continent.! Fig. 22 represents a simple form recently constructed
by G. H. Hurst.; The oil, &c., to be examined is run into the
innermost vessel up to a given height determined by a gauge-
pin, and heated up to the required extent by applying a Bunsen
burner or spirit lamp to the heater at the side, connected by two
tubes with the water reservoir surrounding the oil chamber, so
as to heat the water by circulation. The temperature of the oil
is observed by means of a thermometer placed therein (usually
this registers about 6° F. below the temperature of the water in
the jacket); when the required temperature is reached, the
central valve is raised, and 50 c.c. of oil allowed to run out into
a measuring flask underneath, the time of efflux being noted.
Obviously, with this instrument, the head under which the
liquid issues is continually diminishing as it flows.
Standards of Efflux Viscosity. — In actual practice, water is
too fluid to be a convenient standard substance ;. rape oil is
usually chosen in preference, because, notwithstanding the un-
avoidable differences that exist between samples from seeds
grown in different countries and soils, these differences are
usually not extremely wide. Definite mixtures of pure glycerol
and water, however, can be readily prepared, possessing almost
any required higher degree of " viscosity," § and capable of use
as standards of comparison of considerably greater uniformity,
when prepared by different operators at different times, than is
possible with natural products such as rape oil.
The following tables are selected from the numerous results
published by various authorities, as illustrating the general
character of the numbers obtained with " viscosimeters " of
different kinds for determining the relative efflux rates of
different natural oils, &c., and lubricants made therefrom, or
from petroleum and other hydrocarbons, and the effect of varia-
tions of temperature 011 the values. The figures obtained by
* Journ. Soc. Chem. Industry, 1890, p. 654; from Dinyler's polyt. Journ.,
276, p. 42.
t A still more recent form is described by Engler, with special in-
structions for its use (Journ. Soc. C/icm. Ind., 1893, p. 291 ; from Zeits.
ang. Chem., 1892, p. 725).
$ Journ. Soc. Chem. Industry, 1892, p. 418.
§ With the viscosimeter above described, Boverton Redwood finds that
the relative times requisite for 50 c.c. of water and genuine rape oil to flow
out at the temperature of 150'5 C. (60° F.) are 25'5 and 535 seconds
respectively, taking the average of various samples of pure oil. A. H. Allen
rinds that glycerol diluted with water until the specific gravity at 15 '5 is
1'226, possesses the same degree of viscosity as average rape oil when
tested in the same way.
102
OILS, FATS, WAXES, ETC.
Schiibler represent the " viscosity degree " (viscositdtsgrad) or
" relative viscosity " of the respective oils — i.e., the relative
times requisite for equal volumes to pass (at 70<5 and 15° C.
respectively), the times required by the same volume of water-
being taken as unity ; those quoted from the other authorities
are not thus reduced, but are simply the actual times directly
observed with the particular instruments used : —
^ ;iine of Oil.
Relative Time in Seconds (Schiibler).
Plant from which derived.
At~c'5C.
At 15°-0 C.
Castor oil,
liicinus communis,
377-0
203-0
Olive oil,
Olea europaea, 31 '5
21-6
Hazelnut oil
Corylus avellana. 24*2
18-4
Colza oil,
Brassica campestris oleifera,
22-4
18-0
Rape oil,
Brassica rapa oleifera biennis,
22-0
17-6
Beechnut oil
Fagus sylvatica,
26-3
17-5
White Mustard oil,
Sinapis alba,
24-0
17-4
Almond oil, .
Amydalus communis,
23-3
16-6
Spindlenut oil,
Kuonymus europaeus, 23 '3 15 '9
Black mustard seed oil,
Sinapis nigra,
19-4
15-6
Poppy seed oil, . . Papaver somniferum,
18-3
13-6
Camelina seed oil,
Myagrum sativum,
17-7
13-2
Belladonna seed oil,
Atropa belladonna,
17-3
13 1
Sunflower oil,
Helianthus annuus, 16*4
12-6
Turpentine oil,
Pinus sylvestris,
16-7
11-8
Cress oil,
Lepidimn sativum,
14-4
11-4
Grape seed oil,
Vitis vinifera,
14-2
11-0
Plum kernel oil, .
Primus domestica,
14-7
10-3
Tobacco seed oil,
Nicotiaua tabacum,
13-5
10-0
Walnut oil, .
Juglans regia,
11-8
9-7
Linseed oil, .
Linum usitatissimum,
11-5
9-7
Hemp seed oil,
Cannabis sativa,
11-9
9-6
Relative Time in Seconds (Wilson).
Oils, &.C., Used.
At 15«"6 C.
At 49° C.
At 82° C.
= eo° F.
= 120C l'\
= I80°F.
Sperm oil, ....
47
30-5
25-75
92
37'75 28-25
Lard oil, .... 9(j
38
28-5
Rape oil
Neat's foot oil,
108
112
41-25
40-25
30
29-25
Tallow oil, ....
143
37
25
Engine tallow,
Solid.
41
26-5
YISCOSIMETKY.
VISCOSITY IN SECONDS FOR 50cc.
10;
~te
II
»
t _
S * I
104
OILS, FATS, WAXES, ETC.
Rifintd Rape Oil
Sperm Oil
American Miueitil Oil, sp. gr. -885 .
,. '913
•923 .
Kiuritm , -009 .
. -915 .
.IM no too too goo aio zso
230 290 300 itc
1 Fig. 24. — Temperature in Degrees Fahrenheit.
Oils Employed.
, Sperm oil,
Seal oil (pale),
, Northern whale oil,
Menhaden oil,
Sesame oil,
1 Arachis oil,
Cotton seed oil (refined),
Niger seed oil,
Olive oil,
Rape oil,
Castor oil,
Relative Time in Seconds (Allen).
Spec. Grav.
at 150>5C.
•881
At ln°T.C.
= 60° F.
At r>o° C.
= 122« F.
At 100° C.
- 21'-'° F.
so
I
47
38
•924
131
56
43
•931
186
65
46
•932
172
40
•921
168
65
50
•922
180
64
...
•925
180
62
40
•927
176
59
43
•916
187
62
43
•915
261
80
45
•965
2420
330
60
I
VISCOSIMETRY.
105
Relative Time in Seconds (Redwood).
50° F.
70° F.
100° F.
140' F.
200SF.
260° F.
300° F.
Refined rape oil, No. 1,
712-5
405
147
105-5
58-5
4325
2
...
406
146
106-5
57-5
...
" ," £
...
405-5
147
106-5
57-5
...
» 4,
...
407
147-5
106
58-5
...
Beef tallow,
54-75
40
Sperm oil,
...
136-8
60-5
50-75
42
34-75
30
Neat's foot oil, .
620
366
126
88-4
50-4
44
38
American mineral oil, |
specific gravity, '885 j
145
90
47
41
,,.
American mineral oil, 1
specific gravity, '923 \
Russian mineral oil, \
1,030
2,040
485
820
126
174
82
116
42
48-5
...
specific gravity, '909 J
Russian mineral oil, }
semisolid, . . J
...
... 531
317-5
99-25
5925
42 -G
Redwood's results are indicated graphically by the curves
indicated in Figs. 23 and 24.
Castor oil,
Thickened rape oil,
Sperm oil,
Colza oil,
Whale oil, .
Tallow oil, .
Cotton oil,
American 885 oil, .
American 905 oil, .
American 915 oil, .
Scotch 865 oil,
Scotch 885 oil,
Scotch 890 oil,
Russian 906 oil,
Russian 911 oil,
Rosin oil, dark,
Rosin oil, pale,
Cylinder oil, medium,
Cylinder oil, pale,
Cylinder oil, dark,
Relative Time in Seconds (Hurst).
70° F.
100° F.
120° F.
150° F.
180° F.
1,248
487-5
201-5
91
48
1,370
331-5
279-5
156
78-5
58-5
36-4
26
19-5
17
131
56,
44
325
28
128-7
61
44
28-5
28
105
63,
45
30
20
100
55
40
25
20
68
3->
23
15
14
113
44
32-5
19-5
18
140
47
36
21
19-5
325
22
18
15-5
13
58-5
26
22 18
15-5
71-5
39
26
195
17
292-5
97-5
56
30
22
462
143
91
82-5
26
1525
97-5
38
22
18
136-5
49-4
25
18
17
385
255
170
70
...
405
265
120
90
...
890
495
230
100
As further illustration of the effect of rise of temperature in
diminishing the rate of efflux, the following figures may also be
106
OILS, FATS, WAXES, ETC.
quoted, obtained by Villavecchia and Fabris, whilst investigating
certain lubricating oils* for excise purposes: —
Lubricating oil.
No. 1
n
3
4
5
6
7
Efflux Rate referred to Water at
At 20° C.
At 50° C.
44-39
6-81
51-07
5-94
40-85
5-50
38-77
6-03
72-09
8-35
67-92
9-6(5
56-03
5-71
Thus, the effect of a rise in temperature from 20° to 50° is to
diminish the efflux rate to -J- - -^ of the original value, the effect
being more marked with the more viscous fluids.
According to experiments by Bender, f when an oil is chilled
to - 20° for some time, and then warmed up again, the efflux
viscosity value at the ordinary temperature is often considerably
increased as compared with what it was previously at the same
temperature of observation, thick oils usually showing a greater
increment than thinner ones. On the other hand, if oils are
heated up to 50° or 100°, and then allowed to cool down again
to the air temperature, the thicker oils become perceptibly
thinner, whilst the thinner oils are less affected.
Lepenau's Leptometer. — This instrument is based on a
principle somewhat different from that involved in the above
^described forms of efflux viscosimeter, inasmuch as it depends not
only on the rate of flow through a given orifice, but also on the
.amount of surface tension called into play when drops are formed
in air. It consists essentially of a pair of precisely similar
•cylinders, B B (Fig. 25), immersed in the same bath, A, one of
which contains the oil to be examined, and the other another oil
used as standard of comparison ; the relative rates are noted at
which drops form as the oil passes through equal sized capillary
tubes, r, r, the dimensions of which are too small to permit of
continuous streams being produced, the quantities flowing out in
a given time being weighed or measured.
All these various forms of instrument are subject to one
constant source of error — viz., that the forces coming into play
* " Report of the Central Laboratory of the Italian Customs' Depart-
ment, 1891 ; also Journ Soc. Chem. Industry, 1891, p. 390.
t Journ. Soc. Chem. Industry, 1891, p. 936; from Mitth. Konig. techn.
Versuchs,, Berlin, 1891, p. 100.'
VISCOSIMETRY.
107
when a viscous liquid passes through a tube or orifice under
given conditions of temperature, &c., are not the same as those
obtaining when the liquid is used as a lubricant for shafting,
quickly rotating spindles, axles, and the like ; and, consequently,
that the figures obtained by means of such testing appliances are
only approximations (and not always
close ones) to the relative values
of the substances examined, when
practically applied for lubricating
purposes.
Determination of Viscosity in
Absolute Measure.-When liquids
are examined possessing a compara-
tively low degree of viscous charac-
ter, the rate of flow through a narrow
orifice does not represent the true
physical "viscosity," because a large
proportion of the result is due to
flow pure and simple without any
" shear ; " accordingly, when a com-
paratively long narrow accurately
calibrated tube is made use of as
the jet, figures are obtained not
always showing close agreement
with those yielded by the ordinary
forms of efflux apparatus. Accord-
Fig. 25.
ing to mathematical investigations by Poiseuille and others, the
coefficient of friction in narrow tubes is given by the formula
where 75 is the coefficient of friction, t" the time of efflux, v the
volume of fluid discharged, p the hydraulic pressure, I the length
and r the radius of the capillary tube, and s the specific gravity
of the liquid.* Starting from this, E. J. Mills has made some
measurements in absolute measure of the coefficients of friction
for various liquids, including water, and sperm, olive, lard, and
-castor oils.f
On the C.G.S. system (centimetre, gramme, and second as units
of length, mass, and time respectively) Poiseuille's formula becomes
* Hagenbacli arrives at a formula involving a second term in addition to
that given by Poiseuille —
t Joiirn. Soc. Chem. Ind., 188C, p. 148; also, 1887, p. 414.
108
OILS, FATS, WAXES, ETC.
where v is given in cubic millimetres, and r, I, and p in milli-
metres ; from this formula and his experimental results, Mills
deduces the following values at 12° 0. : —
Specific Gravity.
Value of »j.
Rehitive Viscosity,
Water =1.
Water,
1 -000
•011713
i-oo
Sperm oil, .
•88789
•68828 5876
Olive oil,
•1)2043 1-1393 97-27
Lard oil,
•92051 1-6285 139 '03
Castor oil, . . . -915541
21-721
1854-4
Obviously these relative viscosity values are very dissimilar
from Schiibler's numbers for castor and olive oils compared with
water, although the ratios between the values for the oils alone
do not differ so widely in the two cases ; this chiefly arisen
Fig. 20.
from the error attaching to the viscosity determination in the
case of water by the efflux method through a jet, as compared
with the true value through a long narrow tube.*
* The determinations of absolute " viscosity " values of solutions of gum
relatively to water made by noting the times required for given volumes to
pass through a known capillary tube, show similar differences when compared
with the corresponding values obtained with a "jet" apparatus, such as a
burette (vide paper by S. Rideal, Journ. Soc. Chem. Ltd., 1891, p. 610).
VISCOS1MKTRY.
109
Coefficient of Friction in Capillary Tubes. — Traube has
constructed an arrangement for determining with considerable
accuracy and speed the friction coefficients for oils and other
liquids passing through capillary tubes under pressure. Fig. 26
represents this apparatus.* A is a Marriotte bottle filled with
water, which serves to compress air in the reservoir B, and to
keep the pressure constant ; B is connected by means of a pipe
and cock to the efflux apparatus H, consisting of the bulb G-
(provided with two marks to permit the measurement of volume
of liquid to be discharged) and the capillary tube E. The
reservoir B is filled by means of a pump attached to branch and
stopcock. When the observations are to be made at temperatures
above that of the atmosphere a suitable airbath is employed.
When required to be cleaned, ether is forced through the tube.
With tubes of different diameters, the relative times observed for
water and oils of high viscosities are not identical ; but for oils
of considerable viscosity the differences are not great ; thus, the
following figures were observed with a cylinder lubricating oil
and with olive oil as compared with rape seed oil, being the
respective times of efflux in seconds : —
Diameter of tube in milli- \
metres, . . . J
1-5
0-8
0-5
Cylinder oil, .
155 -5 -100-0
472=100-0
2960=1000
Rape seed oil, .
79-0= 50-8
242- 51-3
1503= 50-8
Olive oil, ....
717- 46-1
222= 47-0
1364= 46-1
In all probability the conditions existing when oil is forced
through a capillary tube are more nearly akin to those obtaining
with a film of oil lying between a shaft and its journal box than
are those subsisting in the ordinary forms of efflux viscosimeter ;
and hence it is probable that the results of valuations on
Traube's system would be valuable as determinations more
closely approximating to the actual practical lubricative values.
Traube s apparatus, however, is far less convenient for ordinary
laboratory work than Redwood's or Engler's viscosimeter.
* Journ. Soc. Chem. Ind., 1887, p. 414.
110 OILS, FATS, WAXES, ETC.
§ 3. Chemical Properties of Oils, Fats,
Butters, and Waxes.
CHAPTER VI.
PROXIMATE CONSTITUENTS AND THE METHODS USED
FOR THEIR EXAMINATION AND DETERMINATION.
VERY few, if any, natural oils, fats, and waxes consist of one
single chemical substance ; almost invariably two, and often
many more constituents are present, the most marked distinc-
tion between which is that some are solid at the ordinary tem-
perature (when obtained separate), others liquid; the former
often deposit in the solid form on chilling, so that a fluid oily
when chilled and pressed, yields a solid so-called " stearine" and
a liquid so-called " oleine " * as first proximate constituents. In.
similar fashion semisolid butters and hard fats, like tallow, can
be showrn to contain a solid and a liquid constituent in each case,
the consistency of the material, roughly speaking, depending
simply on the relative proportions of the two substances. When
"oleine" largely predominates the substance is an oil; when
'* stearine," a hard fat ; and when the two are in intermediate
* The terms "stearine" and "oleine" are practically employed in
several different senses, a circumstance apt to lead to considerable con-
fusion. In the strict chemical sense, stearine is the glyceride of stearic acid,
C8Hfi(O.Ci8H35O)8j and oleine the glyceride of oleic acid, CaHsCO.CjaHssOJa ,
but in the oil trade generally the two terms are applied to indicate respec-
tively the solid and liquid constituents into which a fat or chilled oil can
be mechanically separated, irrespective of the actual chemical composition
of these constituents ; whilst in the candle manufacture they are used to
denote the analogous solid and liquid fatty acids obtainable from fatty
matters by saponification and mechanical pressure, &c. Similar mixtures of
free fatty acids and other substances are also obtainable by subjecting to
distillation various kinds of grease (e.g., Yorkshire grease — Chap, xn.) ;
when these are chilled aud pressed they are separable into solid and
liquid portions, generally designated as "distilled" stearine and oleine
respectively. In the present work the pure chemical triglycerides are dis-
tinguished by the terminal "in" (e.g., stearin, olein, &c.) ; whilst the
commercial articles are indicated by names ending in "ine" (e.g., " dis-
tilled " oleine, candlemakers' stearine, oleomargarine, &c. ). In similar
fashion, the pure chemical compound C3Hr,(OH)3 is referred to as-
" glycerol," whilst the commercial products mainly consisting of this body,
but in a varying state of purity, are distinguished as glycerine (vide p. 8).
PROXIMATE CONSTITUENTS. Ill
proportions, a more or less buttery consistence is possessed at the
ordinary temperature (near 15° C.)
The further investigation of the solid and liquid constituents
thus obtainable from a given oil or fat ; of the variations in their
relative proportions and natures according to the soil and climate
and other conditions under which the plant was grown in the
case of vegetable oils or butter, or the species and habitat of the
animal in that of an animal oil or fat ; of the eifect of cultivation
and domestication, and various similar points, have hitherto
received but little attention. There appears, however, to be
some reason for supposing that very considerable differences in
the relative amounts and even in the chemical nature of the
various constituents of a given oil, &c., may, at any rate in some
cases, be brought about by such causes ; thus, very different
results have been found by various experimenters who have
examined different samples of the same kind of oil — e.g., in
the case of arachis oil (groundnut oil), where several succes-
sive chemists have succeeded in isolating considerable amounts
of hypogceAc acid for the purpose of studying that substance
and its derivatives, whilst more than one other chemist has
found either none at all, or practically none, in the oil ex-
amined by him ; and where, moreover, some observers have
found more or less considerable amounts of palmitic acid, and
others none at all. Similar discrepancies in the results obtained
by different investigators have been noticed in several other
instances, thus leading to the conclusion that marked differences,
are apt to exist in the nature of oils and fats prepared from
seeds, &c., grown under different conditions, just as is well
known to be the case with fruits and other vegetable produce, as-
regards the saccharine matter and other constituents present
therein. Even without taking into account these natural varia-
tions, however, the knowledge at present extant of the proximate
constituents of many of the more commonly occurring oily and
fatty matters is decidedly scanty ; whilst a very large number of
similar substances exist (in many cases of great local importance,
although not always materials largely exported or imported or
otherwise dealt with commercially) concerning the general com-
position of which accurate knowledge is hitherto entirely want-
ing. Many such products promise in the near future to be
important articles of trade, as soon as their respective values for
particular purposes are better ascertained, and the best means,
to be adopted of extracting and refining them so as to render
them marketable ; in Central and Southern Africa, and in many
other parts of the world, the progress of civilisation is continually
tending to bring into notice new products of this kind, many of
which only require attention being called to them to demonstrate
their commercial value.
The separation from one another of the different glycerides,
112 OILS, FATS, WAXES, ETC.
<fec., contained in a given " stearine " or " oleine " is, in most
cases, a very difficult problem, more especially if required to be
performed in such a fashion as to give an approximate idea of the
relative proportions in which they are present. As a rule, the
best results are obtained by saponifying the mixture, and
applying methods for the separation of the resulting fatty acids,
•either by mechanical means (chilling and pressing out the
more liquid portions) or by chemical processes. For example,
the lead salt of oleic acid is soluble in ether, whilst lead stearate,
palmitate, &c., are practically insoluble in that medium ; so that
l)y converting into lead salts the mixture of free fatty acids
obtained on saporiification and acidulation, and treating the mix-
ture with ether, a partial separation may be effected, lead oleate
with comparatively small quantities of stearate, palmitate, &c.,
being dissolved out, and lead stearate, palmitate, etc., with small
quantities of adhering oleate being left. With a mixture of solid
iatty acids (palmitic, stearic, arachic, tkc.), fractional crystallisa-
tion from alcohol of the mixed free acids ; fractional precipitation
.as insoluble salts (of lead, magnesium, &c.); fractional crystal-
lisation of certain salts (e.g., magnesium salt) from alcohol or other
•appropriate menstruum ; and similar processes are applicable in
various cases ; but the complete examination of mixtures of fatty
iicids in this way is so laborious, that it has been thoroughly
carried out in but very few instances. In the case of fractional
precipitation, as a general rule, the acid of higher molecular
weight precipitates first; thus, with a mixture of arachic, stearic,
und palmitic acids in approximately equal proportions, precipi-
tated as salts in several fractions, the first fraction will be
chiefly a salt of arachic acid, and the last will contain little
besides palmitate.
Some oils and fats contain appreciable quantities of the
glycerides of acids of sufficiently low molecular weight to be
volatile along with the vapour of water at the ordinary atmo-
spheric pressure. In such a case, after sapoiiification and acidula-
tion, an acid distillate is obtainable by boiling, preferably by
Mowing through the mass a current of steam from a suitable
generator. The weakly acid aqueous fluid may then be neutralised
with an alkali, evaporated to a small bulk, and decomposed by a
mineral acid ; or converted into silver or barium salts, &c., and
further examined. If more than one volatile acid be present, a
separation may often be effected by fractional precipitation as
silver salt, &c. ; or enough mineral acid may be added to liberate
a fraction of the total organic acids from the evaporated solution
of alkaline salts, and the distillation repeated ; the acid of lowest
molecular weight will then pass over. By similarly liberating
successive fractions and distilling alternately, a series of distillates
will be obtained, the acids of higher molecular weight being
•contained in the respective later fractions (Liebig).
PROXIMATE CONSTITUENTS. 113
When a mixture of acids volatile with steam and others not
volatile therewith is present, if, instead of blowing steam through
the whole mass, the insoluble fatty acids be allowed to float up
in a fused condition, and are then removed (after cooling and
solidifying), the remaining aqueous liquor is often found to
yield perceptibly less volatile acid, a portion having been dis-
solved by the insoluble acids, much as ether dissolves out various
substances from aqueous solution when agitated therewith. In
consequence of this, it is often impossible to obtain a constant
weight of the insoluble fatty acids thus obtained on drying at
100°, unless they have been repeatedly treated with boiling water,
so as to remove soluble constituents (vide Chap. VIIL, " Hehner
Number"); otherwise, the small quantity of volatile acid present
slowly evaporates, giving a continual small loss. In some cases,
this by and by becomes balanced by gain in weight through
oxidation (by spontaneous absorption of oxygen from the air),
and later 011 still the gain from this cause predominates.
By means of superheated steam the fatty acids of higher
molecular weight may be pretty readily distilled; but any-
thing like a complete separation of closely related homologous
acids (e.g., myristic, palmitic, and stearic acids) in this way by
processes of fractional distillation is difficult, if not impossible ;
and the same remark applies to distillation under greatly dimin-
ished pressure (in a partial vacuum). In some cases fractional
saturation with alkali, £c., of a mixture of acids will cause a more
or less complete separation, one combining with the base to the
exclusion of the other: more often the base becomes shared between
the two in proportions depending on the relative masses present.
Thus Thum found * that when a mixture of equal weights of
stearic and oleic acids is dissolved in hot alcohol and treated
with a quantity of alcoholic potash sufficient to saturate only
one half of the total acids, a mixed soap is obtained, which (when
separated from the uncombined excess of fatty acids by means of
petroleum ether) consists substantially of equal quantities of
potassium stearate and oleate ; the free acids similarly consisting
of stearic and oleic acids in sensibly the same proportion.!
A good deal still remains to be done in the case of a consid-
erable number of vegetable oils in the way of identifying and
quantitatively estimating their various proximate constituents;
and much the same remarks apply to certain animal oils, more
especially " train oils " from marine cetaceans, as regards not
only the acids present but also the alcoholiform constituents ;
*Zeit*ch.f. ancjeic. Chemie, 1890, p. 482.
t A similar state of matters is observed when a given fatty acid acts on
a mixture of caustic potash and caustic soda ; both potash and soda soaps
result in proportions sensibly near to those in which the two alkalies are
present in the mixture ; and not one kind of soap to the exclusion of the
other (vide Chap, xxi.)
8
114 OILS, FATS, WAXES, ETC.
whilst it is known that certain of these oils are mainly composed
of compound ethers of non-glyceridic character, which furnish on
saponincation acids mostly of the oleic family, and as comple-
mentary products, alcohols of moderately high molecular weight
(e.g., dodecatylic alcohol, C12H26O, from Doegling oil), the complete
investigation of the products thus formed has been attempted
in very few instances indeed, and much still remains to be done
in this field ; it appears, however, that besides alcohols of the
ethylic series, others of a non-saturated character are also present
in some of these oils, as the alcoholiform constituents extracted
are in many cases capable of combining with iodine, leading to
the conclusion that higher acrylic alcohols are also contained as
compound ethers in addition to cetylic alcohol homologues.
Free Fatty Acids and Higher Alcohols contained in
Natural Oils and Fats, &c. — Owing to the presence of mucila-
ginous, albuminous, or gelatinous matters in most crude vegetable
oils expressed from seeds, or animal fats and oils obtained from
animal tissues, it generally happens that a perceptible amount
of hydrolysis of glycerides is brought about in the process of
extraction, due to the influence of these substances and the
fermentative changes rapidly undergone by them ; even when
solvents (such as light petroleum oil, carbon disulphide, or ether)
are used for the isolation of the oil, &c., it not unfrequently
happens that measurable amounts of free fatty acids are con-
tained in the product obtained ; leading to the conclusion that
hydrolytic actions naturally take place to a greater or lesser
extent in the seeds, tissues, &c., during crushing and analogous
operations, or even on simply keeping, so that small quantities
of free acids are practically always present in the natural
products as obtained on a manufacturing scale from the animal
after death, or from the seed after detaching from the plant,
even when not normally present in the living animal or
growing vegetable. The extent to which actions of this sort
take place is extremely variable ; in general the " cold drawn "
oils expressed from seeds, and the corresponding first runnings,
from fresh fish livers, and the more liquid "oleomargarine,"
obtained by the action of gentle heat on animal fats, contain
much smaller proportions of free fatty acids than the later
fractions obtained by subsequent hot pressing and analogous
operations ; whilst in the case of vegetable oils the maximum
amounts of free fatty acids are contained in the oils extracted
by solvents from oilcakes, and in those obtained from vegetable
pulps (pounded nuts, crushed olives, and such like) by heating
with water so that oily matter floats up, separated by skimming —
i.e., in those cases where contact with fermentible matters has
been most intimate and prolonged. Thus, the following figures
were obtained by Noerdlinger,* the total fatty matter being
* Journ. Soc. Cfiem. Ind., 1890, p. 422, from Zeit*. Anal Chfm., 29, p. 6.
PROXIMATE CONSTITUENTS.
115
extracted from the seeds by means of light petroleum spirit, and
the free fatty acid (determined by titration with phenolphthalein.
as indicator) reckoned as oleic acid (vide p. 117) : —
103 Parts
contain
Free Fatty
Oils.
Acids Reckoned
per 100 of Total
Free Fatty
Acids.
Total Fat.
Fat.
Rape (jBras.nca rapct),
0-42
37'75
MO
Cabbage (B. c.ampestris), .
Poppy (Papover somni/eritm) , .
0-32
3-20
41-22
46-90
0-77
6-66
Earthnut (Arachis hypoy<ea) \
seed, /
1--91
40-09
4-15
Earthnut (Arackift hypogcva) \
outside pale husk, . J
1-91
4-43
43-10
Sesame (Sesamum orientate), .
2-21
51-59
4-59
Castor (Riclnus communit"),
1-21
46-32
2-52
Palmnut (Elais guinenxis) }
containing 6 per cent, husks, J
4-19
49-16
8-53
Cokernut (Cocos nucifera),
2-98
67-40
4-42
Oil Cakes.
Rape, . ...
093
8-81
10-55
Poppy, . ...
5-06
9-63
58-89
Earthnut,
1-42
7-65
18-62
Sesame, . ...
6-15
15-44
40-29
Palmnut, . ...
1-47
10-39
14-28
Cokernut,
1-31
13-11
10-51
Linseed, . ...
0-75
8-81
9-75
Castor, . ...
1-27
653
2007
Obviously, when oil contains any considerable quantity of free
fatty acids the use of alkaline refining processes (Chap, xi.) is apt
to lead to a considerable diminution in the quantity of refined
product obtained, as compared with the raw material employed,
because the free fatty acids are removed in the form of soaps, the
production of which, moreover, often leads to further loss by
the mechanical en tangling of " neutral " oil in .the saponaceous
" foots."
The presence of free fatty acids in any quantity in most
kinds of oils is detrimental to their value, more especially in
reference to certain applications. Thus, in the case of lubricating
oils, corrosion of bearings, etc., is more apt to be brought about
when free fatty acids are present than when the oil is practically
free therefrom ; and hence in such cases alkaline refining pro-
cesses will often give a superior result, the more so that acid
processes are apt to communicate to oil refined thereby traces of
mineral acid, the corrosive action of which is still more marked.
This is notably the case with oils intended for wool spinning and
116 OILS, FATS, WAXES, ETC.
analogous purposes. Colza oil containing much free fatty acids
burns less freely, and is more apt to char the wick than com-
paratively neutral oil. On the other hand, the taste of olive oil
is said to be considerably improved by the presence therein of
small quantities of free acids ; whilst largely hydrolysed oils
(kuiles tournantes] are intentionally prepared for certain special
purposes in the textile and dyeing industries.
In the case of blubber oils largely consisting of the compound
ethers of higher monatomic alcohols of the ethylic series, the
hydrolytic actions taking place during storage before and after
extraction, and whilst the "rendering" is taking place, lead to
another result — viz., that cetylic alcohol and analogous bodies are
largely contained in the oils ultimately obtained ; thus, from 30
to 40 per cent., and sometimes more, of so-called " unsaponifiable
matter " is frequently found to be present in sperm and other
blubber oils, chiefly consisting of alcoholiform products of
hydrolytic actions of this description. Similar remarks apply
to beeswax, and to the various vegetable waxes of analogous
constitution ; figures are on record, obtained by various analysts,
indicating in extreme cases that from J to § of the original
compound ethers have been hydrolysed by actions of this
description, either occurring naturally during storage, or in con-
sequence of the processes adopted in preparing the raw material.
DETERMINATION OF FREE FATTY ACIDS.
FREE ACID NUMBER.
The most accurate process for determining the amount of free
acids contained in a given sample of oil or fat, consists in agitating
it with warm alcohol, and dropping in a standard alkaline solu-
tion (preferably alcoholic) until a persistent pink coloration
appears after continued agitation, phenolphthalein being the
indicator ; the temperature must be high enough to render the
fat perfectly fluid. Or the oil may be dissolved in cold ether,
mixed with a little alcohol, and the solution titrated with
standard alcoholic alkali. If the mean equivalent weight of
the free fatty acids is known (or assumed) to be E, the pro-
portion of fatty acids in the free state is given by the formula,
x = JLX^ x 100,
w
where w is the weight in milligrammes of material taken for
examination, n the number of c.c. of normal alkali used,* and
x the weight of free fatty acids contained in 100 parts of sub-
stance (percentage of free fatty acids) ; for since 1 c.c. of normal
* If seminormal (or decinormal) alkali be used, the value of n will
obviously be * (or Y1^) of the number of c.c. used, and so on.
DETERMINATION OF FREE ACID NUMBER. 117
alkali represents E milligrammes of fatty acids, the^total weight
of acids contained in w milligrammes of substance is n x E
milligrammes, whence 100 parts of substance contain - — x 100
parts of free fatty acids.
In many instances the value of E is not known accurately,
and in such cases it is more convenient to express the amount
of fatty acids in terms of the alkali neutralised. This may be
done with respect to 100 parts of original substance, thus giving
the percentage of potash (or soda) neutralised, according to the
alkali employed ; but a more usual practice is to express the
value relatively to 1,000 parts of original substance, potash
(caustic potash, KOH, equivalent 56'1), being selected as the
alkali, thus giving the permillage of potash neutralised, con-
veniently referred to as the "free acidity potash permillage," or
"free acid neutral' sation number," or, more shortly, as the " free
acid number," and expressed by the value - x 56,100.*
Thus, suppose that 10 grammes (10,000 milligrammes) of palm
butter neutralise 8 c.c. of seminormal alkali, equivalent to
4'0 c.c. of normal alkali ; since 1 c.c. of normal alkali corre-
sponds with 56-1 milligrammes of KOH, and with 256 milli-
grammes of palmitic acid (i.e., E = 256 j, the result may be stated
by saying that the " free acidity potash permillage "or " free
acid number " is JQ-^K x 56,100 = 22*44; or it may be expressed in
terms of percentage of palmitic acid by saying that the substance
4*0 x *^J56
contains free acids jointly equivalent to _ ooo" x ^^ = l^'-M
per cent, of palmitic acid.
When only small quantities of free acid are present, and
extremely sharp valuations are desired, somewhat large quantities
of material should be taken for the determination ; 20 or 25
grammes, or even more. A less accurate method of determining
free fatty acids consists in shaking up the oil, &c., with alcohol,
allowing to stand, separating a known fraction of the alcoholic
fluid, and titrating with standard alkali ; the result is apt to be
somewhat too low on account of incomplete solution of all free
acid by the alcohol.
In some natural oils (e.g., unrefined cotton seed oil) substances
are present of an acid character, although not belonging to the
* Since 1 c.c. of normal alkali represents 56'1 milligrammes of KOH, n c.c.
represent n x 56 '1 milligrammes: then if A be the free acid number as
above defined,
w : n x 56'1 : : 1,000 : A
whence A= — x 56,100.
118 OILS, FATS, WAXES, ETC.
ordinary fatty acid series, but more resembling the acids of pine
resin ; these substances neutralise alkali (phenolphthalein being
the indicator), and are consequently included in the total of "free
fatty acids " determined by titration. Occasionally ordinary
rosin (colophony) is intentionally added to oils or the fatty acids
thence derived, either as an adulterant or for special reasons —
e.g., in the manufacture of some kinds of waggon grease and
"yellow " soap. For the methods used in determining the amount
of resin present in such cases, vide Chap. xxi.
When it is required to separate the free fatty acids from the
neutral fat, this is readily accomplished by adding alcoholic
alkali until just neutral to phenolphthalein, diluting with water,
and agitating with ether, or better, with light petroleum spirit.*
The ethereal liquid on evaporation leaves the neutral fatty
matter, which can be weighed and further examined as desired ;
the aqueous fluid is acidulated and shaken with petroleum spirit,
&c., whereby the free fatty acids are similarly obtained.
If mucilaginous matter, &c., is also present, the oil may be
ground up in a dish with half its weight of solid sodium car-
bonate and as much water, and dried on the waterbath ; the
residue is again stirred up with coarsely powdered pumice-
stone, and exhausted with ether containing no alcohol, whereby
the neutral fat is dissolved out. The residue is exhausted with
hot alcohol, and the resulting soap solution evaporated and
decomposed by a mineral acid, so as to obtain the free fatty
acids, originally present as such, free from the other constituents.
Or the fat, &c., may be treated with ether, carbon disulphide, or
other solvent ; by filtering through a weighed filter and washing
the insoluble matter thoroughly, the mucilage, &c., is obtained,
whilst the filtrate may be evaporated, and the resulting mixture
of neutral fat and free fatty acid further examined as required.
Burstyn's Method. — A physical method of approximately
determining the amount of free acid contained in oil (more
especially olive oil) has been devised by Burstynf for use in
cases where titration by chemical means is inconvenient or
impracticable. 100 c.c. of the oil to be tested are placed in a
stoppered cylinder capable of holding 200 c.c.; this is then filled
up to the mark with alcohol of 88 to 90 per cent., and the whole
well shaken, and allowed to stand two or three hours. The alcohol
floats up, having dissolved out most of the fatty acids together
with a minute amount of oil ; the increase in specific gravity is
determined by testing the upper layer with a highly delicate
araeometer, a similar cylinder of the original alcohol used being
simultaneously examined side by side. By the aid of a table
* In presence of alcohol ether is apt to take up into solution small
quantities of soap, as well as neutral fat.
t Dingier 's Polyt. Journal, ccxvii., p. 314; also Journal Chem. Soc.,
vol. i. (1876), p. 769.
DETERMINATION OF UNSAPONIFIABLE CONSTITUENTS. 11-9
the amount of free fatty acid is deduced from the increment in
specific gravity indicated, the table being so constructed as to
allow for the solubility in alcohol of the neutral oil, etc. Apart
from the error introduced by the possible presence of varying
amounts of phytosterol, or other vegetable substances more or
less soluble in alcohol, a very slight difference in temperature
between the vessels containing the alcoholic oil solution and the
pure alcohol used for comparison produces a great effect on the
result. The table is usually arranged so as to show the number
of " Burstyn degrees " of free acid — i.e., the number of c.c. of
normal alkali neutralised by the free acid contained in 100 c.c.
of the oil examined. "One degree" consequently represents
0-282 gramme of oleic acid per 100 c.c., or close to 0'3 per cent,
by weight.
DETERMINATION OF UNSAPONIFIABLE
CONSTITUENTS.
The unsaponifiable matters contained in many oils and fats
to the extent of a few tenths per cent., are most conveniently de-
termined by saponifying the oil with alcoholic alkali, evaporating
off the spirit, and dissolving out matters soluble in such solvents
as ether, chloroform, carbon disulphide, light petroleum spirit,
«fec., either by means of an extraction arrangement, such as the
Soxhlet apparatus described in Chap, ix., or by adding water and
agitating with the solvent. Ether frequently dissolves a small
amount of soap ; on the other hand, small quantities of oil
often escape saponification, and are thus extracted ; so that it
is always preferable to boil a second time with alcoholic alkali
the residue left on evaporating off the solvent, and repeat the
extraction process with the product. The extraction by means
of a Soxhlet arrangement is generally facilitated by placing some
sand or powdered pumice-stone in the evaporating vessel em-
ployed, and rubbing up therewith the residual soap left after
evaporating off the alcohol ; the solvent thus obtains more easy
access to the matters to be dissolved out, and the operation is
effected more quickly and thoroughly.
In the analysis of soaps similar methods are often employed ;
the soap to be tested is reduced to thin shavings which are
then cautiously dried, first at a comparatively low temperature
(50°-60° C.), later on at steam heat or a little above, so as to
drive off all moisture without fusing the mass. The dried
shavings, coarsely powdered, are packed in the Soxhlet tube
and exhausted with solvent, preferably light petroleum ether;
in this way unsaponified fat contained in the soap, cholesterol
and analogous substances derived from the oils and fats em-
ployed, waxy matter or hydrocarbons (e.g., paraffin oil) added to
120 OILS, FATS, WAXES, ETC.
the soap, or contained in the materials (e.g., in distilled oleins),
and similar constituents are all dissolved out, giving a solution,
the residue left on evaporation of which is further examined ;
whilst the purified soap is also subjected to analysis.
The modification of Soxhlet's extraction apparatus described
by Honig and Spitz (Chap, ix.), is often very convenient for dis-
solving out the unsaponifiable constituents soluble in ether, light
petroleum spirit, &c., after heating with excess of alcoholic alkali,
evaporating off the spirit, and dissolving in a minimum of water.
The use of petroleum spirit is preferable, as although it often
dissolves out a little soap (though usually less than ether), this
may be readily removed by agitating with a mixture of equal
quantities of alcohol and water (50 per cent, spirit), when the
petroleum solution free from soap floats up. Moreover, ethereal
liquids often form froths that remain permanent
without separating properly for many hours
or even days ; petroleum spirit is less liable to
this inconvenience.
In cases where a portion only of the ethereal
or other solution is intended to be drawn off,
this is readily effected by running the solution
and watery fluid into a graduated vessel, into
the mouth of which a doubly perforated cork is
fitted, with a washbottle-like arrangement of
tubes (Fig. 27, Chattaway). The upper and
lower levels of the ethereal liquid being read off,
the cork and tubes are inserted, and air blown
in so as to force out some of the ethereal solu-
tion into a weighed dish in which it is sub-
sequently evaporated, the quantity thus drawn
off being known by withdrawing the tubes and
reading off the difference of level of the top of
Fig 27 the ether stratum. When sharp results are re-
quired, about 90 to95per cent, of the ether should
thus be withdrawn, and the remainder diluted, say tenfold, by add-
ing more ether; the bulk of this is similarly forced out, so that the
remaining ether only represents a small percentage of the original
ethereal solution. Thus, suppose that the original ethereal fluid
measures 58 c.c., of which 52 are removed by the first blowing
out, leaving 6. This is diluted to 60, and another 50 c.c. blown
out, leaving 10 of the more dilute liquid, representing 1 of the
original solution, or 1 x — — = 1'72 per cent, thereof. Then
Oo
100 - 1-72 = 98-28 per cent, of the original solution has been
blown off, so that the weight of the residue obtained therefrom
58 100
by evaporation must be increased in the proportion -^= = ^T^TT-
0 i i/o **jO
Oils, &c., adulterated with any considerable proportion of
DETERMINATION OF UNSAPONIFIABLE CONSTITUENTS. 121
hydrocarbons (paraffin, petroleum, rosin oil, &c.), or similar
mixtures intentionally prepared for lubricating purposes, «fec., are
easily separated by the above treatment ; when the fatty acids
contained in the saponifiable constituents are required to be
further examined, they are readily isolated by dissolving in hot
water the soap thus freed from hydrocarbons, and acidulating
with a mineral acid.
Blubber oils containing the glycerides of higher ethylic alcohols
(cetylic alcohol, &c.) when thus treated yield to the solvent the
alcoholiform constituents set free during saponification ; when
these are mixed with hydrocarbons the proportion of alcohol
present may be arrived at by means of the hydrogen test (p. 13),
or the acetylation test (Chap, viu.)
When only minute quantities of unsaponifiable matters are
contained in a given oil or fat, &c., these are generally either
substances akin to cholesterol and phytosterol dissolved in the
oil, or else matters of mucilaginous or albuminous character
either dissolved in the oil or suspended in a diluted jelly-like
form therein. The former, when dissolved out from the soap
resulting after saponification by such solvents as ether or benzo-
line, may often be obtained in a crystallised condition by
dissolving in hot alcohol and cooling, or may be converted
into benzoic or acetic ethers, &c., and identified either by the
melting point or the " acetyl number." The latter are left un-
dissolved ; on decomposing the soaps with a mineral acid they
form flocculent masses, from which the pure molten fatty acids
are readily separable by filtration through a dry paper filter after
separation from the aqueous liquor. Some oleaginous matters,,
extracted by solvents (such as carbon disulphide) from certain
vegetables, seeds, &c., or from certain kinds of animal fatty
matter, contain complex bodies of the nature of lecithin, a sort
of compound ether of choline, glycerophosphoric acid, and fatty
acids (oleic and stearic) ; phosphorised constituents of this kind
are largely contained in the oily matter from the yolks of hens'
eggs, and to a lesser extent in that from the seeds of certain
leguminous plants, e.g., peas (vide p. 123).
Matters of a saponaceous character are sometimes contained
in commercial oils, owing either to the use of basic sub-
stances in refining (especially in boiling drying oils), whereby
more or less considerable amounts of metallic soaps are formed
and partially dissolved by the oil ; or to other causes, such as the
intentional addition of metallic soaps (aluminium, magnesium,
zinc, ttc.) for the purpose of increasing the viscosity of lubricating
oils ; or simultaneous contact with air and metals, whereby a
metallic oxide is formed, which then is either dissolved as
metallic soap, in virtue of free fatty acids present, or reacts on
the glyceride, forming metallic soap by saponification. Oils that
have been in contact with copper or brass are often rendered
122 OILS, FATS, WAXES, ETC.
green by the formation of copper soap in this way ; similarly,
drying oils that have been " boiled " with metallic oxides as
driers (e.g., lead oxide) generally contain more or less metallic
soap in solution thence derived. Such admixtures, whether
intentional or not, can generally be estimated by diluting the oil
with ether free from alcohol, and filtering, when the metallic soap
is left undissolved ; by decomposing this with dilute nitric acid
the metallic constituents are obtained as nitrates. In most
<jases prolonged agitation of the oil with highly dilute nitric acid
suffices to dissolve out the metallic oxides present as soaps, and
in this way errors are avoided due to solubility of metallic soaps
in the ethereal solution of oil.
Oils containing lead or copper are more or less blackened by
shaking up with a few drops of sulphuretted hydrogen water, or
dilute solution of ammonium sulphide. Preferably a mixture of
equal volumes of glycerol and water is used to dissolve the
sulphur compound employed, as this then acts more readily on
the oil.
Oils containing potash and soda soaps in solution generally
yield these more or less completely to water when shaken up
therewith, so that by allowing to stand and separating the
aqueous liquid, the soaps dissolved therein can be obtained by
evaporation to dry ness.
Water contained in Oils, &c. — Although " oil and water "
are conventionally regarded as immiscible substances, still their
mutual insolubility is in most cases relative rather than absolute.
Water in general dissolves extremely little oil or fat ; but the
converse does not hold so closely, as a few tenths per cent, of
water can generally be retained in permanent solution by fluid
oils, &c., without impairing their transparency. In the case of
semisolid substances (e.g., butter and lard), much larger
quantities of water can be mechanically intermixed with the fat
in the form of minute globules interspersed throughout the mass ;
but in this case there is no true solution, and on gently warming
the mass so as to melt the fatty matter, the water gradually
separates out to the bottom, so that if the operation be effected
in a graduated vessel, the volume of water thus separating may
be by and by read off. In some cases, the separation of the
water in this way is facilitated by adding to the just-fused mass
a sufficient quantity of light petroleum spirit to prevent it
solidifying on cooling, and setting by the whole in a corked-up
graduated tube for some time, so as to allow the water globules
to collect and run together. The amount of admixed water may
also be determined by heating a known weight of substance to a
temperature a little above 100° C. (by means of an airbath, &c.),
and noting the loss of weight.
When the actually dissolved water is to be determined, the
same process may be used; preferably, however, the oil, <fcc., to
DETERMINATION OF UNSAPONIFIABLE CONSTITUENTS. 123
be examined is not heated in contact with air, but is placed in a
weighed U tube, through which a current of dry carbon dioxide
gas is passed, to prevent oxidation by absorption of oxygen from
the atmosphere during the heating.
Adulteration of Fats with Suspended Matters. — Solid and
semisolid fats (lard, tallow, Arc.,) are sometimes intentionally
adulterated by admixture with white weight-giving substances,
such as china-clay, starch, &c. To determine the quantity arid
nature of the adulterants present in such cases, the fat, £c., is
thinned with carbon disulphide or other volatile solvent, and
filtered through a dry weighed filter. The filtrate and washings
being evaporated to dry ness, and the residue dried in a steam
bath, the proportion of actual fat present is known ; the increment
in weight of the filter represents the solid adulterant, and the
deficiency in weight the water. The residue on the filter turns
blue if starch is present (flour, meal, farina, (fee.); cold water
dissolves out common salt and such like saline matters (e.g., in
salted butters, &c.) ; kaolin and sand are left behind on incinera-
tion, whilst albuminoid and caseous matters, cellulose, mucilage,
and other vegetable non-fatty extractives are burnt off during the
process. Oils that have been refined by means of sulphuric acid
and retain minute quantities of free inorganic acid, when thus
treated with a solvent and filtration, leave on the filter paper
a minute amount of residue soluble in water with acid reaction ;
this may be titrated with deciiiormal alkali in the usual way.
Sulphurised and Phosphorised Constituents. — Certain
oils, more especially those derived from cruciferous plants (rape,
camelina, mustard, horseradish, cress, &c.), contain small quan-
tities of sulphurised constituents, such as thiocyanic ethers ; the
presence of these may be qualitatively tested by heating the oil
with concentrated potash solution, whereby potassium sulphide is
formed; the mass, after dilution with water and separation of
the aqueous liquor, gives a brown or black coloration with
potassium plumbate. In some cases, heating the oil to "boiling"
with a bright strip of silver causes the latter to blacken. To
•determine the amount of sulphur, the oil is dissolved in sulphur-
free petroleum or alcohol, and burnt in the manner employed in
determining sulphur in coal gas, the flame being enclosed in a
chimney connected with an aspirator, and absorbing tubes filled
with moistened glass beads being interposed, so as to condense
sulphur dioxide and trioxide along with the water formed by
the combustion; a tray with fragments of solid ammonium
carbonate is fixed over the flame, to furnish an ammoniacal
atmosphere ; the condensed liquid is oxidised with bromine
water, and precipitated with barium chloride and hydrochloric
acid (Allen). Or the oil may be cautiously heated with alcoholic
potash, evaporated, and the residue incinerated with addition of
potassium nitrate till white, the sulphate formed being determined
124 OILS, FATS, WAXES, ETC.
as usual. This latter method is also available for the estimation
of phosphorus, present in certain oils and fats as a compound of
the nature of lecithin, the phosphorus being ultimately weighed
as magnesium pyrophosphate (Benedikt).
The following general scheme for the examination of oils and
fats, &c., is applicable in most cases so far as the above mentioned
impurities or constituents are concerned : —
Dry a convenient quantity so as to determine the amount of
water present (p. 122).
Melt a known weight of fat and pass it through a hot weighed
filter, finally washing out the adherent fat with ether ; the
residue left on the filter may contain saline matters, suspended
organic impurities, dust, tfec., &c., which may be further ex-
amined as occasion requires. On incinerating the filter, the
amount of inorganic suspended matter is obtained. Part of the
filtered oil, &c., may be shaken successively with water to dis-
solve out alkaline soapy matters, and with dilute nitric or
sulphuric acid in case any lead, copper, or other metallic soaps
are present, the watery and acid liquors being separated and
examined. The oil may advantageously be diluted with ether
or carbon disulphide, &c., previously to agitation with water, <fec.
Another part of the filtered oil is diluted with warm alcohol, and
the free acid number determined (p. 116), using phenolphthalein
as indicator ; the alcohol is evaporated and the residue taken up
with light petroleum spirit, &c. ; the residual soap formed from
the free acid is examined as required (Chap, xxi.) for fatty acids,
resin acids, <fcc. Aluminium and other metallic soaps may also be
here present, precontained in the oil.
The light petroleum spirit solution 011 evaporation gives a
residue containing neutral oil, hydrocarbons, and unsapoiiifiable
matters, £c. ; this is saponified with alcoholic alkali, and the pro-
duct diluted with water and shaken with ether or petroleum
spirit; the ethereal solution is evaporated and the treatment
with alcoholic alkali repeated to ensure complete saponification ;
finally, the hydrocarbons, &c., are dissolved out by ether or
petroleum spirit, and the watery solution of glycerol and fatty
acid soaps further examined by acidifying and separating the
fatty acids ; these usually constitute 95 to 96 per cent, of the
original glycerides (Chap, vin.)
EFFECT OF HEAT ON OILS. 125
CHAPTER VII.
CHEMICAL REACTIONS OF OILS, FATS, &c., AND
THEIR USES AS TESTS OF PURITY, &c.
EFFECT OF HEAT ON OILS, &c.
WHEN fixed oils, &c., are subjected to heat, decomposition is
sooner or later brought about ; if the oil is a glyceride, acroleiri
(acrylic aldehyde, C2~H3.COH) is generally evolved, so named on
account of the acrid character of its vapour. In some cases the
fatty acid originally present as glyceride is also volatilised un-
changed in greater or less quantity ; but in general, destructive
distillation only takes place. If the heating be carried out in
presence of water vapour, as when superheated steam is blown
through the mass, in many cases hydrolysis takes place, fatty
acids and glycerol being produced, which more or less completely
pass off along with the water vapour ; on this action are based
certain processes for the manufacture of free fatty acids for candle
making, £c., and for preparing pure glycerol.
When drying oils, more especially linseed, poppy, and walnut
oils, are heated for the purpose of preparing " boiled " oil for the
manufacture of paint, ttc., and particularly when the action is
pushed to a great length, as in the manufacture of printing
ink, the glyceridic portion of the compounds appears to be
almost completely decomposed, the linolic acid or anhydride
developed being more or less dehydrated (and probably poly-
merised) in such fashion as to form a highly viscid or rubber-like
mass. Oxidation by direct addition of oxygen so as to form
oxylinolic acid and derivatives thereof usually occurs simul-
taneously, more especially in the " blowing " process of preparing
boiled oils.
Flashing Point. — The determination of the temperature at
which inflammable vapours are given oif (whether by simple
volatilisation, or in consequence of decomposition) in sufficient
quantity to take fire by the application of a light to the mixture
of air and vapour contained in the upper part of the heating
vessel, is a somewhat important operation in the case of many
oils intended for lubricating and other purposes, where they are
liable to be considerably heated ; with animal and vegetable oils
the " flashing points " are generally high, but much lower num-
bers are often given by mixtures containing hydrocarbon oils,
such as paraffin oil and petroleum distillates, rosin oils, and such
126
OILS, FATS, AVAXES, ETC.
like products. For the determination of the flashing point of
petroleum distillates and similar substances, several special forms
of instrument have been devised by different experimenters ; in
some of the earlier forms the vapour emitted from the warmed
oil was allowed free access to the air ; this mode of operating was
known as the " open test," and was subject to serious irregulari-
ties according to the way in which the heating was conducted,
and so on. In the later instruments the top of the heating vessel
is closed in to prevent the escape of inflammable vapours when
first generated ; in consequence a considerably lower tempera-
ture is registered by the application of the " close test," whilst
the sources of fluctuation in the results are much lessened.
Fig. 28 represents Abel's
flashing point apparatus,
used in Britain as the legal-
ised appliance for testing
petroleum, £c., under the
Petroleum Act. Similar ar-
rangements are in use in
other countries with minor
modifications, partly as to
the construction of the in-
strument itself, and partly
as to the exact details of
manipulation to be observed
during use ; for as the tem-
perature values deduced are
liable to slight fluctuation
with variations in the mode
of heating, etc., a definite
prescribed mode of operating
must be strictly adhered to.
Abel's apparatus consists of
a cylindrical metal cup, Af
placed inside another with an
Fig. 28. air-space between, the outer
one being surrounded by a
water bath, B, heated by a lamp, K, underneath. rlhe oil to be
tested is carefully poured in without splashing until just level with
the top of the gauge, C, 1 J inches from the bottom of the cup, the
water in the jacket being at the temperature 130° F. = 540<4 C.,
as shown by the thermometer, H. The lid of the cup, D, is then
put on, the temperature of the oil being known by means of the
thermometer, E. A small lamp, G, is arranged at the top of the
cover, swinging on an axis, in such a fashion that when a slide
covering an aperture in the lid is drawn aside, the lamp flame is
made to pass over the aperture. As the contents of the cup
slowly heat up, the slide is withdrawn at regular intervals of
EFFECT OF HEAT ON OILS.
127
time, governed by the swinging of a pendulum ; by and by, the
inflammable vapours are given off in sufficient quantity to yield
a flash of blue flame by their kindling when the slide is with-
drawn ; the temperature then indicated by the thermometer, E,
is noted as the flashing point. Obviously this form of apparatus
is only suitable for substances the flashing point of which is
below the temperature of boiling water ; when less volatile sub-
stances are to be examined, the water jacket is replaced by a hot
bath of some other fluid ; or a hot airbath is used instead.
Fig. 29.
Pig. 29 indicates Pensky's modification of Abel's instrument for
such purposes, where the source of heat is the lamp flame, C,
playing on wire gauze, D, and filling the inverted basin, A, with
hot air.*
* An improved form of Pensky's apparatus has been described by Holde
(Journ. Soc. Chem. Ind., 1889, p. 734).
128
OILS, FATS, WAXES, ETC.
Lubricating oils containing hydrocarbons sufficiently volatile
to flash at 150° C. or below are distinctly unsafe as regards risk
of fire. Animal and vegetable fixed oils (unmixed with hydro-
carbons), as a rule, do not flash below 200° to 250° C. ; thus
A. Kiinkler gives the following values * as the flashing points
observed with various lubricating fluids, mostly consisting of
petroleum hydrocarbons, and some natural oils, &c. :• —
Cylinder oils - Russian,
,, American,
Machine oils — Russian,
,, American,
Spindle oils — Russian,
,, American,
Rape oil — crude,
,, refined,
Olive oil, .
Castor oil,
Linseed oil,
Tallow, .
Sp. Gr. at 17° 'o.
Degrees C.
•9 11 --923
183-238
•886--S99
280-283
•893--920
138-197
•884--920
187-206
•893 --895
163-167
•908 --91 1
187 200
•920,
265
•911
305
•914
205
•963
275
•930
285
•951
265
Characteristic Oxidation Products. — In certain cases the
results furnished by cautious oxidation afford useful indications
of the nature of the fatty acids ; this is more especially the case
when an approximate separation of liquid and solid fatty acids
has been previously effected by conversion into lead salts and
treatment with ether, so as to dissolve out oleate and linolate
of lead, <tc., leaving undissolved lead stearate, palmitate, &c.
Hazura recommends the following method of operating : — The
fatty acids obtained by decomposing the soluble lead salts are
neutralised with a slight excess of caustic potash, diluted with
60-70 parts of water, and the liquid treated with about an
equal volume of a solution of potassium permanganate added
in a thin stream with continuous agitation. After ten minutes
sulphurous acid solution is similarly added, sufficient to dissolve
all precipitated hydratecl manganese dioxide, and to give an
acid reaction. The products of oxidation of oleic and linolic
acids (dioxystearic and sativic acids) are only difficultly soluble,
and consequently precipitate ; whilst linusic and isolinusic
acids (the oxidation products respectively of linolenic and
isolinolenic acids) remain in solution. These latter acids are
extracted by neutralising with potash, evaporating to a small
bulk (one-twelfth to one-fourteenth of the original volume) and
decomposing with sulphuric acid ; the precipitate is dried in the
air, treated with ether to dissolve out matters readily soluble
* Journ. Hoc. Chem. Ind., 1890, p. 197; from Dinner's Pol. Journ., 274,
p. 276.
SPONTANEOUS OXIDATION OF OILS. 129
therein, and the residue crystallised from alcohol and from water
so as to separate the more soluble isolinusic acid from the less
soluble linusic acid. Dioxystearic acid and sativic acid are
separated in a similar way from the precipitate thrown down in
the earlier stage ; the precipitate is washed with a little ether to
remove easily soluble fatty acids (unoxidised) and then treated
with large bulks of ether (100 parts ether to 1 of substance).
Dioxystearic acid is chiefly dissolved out, obtainable by evapora-
tion and recrystallisation of the deposited crystals from alcohol
twice in succession ; whilst sativic acid is isolated from the
insoluble portion by boiling with water, filtering whilst boiling
hot, and crystallisation on cooling. The purified acids thus
obtained are further identified by means of their melting points
(p. 43). According to Benedikt the acetylation test (Chap, viu.)
may also be usefully employed for this purpose.
In somewhat similar fashion trioxystearic and isotrioxystearic
acids are obtainable from the fatty acids of castor oil. It is
noteworthy in this connection that the acids obtained by the
oxidation of isoleic acid and of elaidic acid (the isomeride of
oleic acid produced by the action of nitrous acid, p. 28) are
dioxystearic acids, isomeric but not identical with that obtained
from ordinary oleic acid (Saytzeff, p. 30). Similarly, the oxida-
tion products of erucic acid and its elaido derivative brassic acid,
yield two isomeric dioxybenic acids (p. 29).
Spontaneous Oxidation of Oils, Fats, &c. — Oils of the
drying class, and to a lesser extent many other oils and fats,
possess the property of directly absorbing oxygen from the air at
the ordinary temperature, the effect being much more marked
when more or less heated ; the drying and hardening of paint
prepared from linseed oil is an extreme case of such an action,
whilst the thickening and " gumming " of various other oils on
keeping exhibits the same kind of phenomenon in a lesser
degree. The fixation of oxygen during actions of this kind
appears to be principally due to a direct combination of oxygen
with acid radicles of " unsaturated " character, precisely analogous
to the combination therewith of iodine or bromine (p. 31, 45); as
the oxidation proceeds, the "iodine absorbing power" of the
substance usually diminishes pari passu.
In some cases the rapidity with which the absorption of oxygen
takes place is greatly enhanced by heating the oil to a tempera-
ture insufficient to produce any great degree of decomposition,
although high enough to cause incipient breaking-up with evolu-
tion of vapours ; this process of " boiling " oil, especially when
certain metallic compounds or "driers" are added, appears to
consist essentially in the formation of substances that act as
" carriers " of oxygen ;* so that " boiled oils " dry more rapidly
* The rotting of painted canvas sometimes observed appears to be largely
due to oxidation of the fibres of the fabric in consequence of this carrier
9
130
OILS, FATS, WAXES, ETC.
than the same oils in a raw or unboiled condition, these carriers
absorbing oxygen more rapidly from the air, and parting with it
again to the unoxidised portions of the oil. Free exposure to
air whilst heating, in some cases accompanied by the injection of
a current of air through the heated mass, appears to be essential
to the production of the initial degree of oxidation effected in
the boiling of drying oils ; the latter process when applied to
various non-drying oils (more especially fish oils), causes a con-
siderable increase in density and viscidity, so that " blown oils "
thus prepared are more suitable for lubricating and other
purposes than the original untreated substances.
Effect of Light on Oils. — Exposure to light produces a-
remarkable increase in the rate at which spontaneous oxidation
of oils, &c., takes place at the ordinary temperature j the result
of this oxidation is uniformly to cause an increment in specific
gravity and in the amount of heat evolved on mixture with
sulphuric acid (infra), together with a decrement in the iodine ab-
sorption (Chap, viu.) Thus, the following figures were obtained
(along with many others) by H. Ballantyne * with olive, castor,,
rape, cotton seed, arachis, and linseed oils ; specimens kept in
the dark for six months showed little or no alteration whether
in tightly corked or open bottles, and whether undisturbed or
agitated daily so as to aerate them ; whereas similar specimens
exposed to sunlight during the same period exhibited perceptible
amounts of alteration, even when kept undisturbed in corked
bottles ; and much larger amounts when kept in uncorked
bottles and agitated daily : —
VARIATION IN SPECIFIC GRAVITY.
Value after Six Months' Exposure
Original Value,
to Sunlight.
practically
Unchanged in the
Dark.
Undisturbed,
Agitated Daily,
Corked.
Uncorked.
Olive oil, .
•9168
•9185
•9246
Castor oil, .
•9679
•96S3
Rape oil,
Cotton seed oil, .
•9108
•9225
•9171
•9236
•9207
•9320
Arachis oil,
•9209
•9216
•9267
Linseed oil,
•9325
•9327
•9385
action. The presence of certain kinds of resinous matter (such as are
employed in the manufacture of tarpaulins, &c.), seems to diminish the
tendency to this destructive action.
* Journ. Soc. Chem. Int., 1891, p. 29.
EFFECT OF LIGHT ON OILS.
VARIATION IN IODINE ABSORPTION.
131
•
Value after Six Months' Exposure
Original Value,
to Sunlight.
practically
Unchanged in the
Dark.
: Undisturbed,
' Corked.
Agitated Daily,
Uncorked.
Olive oil,
83-16
82-64
78-24
Castor oil, .
83-63
83-27
Rape oil,
105-59
105-27
102-12
Cotton seed oil,
106-84
106-40
100-12
Arachis oil,
98-67
97-60
93-20
Linseed oil,
173-46
172-88
166-17
VARIATION IN HEAT EVOLUTION WITH SULPHURIC ACID.
Values after Keeping Six Months
In the Dark.
In Sunlight.
Undisturbed,
Corked.
Agitated
Daily,
Uncorked.
Undisturbed,
Corked.
Agitated
Daily,
Uncorked.
Olive oil,
44°
43° -5
47°
67°
Castor oil,
73°
73°
74° -5
78°-5
Rape oil,
61°-5
60° -5
63°
72° -5
Cotton seed oil,
75° "5
76° -5
76° -5
100°
Arachis oil, .
73° -5
73° -5
77°
90°
Linseed oil, .
11 3° -5
112° -5
120°
131°
Only minute amounts of free acid were developed in six months
during the course of these observations, indicating but little
hydrolysis of glycerides during the oxidation of the insolated
samples ; the maximum amounts formed were in the case of
linseed and cotton seed oils, and corresponded with a develop-
ment of 0*3 4 and 0*50 per cent, respectively of free acid
(expressed as oleic acid) in sunlight, none at all being formed
in the dark. Olive oil kept six months in the dark gave a hard
solid elaidin ; that exposed to sunlight in corked bottles with-
out agitation a somewhat less hard mass ; but that insolated
and agitated daily, so as to expose as thoroughly as possible
to oxidising influences, did not even thicken when sub-
mitted to the elaidin test. Similarly Becchi's silver test for
cotton seed oil gave only faint indications with the insolated
oxidised oil, although reacting thoroughly with oil kept in the
dark. The viscosity of rape oil, as indicated by the efflux
132 OILS, FATS, WAXES, ETC.
test (p. 95), was notably increased by nine months' exposure
to sunlight (in corked bottles without agitation) ; oil kept
in the dark giving times of flow 56 at 15° -5 and 25-5 at 50°,
whilst insolated oil gave 66 at 150<5 and 26-5 at 50°. Castor oil,
mainly consisting of the glycerides of acids already oxidised, as
might a priori be expected, is less changed by oxidation than
any of the others.
Similar, but less systematic, observations have been recorded
by various other experimenters, the general result of which is
to show that the changes brought about in oils and fats by
keeping and atmospheric oxidation are greatly accelerated by
the influence of light. According to E. Ritsert rancidity is only
produced in oils in presence of oxygen (air), the action being
greatly accelerated by simultaneous exposure to light. No
effect, however, is produced by the action of light alone, when
access of oxygen is entirely excluded.
Spontaneous Combustion. — When a film of readily oxidisable
oil is spread over a considerable surface, so that a large area is pre-
sented for atmospheric oxidation, if the circumstances are such
that the heat generated by the action is not readily lost, the mass
heats greatly, in some cases to such an extent as to bring about
spontaneous inflammation. Gellatly has shown that greasy
cotton rags and similar materials kept in a warm place are,
in consequence, liable to ignite spontaneously, and are accord-
ingly a source of danger as regards fire. Boiled linseed oil
appears to be the most energetic of oils in this respect ; a
handful of cotton waste soaked in this fluid and squeezed out,
and then kept in a box at 70° to 80", soon rises greatly in
temperature to near 200° ; in little more than an hour the mass
is so hot that smoke issues, and on opening the box the whole
takes fire. Unboiled linseed oil takes a much longer time to
produce the same result * (from four to six hours), and rape oil
longer still (some ten hours). On the other hand, an admixture
of mineral oil greatly retards the action. In general, the ten-
dency to spontaneous oxidation is greater the greater the iodine
absorption of the oil.
A testing apparatus has been constructed by Allbright &
Clark f for determining the comparative liability of oils to
spontaneous combustion, consisting of an outer shell formed by
a six inch wrought iron tube which can be closed at each end by
discs of wood. Inserted into this tube is an inner four inch
sheet iron tube with overlapping metal covers at each end, so
that an air space is left of one inch around the inner tube, and of
three inches at each end ; three thermometers are inserted into
the inner shell through the outer one. A ball of say 50 grammes
* Renouard, Journ. Soc, Chem. Ind., 1882, p. 184, has repeated and con-
firmed this difference between boiled and raw linseed oil.
t Journ. Soc. Chem. Industry, 1892, p. 547.
ABSORPTION OF OXYGEN BY OILS. 133
of waste, over which an equal weight of oil is distributed, is care-
fully pushed to one end of the inner tube, and the corresponding
thermometer bulb inserted into the middle of the ball. A
similar ball of unoiled waste is placed at the other end, with
another thermometer bulb inserted as before. The third ther-
mometer is placed between the two. On heating the outer tube
by means of a Bunsen burner, so that the central thermometer
indicates about 125°, the temperature of the unoiled waste ball
will be about 100°. That of the other rises in proportion as the
oil oxidises more rapidly. E. H. Richards reports that this
arrangement gives most valuable results as regards gauging the
degree of safety of lubricating oils, &c. ; for instance, the per-
centage of fatty oil which may be safely mixed with mineral oils
may be thus determined. Thus neat's foot oil and best lard oil
may be added to the extent of 50-60 per cent., whilst not more
than 25 per cent, of cotton seed oil is permissible.
Film-test. — If a film of oil be freely exposed to the air, so that
heating to any considerable extent is impracticable, the effect of
the oxidation is gradually to inspissate the oil, and finally to con-
vert it into a varnish-like product; a test of the quality of a given
sample of drying oil is based upon this, a glass plate being
coated on one side with a film of oil, after the fashion of a photo-
grapher's collodion plate, and then kept in a steam bath for
some hours, preferably side by side with another plate similarly
coated with oil of standard quality ; the relative length of time
requisite before the film ceases to be " tacky," being converted
into a dry varnish, serves as a measure of its drying quality.
Thus, whilst a good sample of linseed oil is completely solidified
in some twelve hours, non-drying oils like arachis and olive oils
are scarcely thickened at all ; whilst cotton seed oil and similar
substances possessing only a certain degree of drying power are
intermediate. In this respect the order in which oils are
arranged by means of this test is sensibly the same as that in
which they are arranged by means of the iodine absorption
reaction (Chap, vm.)
Livache's Test. — Livache finds that the rate of absorption of
oxygen is much quickened if finely divided metallic lead is
mixed with the oil to be examined ; comparative tests are readily
made by placing on a watchglass about a gramme of lead * in a
thin layer, and then dropping on to it a few decigrammes (not
more than 6 or 7) of oil in small drops, scattered over different
portions of the lead, so as not to run into one another. The
whole is then weighed and allowed to stand at the ordinary
temperature. Drying oils begin to increase measurably in
weight in less than twenty-four hours, and cease to gain weight
* Precipitated from lead acetate solution, and rapidly washed with water,
alcohol, and ether in succession, and finally dried in vacuo. According to
Hiibl, precipitated copper is preferable to lead.
134
OILS, FATS, WAX MS, ETC.
after three to six days, whilst oils possessing little or no drying
qualities do not increase at all for several days. Similar remarks
apply to the fatty acids isolated from the oils. Thus the follow-
ing figures were obtained : —
Percentage Increment in Weight
.
Of Oil after
Of Fatty Acids
2 Days.
7 Days.
8 Days,
Linseed oil, .
14-3
11-0
Nut oil,
7-9
..
6-0
Poppy oil,
0-8
..
3-7
Cotton seed oil,
5-9
0-8
Beech mast oil,
4-3
2-6
Colza oil,
Nil.
2-9
2-6
Arachis oil, .
Nil.
1-8
1-3
llape oil,
Nil.
2-9
0-9
Olive oil,
Nil.
1-7 0-7
Sesame' oil, .
Nil.
2-4
2-0
Bach,* following Freseiiius, tests the oxygen- absorbing power
of oils by heating in a closed tube containing oxygen, and noting
the bulk of gas absorbed. The presence of excess of oxygen after
the experiment must be proved by means of a glowing splinter
of wood. This test is more particularly useful in the valuation
of certain kinds of lubricating oils.
CHEMICAL CHANGES OCCURRING DURING
DRYING OF OILS.
The nature of the chemical changes taking place during the
complete atmospheric oxidation and consequent drying up of a
drying oil has been the subject of various investigations ; but it
can hardly be said that the matter is yet settled beyond dispute.
The earlier researches on linseed and other drying oils by
Mulder and others led to the conclusion that the chief consti-
tuent of drying oils, giving them their peculiar properties, was
linolin, the glyceride of linolic acid, regarded as C16H28O9, and
then termed linoleic acid. During drying this glyceride was
supposed to become hydrolysed or otherwise broken up,
losing its glyceridic character, and forming oxylinoleic acid,
C16Ho6O5 . 2H.2O, by oxidation ; a neutral polymerised amorphous
anhydro derivative, linoxyn, C32HS4On, being subsequently
developed as the leading ingredient of the " skin " formed as the
oil dries. Later researches have indicated that what \vas formerly
* Journ. Soc. Chem. Twd.,-1889, p. 990 ; from Chem. Zeit., 13, p. 905.
CHEMICAL CHANGES OCCURRING DURING DRYING OF OILS. 135
termed "linoleic acid," C16H28O2, is really a mixture of three
acids of notably higher molecular weights — viz., true linolic acid,
C18H32O2, related to oleic acid as oleic acid is to stearic ; and
two isomeric acids still less saturated, related to linolic acid in
the same way, linolenic and isolinolenic acids, both represented
by C18H30O2. These substances by gentle oxidation yield
crystallisable acid products, sativic acid (tetroxystearic acid),
melting at 173°, being formed from linolic acid, and linusic and
isolinusic acids (hexoxystearic acids), melting at 203° to 205°
and 173° to 175° respectively (vide p. 43), being produced from
the other two acids ; but these crystallisable ultimate oxida-
tion products are apparently not formed in the " boiling"
process at all \ and even if contained in the dried skins are
certainly not the constituents giving the peculiar physical
properties to these substances. Moreover, the proportions of
oxygen and water requisite to be taken up by linolic and
linolenic glycerides in order to convert them into free oxy-
stearic acids, are greatly in excess of the increment in weight
observed to take place during the drying of oils of this class
(p. 134) ; whilst the skins are found to be susceptible of some
degree of saponification, furnishing glycerol. Hence it would
seem probable that the essential constituents of dried skins are
a mixture of polymerised glycerides (possibly more or less hydro-
lysed) of acids derived from linolic, linolenic, and isolinolenic
acids by oxidation processes not carried so far as to produce the
various oxystearic acids obtainable by means of alkaline perman-
ganate.* That some of these substances are of a feebly acid
•character, or at any rate are capable of forming salts by the action
of metallic oxides, is suggested by the well-known fact that the
•effect of basic matters like white lead (basic lead carbonate) and
zinc white (chiefly zinc oxide) on the paint produced by their
admixture with drying oils is different in many respects from
that of neutral pigments like lead sulphate and sulphate of
barium ; in practice these latter are found to be far less suitable
for the production of firm adherent coats that will stand ordinary
wear and tear, which is usually considered to be due to the
absence of the metallic salts contained . in white lead and zinc
white paints, formed by the neutralisation of acids developed by
oxidation, or possibly by the saponification of glycerides.
The drying qualities of an oil appear to be the more marked
the greater the proportion of linolenic and isolinolenic acids is
*Fahrion (Zeitsch. /. angew. Ckem., 1891, p. 540; 1892, p. 171) finds
that the acids formed on saponification of boiled linseed oil where partial
•oxidation has taken place are not wholly soluble in light petroleum spirit,
whereas the fatty acids of unoxidised oil are readily soluble therein ; from
0'6 to 31 '0 of such insoluble acids were found in different samples of oil.
The proportion present appears to be the greater the more marked the
decrement in "iodine absorbing power" produced by the oxidation process.
These " oxyacids " readily dissolve both in alcohol and in ether.
136
OILS, FATS, WAXES, ETC.
present. Hazura and Griissner deduced the following percentages
from the relative proportions in which the oxystearic acids were
produced on oxidising the liquid fatty acids of linseed, hemp seed,
nut, poppy seed, and cotton seed oils, the solid acids being pre-
viously separated by conversion into lead salts and treatment
with ether (p. 112).
Linolenic
Acid.
Isolinolenic
Acid.
Linolic
Acid.
Oleic Acid.
Linseed oil, .
15
65
15
5
Hemp seed oil,
15
70
15
Nut oil,
13
80
7
Poppy seed oil,
5
65
30
Cotton seed oil,
60
40
Bauer and Hazura regard the drying of oils as being mainly
due to the linolenic and isolinolenic acids, which, by taking up
oxygen, become converted into the " oxylinoleic acid '' of Mulder,
which they regard as C18H30O7. For the most part, however, the
glyceridic character of the product is not destroyed during the
oxidation, so that, instead of free acid, a neutral body results,
substantially the "linoxyn" of Mulder, but termed by them
hydroxylinolein. Small quantities of free fatty acids are, however,
developed by the decomposition of .the glycerides of the solid
fatty acids present (myricin, palmitin, ttc.) ; the glycerol of these
glycerides being converted into carbon dioxide and other volatile
products.
According to experiments by Cloez,* the effect produced by
prolonged exposure to air of a drying oil is not quite so simple
as wTould appear from the above. The following figures were
obtained with linseed and poppy seed oils, the final increment in
weight being a little more than 7 per cent, in each case after
eighteen months : —
LINSEED OIL.
Before Exposure.
After Oxidation.
Percentage
Composition.
Calculated per 100
Parts of Linseed Oil
originally used.
Carbon,
Hydrogen, .
Oxygen, .
77-57
11-33
11-10
67-55
9-88
25-57
72-30
10-57
24-16
100-00
100-00
107-03
Bulletin Soc. Chimique de Paris, 1865, hi., p. 49.
POUTET'S ELAIDIN REACTION — NITROUS ACID TEST.
POPPY SEED OIL.
137
Before Exposure.
After Oxidation.
Percentage
Composition.
Calculated per 100
Parts of Linseed Oil
originally used.
Carbon, . . .
77-50
66-68
71-38
Hydrogen, .
Oxygen,
11-40
11-10
9-94
23 -38
10-64
25-03
100-00
100-00
107-05
The original oils thus had a composition closely akin to that of a
triglyceride of an acid of formula C18H32O2 (p. 33), requiring
carbon 77"90, hydrogen 11 "16, oxygen 10*94; during oxidation,
from TV to TTT of the carbon disappeared and not far from the
same proportion of hydrogen. Even if the whole of the glyceridic
part of the oil had been oxidised to volatile products, only Jg- of
the carbon would have disappeared ; so that, obviously, carbon
dioxide, or acetic acid, &c., must have been formed at the
expense of the fatty acids present, indicating a more deep-seated
oxidation change than the simple absorption of oxygen, con-
verting the glycerides of linolenic and isolinolenic acids into
hydroxylinolein.
With castor oil Cloez found the gain in weight after eighteen
months was much less marked (2*68 per cent.) ; whilst only a,
practically inappreciable amount (0*4 per cent.) of the original
carbon had disappeared. Intermediate results were obtained
with a semi-drying oil, sesame oil, the gain in weight in eighteen
months being 4-83 per cent., and the loss of carbon about ^ of
the original amount.
POUTET'S ELAIDIN REACTION— NITROUS
ACID TEST.
Oils containing unsaturated acid glycerides, more especially
olein and its homologues, or ricinolein, often undergo a marked
change, when treated with nitrous acid, becoming more or
less solidified without alteration of composition. Gaseous,
nitrous anhydride (fumes from nitric acid heated with starch
or arsenious anhydride) will produce the reaction, or agitation
with substance containing nitrous acid dissolved — e.g., red nitric
acid, solution of a nitrite recently acidified, copper or mercury
recently dissolved in nitric acid, or even nitric acid warmed
until it begins to act on the oil. Of these the liquid originally
138
OILS, FATS, WAXES, ETC.
described by Poutet, obtained by dissolving 12 parts by weight
of mercury in 15 of cold nitric acid (sp. gr. 1'35), is the most
convenient ; * 2 c.c. of the fresh deep green liquid, and 50 of oil
are shaken together in a bottle at intervals for about two hours,
at the end of which time the action is nearly complete, although
the product usually becomes stiffer or harder on standing twenty-
four hours. Olive oil of good quality thus treated gives a
bright yellow extremely hard "elaidin;" arachis and lard oils
yield products little inferior in stiffness ; mustard, rape, sesame,
sunflower, cotton seed, and other oils give softer products, vary-
ing in consistency from a stiff buttery mass to a mixture of
pasty product with still fluid substance ; whilst linseed and
other drying oils are comparatively little affected.
A. H. Allen classifies the more important fixed oils as follows,
in accordance with the physical character of the product : —
Solid Hard Mass.
Buttery Mass.
Pasty or Buttery Mass
separating
from a Fluid 'Portion.
Liquid Products.
Olive oil.
Bottlenose oil.
Rape oil.
Linseed oil.
Almond oil.
Mustard oil.
Mustard oil.
Hempseed oil.
Arachis oil.
Neat's foot oil \
Sesame oil.
Walnut oil.
Lard oil.
Arachis oil [ Some-
Cotton seed oil.
Sperm oil.
Sperm oil / times.
Sunflower seed oil.
Neat's foot oil
(sometimes).
Rape oil J
Niger seed oil.
Cod liver oil.
Whale oil.
Porpoise oil.
In certain cases (more especially with olive oil) the nature
and consistency of the elaidin formed on treatment with nitrous
acid affords a useful means of detecting the presence of adulter-
ations with oils of different character. In all such cases, the
most satisfactory results are obtained when the oil examined is
tested side by side in the same way with samples of oil of
standard purity, and of the same mixed with known proportions
of other oils.f
The free fatty acids obtained by saponifying oils and decom-
posing the resulting soaps with a mineral acid, are affected by
nitrous acid in similar fashion. Attempts have been made to
* Archbutt (Journ. Soc. Chem. IncL, 1886, p. 303) dissolves 18 grammes
of mercury in 15 '6 c.c. of nitric acid, sp. gr. 1'42 (22'2 grammes of acid),
and uses 1 part of the resulting green fluid to 12 of oil (by weight).
t There is often great difficulty experienced in obtaining absolutely pure
samples of oil for use as standards. In many cases it is only possible to
obtain such standard substances by actual expression of hand-picked seeds,
&c., in the laboratory, and subsequently refining the product; but this is
not readily practicable, unless a plentiful supply of pure seed is to hand,
as well as a good form of small experimental or laboratory press.
NITRIC ACID TEST.
139
utilise for candle-making and other purposes the polymerised
solid acids of higher melting point thus formed ; but, hitherto,
various practical difficulties have stood in the way of utilising
the products effectively.
Legler's Consistency Tester. — Legler has constructed a
simple form of apparatus by means of which comparative tests
can be made of the degree of consistence of the
elaiclin. mass produced when any given oil sample
is treated with nitrous acid. It consists of piece of
glass tubing narrowed at one end (Fig. 30) ; through
the tube passes a glass rod supported by means of
a spiral spring, and furnished with a horizontal disc
on the top, so that by placing weights on the disc
the end of the rod is depressed to an extent pro-
portionate to the weight added. The outer tube is
held vertically by a suitable clamp holder, so
adjusted that the bluntly pointed end of the rod
just rests on the surface of the elaidin to be tested.
The measurement is made by placing a given
weight on the disc and noting how far the rod
sinks into the elaidin in a given time (e.g., a
minute), by reading off the level on a scale the zero
point of which is level with the top of the outer
tube when the disc is unweighted. The elaidin
samples are best prepared by mixing together
10 c.c. of oil, 10 c.c. of nitric acid of 25 per cent.,
and 1 grin, of copper wire or turnings, and allowing
to stand twenty-four hours; the mass is fused by
dipping the containing vessel in warm water so as
to bring about complete separation of elaidin and
watery fluid, and the former removed and allowed
to solidify. To obtain comparable results, a uni-
form method of manipulating should be adopted,
the samples tested being examined side by side
with others similarly prepared from genuine oils or
known mixtures.
Exposure of olive oil to sunlight greatly diminishes
the solidity of the elaidin formed from it ; the nature j?ig. 30.
of the change brought about is uncertain ; probably
oxidation takes place with formation of oxyolein (or possibly
linolin), as the insolated oil develops more heat by the action of
sulphuric acid than the original oil kept in darkness (vide p. 131).
Nitric Acid Test. — When fixed oils are brought into contact
with nitric acid a complex effect is often produced ; oxidation of
a part of the oil by the acid is brought about with the evolution
of lower oxides of nitrogen, which convert the olein constituent
of the oil into elaidin. In some cases, characteristic colours are
produced with oils of pure nature, so that a comparison of the
140
OILS, FATS, WAXES, ETC.
substance tested with a pure standard substance, or with a known
mixture, enables deductions to be drawn as to the nature of the
admixture or adulteration present. This kind of test is more
especially useful in the case of olive oil ; thus, when pure
olive oil is treated with one-ninth its volume of nitric acid
of sp. gr. 1-42, the mixture being gently warmed in a capacious
dish until the acid begins to act pretty vigorously, and then
stirred briskly (the source of heat being removed) until no
further action is visible, a pale yellow solid mass is formed
after standing an hour or two ; whereas, if cotton seed oil be
present, a much darker tinted product is formed, which does
not set so readily j and similarly when various other oils are
present.
A. H. Allen gives the following table,* indicating the different
tests developed when several of the commonest oils are tested in
the following ways : —
a. Nauchcorne's Test, as extended by Stoddart. — Agitate to-
Oil.
a.
b.
!
Olive oil,
Colourless or tran-
Colourless, yel-
Broad bright
sient yellow.
lowish, or
bluish green
greenish.
zone.
Almond oil, .
Nearly colourless,
Colourless or
Narrow bright
changing to solid
white mass.
slightly greenish.
green zone ; oil \
flocculent or
opaque.
Arachis oil, .
...
Reddish.
...
Peach kernel oil,
...
Immediate red
liniment.
Rape oil,
Red or orange.
Reddish or orange.
Sesame oil,
Yellowish or
j
orange.
Cotton seed oil,
Red or orange.
Reddish or orange.
Brown red,
greenish below.
Niger seed oil,
Red or orange.
Brown or
...
brownish red.
Linseed oil,
Red or orange.
Red or orange.
Green zone, oil
red.
Poppy seed oil,
...
Reddish.
Dark green zone,
oil pink.
Hemp seed oil,
...
Brownish red.
Castor oil,
Transient yellow.
Yellowish or
...
orange.
Lard oil,
Colourless or tran-
...
...
sient yellow.
Whale oil, .
Dark red.
...
Seal oil, .
Dark red.
...
Cod liver oil, .
...
.
Brown red.
Rosin oil,
Reddish brown.
.
...
Mineral oil, .
Dark red.
•
...
Commercial Organic Analysis, vol. ii., p. 61.
ZINC CHLORIDE REACTION AND COLOUR TEST. 141
gether from 3 to 5 measures of the oil with 1 of nitric acid of
specific gravity \'3'2. Heat the tube for five minutes in boiling
water ; then take it out and allow it to stand. Observe the
colour of the oil from time to time for one and a-half hours.
b. Massies Test. — Agitate 3 measures of the oil for two
minutes with 1 measure of colourless nitric acid of specific
gravity 1-40. Observe the colour of the oil after separation.
c. Glassner's Test. — Pour the oil cautiously into an equal
measure of red fuming nitric acid, and observe the colour of the
oil and of the zone which forms between the oil and the acid
liquid.
ZINC CHLORIDE REACTION AND COLOUR TEST.
Some oils, more especially castor oil, when heated in contact
with a highly concentrated solution of zinc chloride, become
converted into a gristly mass, which, on treatment with water
to dissolve out the zinc chloride, more or less breaks up into
cartilaginous or fibrous portions, which swell up largely to white
masses closely resembling rasped cartilage, the oil being com-
pletely solidified by the process. Apparently, the chemical action
consists chiefly of polymerisation, somewhat after the fashion of
the elaidin reaction, possibly accompanied by dehydration; by
long continued boiling of the product with alkalies, partial
saponification is effected, glycerol being set free.
To produce the most gristly product, the following process
may be followed:* — Zinc chloride solution is boiled down until
the boiling temperature rises to about 175° C. or upwards, the
composition of the fluid then being close to that indicated by
the formula, ZnCl2, H2O, or slightly less hydrated. Three parts
of this fluid by weight, and one of castor oil are then well
intermixed together at a temperature of 125° or thereabouts;
the oil speedily, becomes more viscid, and then coagulates to a
leathery mass resembling bullock's liver, but tougher, mostly
separating from the zinc chloride in so doing. This mass is then
chopped up, soaked in water till disintegrated to a mass some-
what resembling coarsely scraped horseradish, drained from zinc
chloride solution and washed, when it is in suitable condition for
use in the manufacture of india-rubber substitutes, insulating
coatings for electric leads, &c.
By using weaker zinc chloride, or smaller proportions, or
lower temperatures, the action can be controlled and stopped
before going quite so far, so as to produce substances of less
cartilaginous and more plastic character ; or other oils, less
* Patent specification, C580, 1886, Hun-head and Alder Wright.
142
OILS, FATS, WAXES, ETC.
readily acted upon, may be mixed with the castor oil ; or resin,
Kauri gum, and similar substances may be similarly admixed.
Colour Test. — When zinc chloride solution of somewhat
lesser strength (of thick syrupy consistence when cold) is mixed
with certain oils, colours are developed. Muter gives the
following table, founded on the results of Chateau :* —
To 10 drops of the oil in a porcelain capsule, add 5 drops of
syrupy zinc chloride, and stir.
White or scarcely affected.
Yellow, Red, or Brown.
Green or Blue Shades.
Poppy.
Nut.
Almond (hot pressed).
Gingelly.
Cokernut.
Linseed (English), )
Rape, ' yellow.
Groundnut, }
Castor, rose yellow.
Beech, flesh rose.
Linseed (foreign),
bluish green.
S£}«~-
Gold of pleasure
Neat's foot.
Lard.
Horse bone.
Sperm.
Whale (sometimes
pale violet tinge).
Cod liver (cold).
Whale, yellow brown.
Fish, orange yellow.
Seal, red brown.
green.
Almond, milky with
green tinge.
Cod liver (hot),
green.
Action of Zinc Chloride on Oleic Acid. — Zinc chloride,
when heated with oleic acid, converts it into a solid isomeride
closely resembling elaidic acid, but not identical therewith ; thus,
when oleic acid, mixed with 10 per cent, of its weight of zinc
chloride, is heated to 180° to 185° (but not exceeding 195°) for
some time, the transformation is so far complete that a sample
taken out and treated with hot dilute hydrochloric acid yields a
layer of fatty acids, solidifying on cooling. By diluting with
water and subjecting to distillation with superheated steam (or
under diminished pressure), a buttery mass is obtained which,
on pressing (first cold and then hot), finally yields a hard
crystallisable material of melting point 41° to 42°, suitable for
making certain kinds of candles not requiring fatty matter of
high fusing point (Schmidt's process). Benedikt obtained the
following results on analysis of the products thus formed : — f
A. Crude product obtained by boiling the heated mass with
diluted hydrochloric acid.
B. Product of distillation under diminished pressure.
C. Solid mass, after pressing until the melting point rises to
41° to 42°.
* Spon's Encyclopaedia of Arts and Manufactures, ii., p. 1473.
•\-Journ. Soc. Chem. 2nd., 1890, p. 658; from Movatsh., 1890, ii., p. 71.
ACTION OF SULPHURIC ACID ON OILS AND FATS.
143
A.
B.
c.
Liquid anhydride,
8
Stearolactoiie, .
28
31-0
75-8
Oxystearic acid,
17
...
Oleic and isoleic acids,
40
43-3
15-7*
Saturated fatty acids,
7
12-1
8-5
Unsaponifiable matters, .
13-6
...
100
100-0
100-0
The " unsaponifiable matters" contained in B were mainly
liquid hydrocarbons of the olefine series (carbon = 84*1, hydro-
gen = 13-7, oxygen = 2-2).
It would appear that the general character of the main action
is that zinc chloride directly combines with the oleic acid, and
that the resulting compound (or, possibly, pair of isomeric com-
pounds) is partly decomposed again into oleic and isoleic acids,
and partly hydrolysed with formation of oxystearic acids, more
especially the 7 acid, which then loses the elements of water,
forming stearolactone (vide p. 39) ; the hydrolytic action pro-
bably being as follows : —
Oleic Acid.
Cl8H3402
Compound.
Cl8H3402, ZnCl2
Zinc Chloride.
ZnCl2
H20
Compound of Zinc Chloride
aud Oleic Acid.
Cl8H3402,ZnCl2.
Oxystearic Acid.
ZnCl2 + C18H3603.
In all probability, similar reactions occur when glycerides
containing olein are saponified by means of sulphuric acid, the
yield of liquid oleic acid in the products finally obtained by
distillation with superheated steam being very small.
ACTION OF SULPHURIC ACID ON OILS AND FATS,
TURKEY RED OILS.
When sulphuric acid is added to a fixed oil or fat, various
kinds of effects are produced in different cases; in many instances
distinctive colours are developed, due not so much to the action
of the acid on the glycerides themselves as to that upon other
bodies accompanying them in small proportion; this is especially
marked in the case of certain fish liver oils where biliary con-
stituents are present (vide infra). In other cases action occurs
between the acid and the glyceride, producing more or less
* Isoleic acid only.
144
OILS, FATS, WAXES, ETC.
marked heat development, sometimes leading to charring and
destruction, sometimes to less deep-seated changes of a definite
character. Thus, when oils mainly consisting of olein are
cautiously mixed with sulphuric acid hydrolysis ensues, the
resulting glycerol being more or less converted into glycero-
sulpkuric acid, much as ordinary alcohol is into ethylsulphuric
acid.
Sulphuric Acid.
on ,JOH
S°2\OH
Ethylsulphuric Acid.
= S02
Iphuric Acii
O . C2H5
OH
Sulphuric Acid. Glycerosulphuric Acid.
SO, /RS = S02(O.C3Hi(OH)2
Water.
H20
Water.
H20
Alcohol.
C2H5 . OH
Glycerol.
( OH
C3H5 OH
( OH
Simultaneously the oleic acid is acted upon, direct combination
taking place between the two acids * with the formation of
oxystearosulpliuric acid.
* According to M tiller- Jacobs, the product thus formed contains the
elements of a molecule of waterless, Cl8H3405S instead of C^HaflOfjS ; and
( SO OFT
is represented by him as a sort of sulphonic acid, Cl7H32 j nr/' QTJ» breaking
tip on hydrolysis with the formation of oxystearic acid, C^Ks.-! nn ntr'
( C\~\3 L ^-'^'•^-'•£1
oxyoleic acid, C^HsoJpQ QTT being also formed, probably by a secondary
action. Geitel considers that a mixed glyceride is formed, part of the three
oleic radicles being modified by direct addition of sulphuric acid thereto so
as to form a glyceride where the radicle of oxystearosulphuric acid partly
replaces the oleic radicle, saponification of the glyceride not taking place,
at any rate, at first.
Liechti and Suida also consider a mixed glyceride to be the first product,
containin
thus—
2C3H5
simultaneously the radicles of sulphuric and oxystearic acids,
Triolein.
O.C18H330
O.C18H3,0
O.C8HS30
Water. Sulphuric Acid.
vy.^H^
4H20
S02(OH)2 =
Oleic Acid.
4C]8H3402
Oxystearosulphuric
Diglyceride.
( O.C18H3502
OH
°}S02
OH
O.C18H,,02
Simultaneously, they regard an analogous mixed diglyceride as being
formed, containing the radicle of oxyoleic acid (C]8H3302) instead of that
of oxystearic acid (Cl8H3.502). this substance being produced in virtue of an
oxidising action exerted by the sulphuric acid, whereby S02 is evolved.
Inasmuch as practically no glycerol is obtainable from Turkey red oil by
saponification (beyond what is due to undecomposed original oil present
therein), whilst free oleic acid gives products similar to those prepared from
olive oil (the more free acid contained in the oil the better it is suited for
the purpose), it is obvious that these mixed glycerides, even if formed
under special conditions, are at any rate not the main constituents of the
commercial products.
TURKEY RED OILS. 145
Oleic Acid. Sulphuric Acid. Oxystearosulphuric Acid. Water.
C17H33.COOH + S02° = S02°Cl'H34-CO-OH + H20
This product, being a saturated compound, does not combine
with iodine like the original oleic acid (Benedikt and Ulzer) ;
under the influence of hydrolysing agents it breaks up into
oxystearic and sulphuric acids, thus * —
Oxystearosulphuric Acid. Water. Sulphuric Acid. Oxystearic Acid.
Qn f 0 . C17H34 . CO . OH , w n Qn J OH , r „ J OH
S°2 + H20 = S02 + C17H34
10H
Products containing more or less Oxystearosulphuric acid and
the oxystearic acid thence formed by hydrolysis, together with
unchanged olein, and some free oleic acid (also whatever solid
fatty glycerides were originally present in the oil employed and
the products of the action of sulphuric acid thereon) are manu-
factured from olive, cotton seed, and similar oils chiefly consisting
of olein, for use in dyeing and calico printing, especially in the
production of " Turkey red," whence the name " Turkey red
oils " applied to these products ; the free acidity is usually
partially or wholly neutralised by cautious addition of ammonia
or other alkali to the oil after washing with brine or water.
Another variety of Turkey red oil, considerably superior for
some special applications, is produced when castor oil is
employed instead of olein-containing oils. According to the
generally received view, the chief action of the sulphuric acid is
precisely analogous to that on ordinary alcohol ; the glyceride is
hydrolysed into glycerol and ricinoleic acid, the former being
more or less converted into glycerosulphuric acid, as above ; the
ricinoleic acid reacts on the sulphuric acid in a parallel way,
forming ricinoleosulphuric acid, thus —
Riciuoleic Acid. Sulphuric Acid. Water. Ricinoleosulphuric Acid.
r w f°H i. ^n /OFI w n j. r w /O.S02.OH
CirH^o -^ CQ QH - =>U2 j QR = LlrH32 j C0 OH
the resulting product differing from that formed from oleic acid in
that it contains H9 less, and is, therefore, an "unsaturated" com-
pound, capable of taking up iodine or bromine in the same manner
as the original ricinoleic acid itself (Benedikt and Ulzer). Accord-
ingly, castor Turkey red oil is capable of taking up oxygen, and
generally of behaving in ways not observed in the case of olive
Turkey red oil ; which circumstance renders it more suitable for
certain particular applications in reference to dyestuffs, &c.
* The effect of sulphxiric acid in decomposing fatty glycerides, together
with the hydrolysing action of water on the product, is utilised in the
preparation of caudle material ; a larger yield of solid matter is thus
obtained than by the ordinary saponification processes, on account of the
conversion of liquid oleic acid into solid substances. According to Geitel,
y-oxi/fstearic acid (p. 39) is usually produced (inter alia) by the hydrolysis
of the compouud of oleic acid with sulphuric acid, which immediately splits
up into water and stearolactone.
10
14 G OILS, FATS, WAXES, ETC.
A somewhat different view of the action of sulphuric acid on
castor oil has been lately put forth by Scheurer Kestner"* as the
result of his investigations. After the glyceride has been hydro-
lysed, he finds that part of the resulting ricinoleic acid becomes
"polymerised" (or more accurately, dehydrated and "con-
densed "), so as to form a more complex molecule of diricinoleic
acid, which is then acted upon by sulphuric acid so as to form
diricinoleosulphuric acid ; the reactions may be written thus —
Ricinoleic Acid (2 molecules). Diriciuoleic Acid.
TT JOH „ (OH
TT
17H
o OH 1732^CO,
H 0 TT $° /
32 co . OH C"H«* CO .OH
Diricinoleic Acid. Sulphuric Acid. Diricinoleosulphuric Acid.
TT JOH r TT JO. SO.,. OH
17^32 I rv\ \ ^irn32 T Cf) } ~
= 0
22 2
C17H -
S02(OH)2 = H20
| co OH 1732 -| co . oil
Obviously the diricinoleosulphuric acid thus formed is "un-
saturated," and is, therefore, capable of taking up two halogen
atoms for each C1S present. More or less of the diricinoleic acid
escapes conversion into diricinoleosulphuric acid; so that in
addition to unaltered castor oil, &c., the resulting Turkey red
oil consists of a mixture of diricinoleic acid, and diricinoleo-
sulphuric acid, together with some amount of ricinoleic acid that
has escaped condensation to diricinoleic acid, and of ricinoleo-
sulphuric acid formed by the direct action of sulphuric acid upon
it. The non- sulphurised fatty acids tend to the development of
blue shades with alizarin, whilst the ricinoleosulphuric acids tend
to produce yellow shades.
Diricinoleosulphuric acid is hydrolysed by caustic alkali, the
soda or potash salts of diricinoleic and sulphuric acids being
formed if the action take place at temperatures below 80° C.: but
by prolonged boiling with alkali, or treatment therewith under
pressure, water is taken up and ordinary ricinoleic acid regenerated
by reversal of the two reactions above indicated. In just the
same way ricinoleosulphuric acid becomes hydrolysed into sul-
phuric and ricinoleic acids, the action taking place extremely
readily in presence of hydrochloric acid. In presence of sulphuric
acid, Turkey red oil is apt to be yet further decomposed on
heating, osnanthic acid, inter alia, being formed: hence, in the
preparation of the oil care must be taken that overheating does not
take place } and similarly in washing out the excess of sulphuric
acid, (tc., with brine (to avoid solution of the soluble compound
sulphuric acids formed), otherwise hydrochloric acid is apt to
be formed and considerable loss of soluble acids occasioned by
* Comptes Rendus, 112, pp. 153 and 395; also, Journ. Soc. Chem.
Ind., 1891, p. 471.
.ACTION OF SULPHURIC ACID ON OILS AND FATS.
147
hydrolysis ; sodium sulphate is accordingly preferable to sodium
chloride as diminishing this tendency to loss.
According to Juillard* acids still more
highly "polymerised" than diricinoleic acid
are formed when sulphuric acid acts on
castor oil, three, four, and five molecules of
riciiioleic acid becoming condensed and dehy-
drated, with the formation of triricinoleic,
tetraricinoleic, and pentarwinoleic acids re-
spectively. He regards the first action as
giving rise, by partial hydrolysis and etherify-
ing action jointly, to the product,
0 . CO . C17H,., . 0 . SO.SH
OH
(0. CO. C,7H32. OH
which then loses a molecule of water forming
an anhydride, termed by him dicinolein sul-
phuric anhydride.
(0. CO. C17H,,. 0. SO.,
C3HS}0—
(0. CO. C17H32.OH
This reacts slowly with riciiioleic acid and
sulphuric acids forming the various poly-
ricinoleic acids above mentioned, and the
polyricinoleo sulphuric acids thence derived ;
so that commercial castor Turkey red oils are
highly complex mixtures.
Maumene's Sulphuric Acid Thermal
Test. — A considerable development of heat
usually attends the chemical action brought
about 011 mixing together a fixed oil and
strong sulphuric acid ; by making compara-
tive observations in precisely the same way
with standard pure oils, or known mixtures,
and the substance to be tested, useful infor-
mation can often be obtained as to the
character, and to some extent the amount,
of foreign admixture present. It is, how- pjg 3^
ever, impossible to lay down any precise
figures universally applicable in such cases, because the rate of
action, and consequently the rise in temperature, greatly de-
pends on the way in which the intermixture is effected, and
especially on the strength of the acid used. Commercial oil of
vitriol varies considerably in its strength, sometimes containing
* Journ. ,S'oc. Chem. Ind., 1892, p. 355; from Bulletin Soc. Chim., Paris,
1891, 6, p. 6,38.
148 OILS, FATS, WAXES, ETC.
96 to 97 per cent, of true sulphuric acid, H0S04, sometimes only
90 to 91 per cent., or even less. If the liquid be boiled in a
retort under ordinary atmospheric pressure until about a quarter
has distilled over, the residue when cool enough may be bottled
and kept for use, being acid of about 98 per cent, strength.*
Eig 31 represents a form of apparatus for applying the test ; a
graduated cylinder, B, is provided with an india-rubber stopper,
through which passes the stem of a thermometer, A, so graduated
that the divisions are all above the stopper ; a short piece of
quill tubing, 0, also passes through the stopper, serving as a
vent. 25 c.c. of oil are run into the cylinder, and then 5 c.c. of
sulphuric acid, the latter by means of a pipette applied to the
side of the cylinder, so that the acid falls to the bottom without
mixing with the oil. The stopper and thermometer being in-
serted and the temperature taken, the end of C is closed by the
finger, and the whole shaken up for a few seconds ; C is imme-
diately unclosed, and the thermometer watched, so as to note
the highest point to which it rises, and hence the range through
which the chemical action has heated the mass.
In order to diminish errors due to radiation and convection,
a small beaker may be used, jacketted outside with a somewhat
larger one, the interspace being filled with cotton wool or fibrous
asbestos. 50 grammes of oil and 10 c.c. of sulphuric acid are
convenient quantities, the two being at the same temperature to
start with ; the acid is run in slowly from a pipette, the mixture
being vigorously stirred with a thermometer, and about a
minute being allowed for the addition ; the temperature gra-
dually rises to a maximum as the stirring is continued, remains
nearly constant for a short time, and then falls again, the precise
amount of rise depending, to some extent, on the way in which
the admixture is made. When drying oils are examined,
Maumene recommends dilution with olive oil, so that the
temperature should not rise so high as to char the mixture
(paraffin hydrocarbons are regarded by other experimenters as
preferable) ; further, he recommends that trials should be made
with different proportions of oil and acid, e.r/.,f
50 grammes oil to 18 c.c. acid.
50 „ „ 36 „
100 „ „ 18
* Pure "monohydrated" sulphuric acid, H2S04, cannot be obtained by
evaporation; when a strength of 98 to 98 '5 per cent, is attained, the
temperature rises to a point where the substance dissociates into water
and sulphur trioxide, the latter passing off at the same rate as the water
vapour, so that acid of that strength distils unchanged. Pure H2S04 may
be obtained by adding the calculated amount of SOjj to oil of vitriol,
strengthened by evaporation as far as possible ; or by chilling the acid, and
draining off the unfrozen mother liquor from the crystals of H2S04 that
form. When heated, S03 is evolved, and acid of about 98 per cent, left,
which then distils unchanged.
•\ComptesRendus, xxxv., p. 572; also/owr/?. Soc. Chem. Ind., 1SSC, p. 361.
ACTION OF SULPHURIC ACID ON OILS AND FATS.
149
The following table exhibits some of Maumene's results,
together with those subsequently obtained by others ; numerous
other analogous values have been recorded, exhibiting more or
less marked differences according to the particular mode of
manipulation adopted : —
Maumene".
Allen.
Baynes.
Archbutt.
Degrees.
Degrees.
Degrees.
Degrees.
Menhaden oil, .
126
123 to 128
Cod liver oil, .
102 to 103
113
lie
Linseed oil,
103
104 to 111
104 to 124
Walnut oil,
101
...
...
Hemp seed oil,
98
Seal oil, .
92
...
Whale oil, northern,
...
91
Whale oil, southern,
...
92
Poppy seed oil,
74
...
86 to 88
Cotton seed oil, crude,
...
67 to 69
...
70
Cotton seed oil, refined,
...
74 to 75
77
75 to 76
Arachis oil,
67
47 to 60
Beechnut oil, .
65
...
Rape and colza oils,
57 to 58
51 to 60
60 to 92
55 to 64
Almond oil,
52 to 54
...
35
Horse foot oil, .
51
...
...
Tallow oil,
41 to 44
...
...
Lard oil, .
41
...
...
Sperm oil,
...
45 to 47
...
51
Bottlenose oil, .
...
41 to 47
42
Olive oil, .
42
41 to 43
40
4i to 45
Castor oil,
47
65
46
Neat's foot oil,
...
...
...
43
Oleic acid,
...
38-5
37-5
Obviously, an admixture of rape oil with linseed oil, or vice
versa, may be characterised with some degree of precision (the
former yielding a value of little more than half that given by
the latter), when the suspected sample is examined side by side
with samples of known purity mixed in known proportions (e.g.,
2 to 1, equal proportions, or 1 to 2, and so on). Similarly with
olive oil admixed with arachis oil, or with cotton seed oil ; or
sperm oil mixed with fish oil. According to Archbutt, olive oil
exposed to sunlight for some time develops considerably more
heat with sulphuric acid than the same oil kept in the dark ;
52°-o rise of temperature being noted by him instead of 41°'5.
A yet greater difference was observed by Ballantyne in the
case of olive oil exposed to light for six months, and agitated
daily so as to promote aerial oxidation (67° instead of 44°),
analogous differences being also observed with several other
kinds of oils similarly treated (p. 131).
Specific Temperature Reaction. — In order to render the
thermal test practically independent of variations in the strength
150
OILS, FATS, WAXES, ETC.
of the sulphuric acid used, Thomson and Ballantyne* make simul-
taneously a comparative valuation with water, and calculate the
ratio between the heat developed with the oil examined and
that with the water ; the resulting ratio they term the specific,
temperature reaction. Thus the following figures were obtained
with acid of different strengths, showing a considerably closer
concordance between the " specific temperature reactions " than
between the uncorrected values first obtained with the different
strengths of acids ; of course, exact agreement is not to be ex-
pected, as the heat development in the case of an oil is not
brought about solely by the mere physical admixture, but is also
influenced by the chemical changes set up, which necessarily are
apt to vary with the strength of the acid : —
Sulphuric Acid of 954
Sulphuric Acid of 96 8
Sulphuric Acid of 99
per cent. H2S04.
per cent. H2S04.
per cent. H2S04.
Substance Used.
Rise in
Tempera-
ture.
Specific
Tempera-
ture
Reaction.
; Rise in
Tempera-
ture.
Specific
Tempera-,
tu re
Reaction.
Rise in
Tempera-
ture.
Specific
Tempera-
ture
Reaction.
Degrees C.
Degrees C.
Degrees C.
Water,
38-6
100
41-4
100
46-5
100
(
36-5
95
39-4 95
44-8 96
Olive oil, <
34-0
88
38-1
92 44-2 95
\
...
39-0
94
43-8
94
Rape oil, .
49-0
1'27
...
58-0
124
Castor oil,
34-0
88 37-0
89
Linseed oil,
104-5
270
125-2
269
The following values for the specific temperature reactions of
various kinds of oils were thus determined : —
Nature of Oil.
Specific Temperature Reaction
Water = 100.
Olive oil (13 kinds examined),
Cotton seed oil (crude), ....
,, (refined — 2 kinds), .
Rape oil (5 kinds), .....
Arachis oil (commercial),
(refined), ....
Linseed oil (4 kinds), ....
Castor oil (2 kinds), ....
Southern sperm oil, ....
Arctic sperm oil (bottlenose),
Whale oil (pale),
Seal oil (4 kinds),
89 to 95
163
169 to 170
125 to 144
137
105
270 to 349 '
89 to 92
100
93
157
212 to 225
Cod oil (3 kinds),
Menhaden oil, .....
243 to 272
306
* Journ. Soc. Chem. 2nd,, 1891, p. 233.
ACTION OF SULPHURIC ACID ON OILS AND FATS.
151
F. Jean uses a special form of apparatus, termed by him a
<f Thermeleometer," "* for the determination of the heat evolved
in mixing sulphuric acid and oils (Fig. 32). A is a small vessel
40 mm. diameter and 60 high, enclosed in a felt-lined case, E ;
this holds the oil (15 c.c.) B is a U-shaped
tube, holding 5 c.c. of sulphuric acid (at 65°
B), furnished with a hollow glass stopper, to
which is attached a piece of rubber tubing,
Jl.V.; by blowing through the tubing the
acid is forced out of the reservoir, B, and
runs down on to the oil through the turned-
over narrow exit pipe. T is a thermometer
clamped to B. To use the instrument the
acid is introduced into B by removing the
stopper, and the oil run into A up to a
given mark representing 15 c.c.; the oil is
heated up to 40° to 50° C., the acid-holder
placed in it, and the whole allowed to cool
with occasional stirring to 30° ; A is then
placed in the casing, E, and the acid blown
over into the oil, B, the attached ther-
mometer being used as a stirrer, and the
highest temperature attained read off.
Colour Reactions produced by Sul- Fig. 32.
phuric Acid. — The table on p. 152 is given
by A. H. Allen, exhibiting the effect of placing a drop or- two
of sulphuric acid in the centre of about twenty drops of oil,
observing the colour before and after stirring, f
Some oils char more or less with sulphuric acid ; in such
cases, one drop of the oil may be dissolved in twenty of carbon
disulphide, and one drop of sulphuric acid added. Whale oil
thus treated gives a fine violet coloration, quickly changing to
brown, whereas, with sulphuric acid alone, a mere red or reddish
brown colour, changing to brown or black, is obtained.
Miscellaneous Colour Reactions. — Various other reagents
have been proposed as colour tests for oils — e.g., stannic chloride,
barium polysulphide, phosphoric acid, mercuric nitrate (alone or
with subsequent addition of sulphuric acid), aqua regia, caustic
soda, &c. For the most part, these give but little more informa-
tion than is afforded by the colour tests above described, except
in some few special cases ; thus, linseed oil boiled with caustic
soda gives a yellowish emulsion, but if fish oils are present, a
*Journ. Soc. Chem. Ind., 1890, p. 113; from Pharm. Chem., 1889, xx.,
p. 337.
t Various modifications of the colour test proposed in 1861 by Chateau
(by mixing oils with sulphuric acid) have been suggested by different
observers ; in some cases the test produced is subject to considerable
variation, according to the amount of acid used relatively to the oil, and
its strength.
152
OILS, FATS, WAXES, ETC.
reddish colour results. A solution of silver nitrate in alcohol
(2 parts nitrate to 12 of water, 88 parts alcohol added to the
liquid), when heated with about five times its volume of oil, is
OiL
Before Stirring.
After Stirring.
Vegetable Oils.
Olive oil, .
Yellow, green, or pale \
brown. /
Light brown or olive
green.
Almond oil,
Colourless or yellow. -
Dark yellow, olive, or
brown.
Arachis oil, . -|
Greyish yellow to \
orange. j
Greenish or reddish
brown.
Rape oil (crude),
Green with brown )
riiijjs. \
Bright green, turning
brownish.
(refined), |
Yellow with red or j
brown rings. \
Brown.
Mustard oil,
Bark yellow withl
orange streaks. /
Reddish brown.
Cotton seed oil (crude),
, , (refined),
Very bright red.
Reddish brown.
Dark red, nearly black.
Dark reddish brown.
Xiger seed oil, . -I
Yellow with brown 1
clot. J
Reddish or greenish
brown.
(
Yellow spot with )
Poppy seed oil, .
orange streaks or >
Olive or reddish brown.
(
rings. )
Linseed oil (raw),
Hard brown or green- 1
ish brown clot. J
Mottled, dark brown.
(boiled), .
Hard brown clot.
Mottled, dark brown.
Castor oil, .
Yellow to pale brown, j
Nearly colourless or
pale brown.
Animal Oils.
I
Greenish yellow or }
Lard oil, . . <
brownish with brown >
Mottled or dirty brown.
(
streaks. \
Tallow oil,
Yellow spot with pink \
streaks. J
Orange red.
Whale oil, . . j
Red, turning violet.
Brownish red, turning
brown or black.
Seal oil, . . j
Orange spot with pur- \
pie streaks. J
Bright red, changing
to mottled brown.
Cod liver oil, . j
Dark red spot with \
purple streaks. /
Purple, changing to
dark brown.
Sperm oil, .
Pure brown spot with \
faint yellow ring. j
Purple, changing to
reddish or dark
brown.
Hydrocarbon Oils.
Petroleum lubricating ~|
oil, J
Brown.
Dark brown with blue
fluorescence.
Shale lubricating oil, .
Dark reddish brown, -j
Reddish brown with
blue fluorescence.
Rosin oil (brown),
Bright mahogany )
brown. \
Dark brown with pur-
ple fluorescence.
(pale), .
Mahogany brown.
Red-brown with purple
fluorescence.
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Reddish brown.
Black brown.
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154 OILS, FATS, WAXES, ETC.
more or less reduced in many cases, developing a brownish red,
brown, or black colour ; * cotton seed, bitter almond, hemp,
linseed, neat's foot, and colza oils show the reaction most
markedly, especially the first named.
The table on p. 153 (by Schadler) exhibits synoptically the
results of various reagents on several of the more commonly oc-
curring oils, &c. ; the test with hydrochloric acid and sugar is made
by mixing equal quantities of the oil to be examined and hydro-
chloric acid of specific gravity 1-125 (about 1 c.c. of each), adding
a gramme of cane sugar, and shaking vigorously for some time.
SULPHUR CHLORIDE REACTION.
VULCANISED OILS.
The use of sulphur chloride in " vulcanising " india-rubber " is
well known ; a somewhat analogous change takes place wThen
this substance (preferably diluted with light petroleum oil,
carbon disulphide, or other suitable solvent) is intermixed with
certain oils, more especially linseed oil ; solidification ensues,
with the result of forming a more or less leathery mass, which is
employed to some considerable extent in the manufacture of
insulating coverings for electric mains and leads, and similar
purposes. During the action considerable quantities of hydro-
chloric acid are evolved, whilst the final product contains
sulphur, some of which is in a condition insoluble in carbon
disulphide, apparently combined with the oil constituents ; so
that the chemical action of sulphur chloride appears to be of a
far more deep-seated nature than that of nitrous acid (elaidin
reaction), where the solidification appears to be due simply to
polymerisation or isomeric re-arrangement of atoms. Although
no true oxidation takes place during the .treatment, the term
"oxidised oil" is often applied to this product in the trade,
probably because the solidification brought about is some-
Avhat akin in appearance to that effected when drying oils
are oxidised by exposure to air, forming solid products.
Another kind of "vulcanised oil" is obtained by mixing
fiowers of sulphur with the oil to be treated, and then applying
heat, much as in the process of vulcanising india-rubber. In
some cases the oils are previously partly saponified. By heating
linseed oil to about 230° C., cooling to 176° C. (350° F.), and
then stirring in sulphur, an india-rubber like mass is finally
obtained, useful in the preparation of rubber substitutes. As
with sulphur chloride, hydrogen appears to be removed during
the process, sulphuretted hydrogen freely escaping; this renders
the manufacture an especially foetid one unless great care be
taken to destroy the evil-smelling vapours evolved, by causing
* Cruciferous oils containing sulphur form black silver sulphide by this
treatment.
SULPHUR CHLORIDE REACTION.
155
them to pass through a furnace before escaping into the factory
chimney, or some analogous treatment.
The effect of chloride of sulphur (diluted with carbon disul-
phide) upon oils of various kinds is so far different that in
certain cases it may be employed to discriminate one from
another, or to test for admixture ; as in all other analogous
cases, comparison of the sample tested with genuine oils, treated
side by side, is necessary in order to obtain reliable results.
Bruce Warren finds * that when 5 grammes of oil are mixed
with 2 c.c. of carbon disulphide and 2 of a mixture of equal
volumes of carbon disulphide and yellow sulphur chloride (free
from dissolved sulphur) and the whole heated on a waterbath
till action commences, the products formed (after evaporating off
carbon disulphide) differ in weight and character according to the
nature of the oil, being partly soluble in carbon disulphide and
partly insoluble therein. Thus poppy seed and linseed oils gave
the following figures (5 grammes used in each case) :—
Poppy Seed.
Linseed.
Mixture of .Equal
Quantities of the Two.
;
Soluble, .
Insoluble,
1-96
4-50
0-78
5-58
MO
5-37
Total,
6-46
6-36
6-47
C. A. Fawsitt f employs sulphur chloride, S2C10, purified by
distillation, in the proportion of 2 c.c. to 30 grammes of oil,
operating as in the case of Maumene's sulphuric acid test ; very
considerable differences are observed with different oils as
regards the amount of heat evolved, the rate of its evolution,
and the formation or otherwise of hydrochloric acid gas ; thus,
the following figures were obtained, inter alia.
4 c.c. Sulphur Chloride to 30 grins. Oil.
Name of Oil.
Gas Evolution.
Rise in
Temperature.
Time in Rising.
Rise per Minute.
Degrees C.
Minutes.
Sperm,
Very small.
71
8
8-8
Seal, .
None.
112
5
224
Whale,
Slight.
91
3
30-2
Neat's foot,
j>
82
4
20-5
Eape,
None.
89
6
14-8
Cotton seed ,
Slight.
93
6
15-4
Linseed,
Considerable.
97
2
48-7
Olive,
Slight.
94
4
23-5
Cod liver,
Abundant.
103
3
34-3
Palmnut,
Slight.
9
7
1-4
Oleic acid,
Considerable.
99
G
165
Stearic acid, j None.
8
5
1-6
Chemical News, 1888, 57, p. 113. t Jour a. Sec. Chem. Ind., 1888, p. 552.
156
OILS, FATS, WAXES, ETC.
Name of Oil.
2 c.c. Sulphur Chloride to 30 grms. Oil.
Gas Evolution.
Rise in
Temperature.
Time in Rising.
Rise per Minute.
Degrees C.
Minutes.
Sperm,
Very small.
37
16
2-3
Seal, .
None.
45
10
4-4
Whale,
Slight.
57
6
9'4
Neat's foot,
»
51
7
7-3
Lard, .
»
40
16
2-4
Rape,
None.
53
10
5-3 '
Cotton seed,
Slight.
49
11
4-4
Linseed,
Considerable.
57
5
11-4
Olive,
Slight.
52
6
8-7
Castor,
Abundant.
56
2
277
Cod liver, .
) 9
55
4
13-7
Palm,
35
3
11 6
Palmnut, .
Slight.
5
9
0-5
Rosin,
Abundant.
31
' 7
4-4
Oleic acid, .
Considerable.
53
6
10-6
Stearic acid,
None.
5
7
07
It would hence seem that the relative figures obtained with
a given pair of oils often vary considerably according as 2 or 4
c.c. of sulphur chloride are used ; so that the value of the test as
applied to mixtures is somewhat doubtful.
CHAPTER VIII.
QUANTITATIVE REACTIONS OF OILS, &c.
A VARIETY of quantitative chemical tests are in use with the
object of obtaining information on various points connected with
the general chemistry of fatty matters, so as to afford evidence
in cases of suspected adulteration, <tc. Some of these depend on
the occurrence of saponification changes; others on different
principles. Amongst them may be reckoned the determination of
the amount of unsaponifiable matter present effected, as described
on p. 119, and the valuation of the amount of free fatty acids
present, not contained as glycerides (vide p. 116) ; in addition to
these, the following tests are also more or less frequently em-
ployed, named after the various chemists who have proposed
them : —
1 Kattstorfer' s Tes\ — Determination of the amount of potash
KCETTSTORFER'S TEST. 157
(KOH, equivalent 56'1) requisite to saponify 1,000 parts of sub-
stance— i.e., the permillage of potash requisite for saponification.
2. Heliner's Test. — Determination of the percentage of fatty
acids formed, insoluble in hot water.
3. JBeichert's Test. — Determination of the proportion of acids
formed, volatile with the steam of water when distilled under
certain arbitrary conditions.
4. llubl's Test. — Determination of the quantity of iodine
capable of direct combination with 100 parts of substance.
5. Benedikt and Ulzer's Test. — Determination of amount of
acetic acid formed by acetylating substances containing alcoholi-
form hydroxyl, and saponifying the product ; expressed as per-
millage of potash, equivalent to the acetic acid thus formed,
reckoned per 1,000 parts of acetylated product.
6. ZeiseUs Test. — Determination of amount of silver iodide
formed from the alkyl iodide (methyl, ethyl, &c., iodide), evolved
on heating with hydriodic acid ; expressed as the weight of
methyl (CH3 = 15), equivalent to the silver iodide thus formed
from 1,000 parts of substance.
KCETTSTOKFER'S TEST— TOTAL ACID NUMBER.
Owing to the different molecular weights of the various fatty
acids contained in glycerides and compound ethers, it necessarily
results that equal weights of different substances are chemically
equivalent to different amounts of alkali — i.e., that the quanti-
ties of caustic potash, for example, requisite to bring about the
saponification reaction
Glyreride. Caustic Potash. Glycero!. Potash Soap.
+ 3KOH = C5°3 + 3KOX
vary with the nature of X when equal weights of fatty matter
are used throughout. The greater the molecular weight of X,
the less potash will be requisite to saponify a given weight.
The quantitv of caustic potash requisite for saponification, being
a measure of the molecular weight of the fatty glycerides, &c.,
present, has been shown by Kcettstorfer to afford in many
cases a useful means of checking the nature and purity of the
oil, &c., examined. The weight of potash (KOH — 56'1) thus
consumed by 1,000 parts of substance (milligrammes of potash
per gramme) is accordingly known as the " Kcettstorfer number,"
{ Verseifungszahl) ; or otherwise as the " total acid potash per-
millage " or " total acid number" of the oil, &c., examined. The
determination of this value is effected in somewhat the same
fashion as that of the "free acid number" above described
158
OILS, FATS, WAXES, ETC.
(p. 116), by saponifying the oil with an excess* of alcoholic potash,
and back-titrating the unneutralised surplus ; in this way the
potash consumed represents not only the free fatty acid present
but also that liberated during saponification — i.e., the total fatty
acids present — whence the name.
Knowing the total acid number (Koettstorfer number), K of
a given substance, the mean equivalent weight of the substance
is readily calculated by the proportion
56-1
1,000
The value of x thus deduced is generally referred to as the-
" saponification equivalent " of the body in question.
Substance.
Total Acid Number, or
Koettstorfer Number
Chief Sources. (Permillage of Potash
required for
Saponification, &c.).
Saponification
Equivalent.
Glycerides.
Tributydn,
Butter fat,
557-3
100-7
Trivalerin,
Porpoise, dolphin,
and whale oils,
489-2
114-7
Trilaurin, .
Cokernut and
palmnut oils,
263-8
2127
Tripalmitin,
Palm oil, lard,
208-8
268-7
Tristearin,
Tallow, lard, cacao
butter,
189-1
296-7
Triolein, .
Olive and almond
oils,
190-4
294-7
Trierucin,
Colza and rape oils.
160-0 350-7
Trilinolin,
Linseed, hemp, and
walnut oils, 191-7 2927
Triricinolein,
Castor oil,
180-6 310-7
Compound Ethers.
Cetyl palmitate,
Spermaceti,
116-9 480
Myricyl palmitate,
Beeswax,
83-0 676
Ceryl cerotate, .
Chinese wax,
71-2 788
Dodecatyl oleate,
Sperm oil,
1247 450
Dodecatyl
doeglate,
Bottlenose oil, 120-9 464
The foregoing table represents the total acid numbers and
saponification equivalents of various triglycerides and compound
ethers of frequent occurrence ; in the case of glycerides the
molecular weight is three times the saponification equivalent,
whilst with compound ethers of monohydric alcohols it is
identical therewith.
Classification of Oils, &c., by Means of their Saponifica-
tion Equivalents. — The table on p. 159 has been arranged by
* Unless a more or less considerable excess be used, it is very difficult to
ensure complete saponification.
SAPONIFICATION EQUIVALENTS.
159
Percentage of KOH re- Saponification
quired lor Saponification. Equivalent.
; A. OLEINES—
Lard oil,
19-1 to 19 6 |\
Olive oil,
18-93 to 19 6 I
Sweet almond oil,
19-47 to 19 61 1
Arachis oil,
19 ^lo^9'66 } 285to29G
Tea oil, ....
Sesame" oil,
19-00 to 19-24 1
Cotton seed oil,
19-10 to 19-66
B. RAPE OIL CLASS—
/
Colza oil,
17-08 to 17-90
Rape oil,
Mustard seed oil,
17-02 to 17-64
17-4
313 to 330
Cabbage seed oil,
17-52
C. VEGETABLE DRYING OILS—
Linseed oil,
Poppy seed oil, .
18-74 to 19-52
19-28 to 19-46
\
Hemp seed oil, .
19-31
> 286 to 300
Walnut oil, .
19-60
L
Niger seed oil, .
189 to 19-1
)
D. MARINE OLEINES —
Cod liver oil, .
18-51 to 21-32
1*
Menhaden oil, .
19-20
Pilchard oil,
18-6 to 18-75
Seal oil,.
189 to 19-6
250 to 303
Southern whale oil,
19-31
Northern whale oil,
18-85 to 22-44
Porpoise oil,
21-60 to 21-88 J
E. BUTTER CLASS—
Butter fat,
22-15 to 23-24 241 to 253
Cokernut oil, .
Palmnut oil,
24-62 to 26-84
22-00 to 24-76
} 209 to 255
F. STEARINES, &c.—
Lard, ....
19-20 to 19-65
\
Tallow, ....
19-32 to 19-80
1
Dripping,
19-65 to 19-70
Butterine,
Goose fat,
19-35 to 19'65
19-26
V 277 to 294
Bone fat,
19 '06 to 19 71
Palm oil,
19-C3 to 20-25
1
Cacao butter, .
19-98
/
G. FLUID WAXES—
Sperm oil, . . .
12 34 to 14 74
380 to 454
Bottlenose oil, . . .
12-30 to 13-40
419 to 456
H. SOLID WAXES—
Spermaceti,
12-73 to 13-04
432 to 441
Beeswax,
9-2 to 9-7
...
Carnauba wax, .
7-9 to 851
I. UNCLASSED—
Shark liver oil, .
14 00 to 19-76
284 to 400
Wool fat (suint),
17-0
330
Olive kernel oil,
18-85
298
Castor oil,
17-6 to 18-15
309 to 319
Japanese wood oil,
211
266
Japan wax,
21-01 to 22-25
252 to 267
Myrtle wax,
20-57 to 21-17
265 to 273
Blown rape oil,
198 to 20 4
275 to 284
Colophony,
170 to 19 3
290 to 330
160
OILS, FATS, WAXES, ETC.
A. H. Allen * representing the percentages of caustic potash
required for the saponification of most of the usually occurring
oils, &c., deduced by collecting together the published results of
a number of observers, some of the values being deduced from
upwards of forty different samples.
Values but little removed from these have been subsequently
collected and recorded by Benediktf and Schadler,| including
various later valuations of the Koettstofer's values of other oils
and fats : —
Name of Oil, &c.
Schadler.
Benedikt.
Apricot kernel, ....
192-193
192-9
194-196
190-1-197
Almond, sweet, ....
190-192
187-9-196-1
Almond, bitter, ....
...
194-5-196-6
Butter,
225-230
227
Beeswax (yellow),
95-100 >
97-107
Bone oil, .....
190-191
...
Cacao butter, ....
198-200
Cokernut, .....
255-260
255
Colza,
177-178
175-179
230-231
230-5
Charlock,
176-177
Castor,
201-203
176-181-5
Carnauba wax, ....
79
Cotton seed, ....
194-195
191-210-5
Cod liver, medicinal, .
Cod liver, brown,
175-185
180-200
j 171-213-2
Galam butter, ....
192-193
...
Gundschit (lallemantia),
184-185
185-0
Hemp seed, ....
192-194
193-1
Hedge radish, ....
176-177
174-0
Japanese wax, ....
222-223
...
Linseed oil, ....
190-192
187 -4-1 95 -2
Lard,
195-196
Malabar tallow (piney tallow), .
191-192
...
Menhaden, .....
...
192
Maize, .....
188-189
188-1-189-2
Neat's foot, ....
191-193
189-191
189-191
Nut (Walnut), ....
196-197
1960
Olive, salad, ....
Olive, inferior, ....
191-193
186-188
| 185-2-196
Olive kernel, ....
188-189
188-5
193-194
192-8-194-6
Palm,
201-202
Palm kernel, ....
246-248
257-6
Pumpkin seed, ....
189-190
189-5
* Commercial Organic Analysis, vol. ii., p. 41, et seq. The "percentage
of caustic potash requisite " is obviously one-tenth of the Kcettstorfer number,
or permillage of potash necessary for saponitication.
t Analyse dtr Fette und Wachsarten, pp. 294 and 317.
£ Unttrsuchunrjen der Fette Oele und Wachsarten, pp. 134, 135.
SAPONIPICATION EQUIVALENTS.
161
Name of Oil, &c. Schadler.
Benedikt.
143-9
Pilchard,
Shark liver oil, ....
Seal oil, . . . . . 180-195
Fluid portion 263'0
186-187-5
84-5
191-196
Sesame, 192-193
Sunflower, 193-194
Spermaceti, .... 108
Sperm oil, 134
Suet (ox tallow, beef tallow), . 193-195
Tallow (sheep), .... 192-195
Tacamahac, .... 199-200
187-6-192-2
193
108-1
132-2
Unguadia, 190-192
Whale, 190-191
Whale, bottlenose, ...
Woolgrease, .... 169-170
1
190-191
197-3
Fluid portion 290 '0
Practical Determination of Saponiflcation Equivalents
of Glycerides, &c. — A known weight of the substance to be
examined (conveniently 2 or 3 grammes) is accurately weighed
up in a flask, and 25 c.c. (or other suitable quantity) of standard
alcoholic potash added (approximately seminormal); this should
be made from alcohol — not methylated spirit — that has been coho-
bated with caustic potash, and distilled so as to remove as far as
possible all compound ethers and other impurities that might be
resinised by potash, or otherwise partially neutralise alkali ;
methylic alcohol of high purity may be similarly used, preferably
after the same treatment. The whole is heated on a waterbath
with a reflux condenser attached, and gently agitated at intervals
until complete solution has taken place ; after a few minutes
more heating to ensure that saponification is complete, the un-
neutralised alkali is titrated by seminormal standard acid (pre-
ferably hydrochloric), using phenolphthalein as indicator. The
standardising of the alcoholic potash in terms of the acid is pre-
ferably effected by heating 25 c.c. on the waterbath, with an
inverted condenser attached, side by side with the oil examined,
and subsequently titrating ; the difference between the acid
required in the two cases thus directly represents the acid
equivalent to that formed by the saponification. If w be the
weight in milligrammes of oil taken, and n the number of c.c. of
normal acid equivalent to the acid formed by saponification (i.e., if
2n c.c. of seminormal acid be used, lOn of deciiiormal, and so on),
then the saponification equivalent E is given by the equation *
*1 c.c. of "normal" acid represents E milligrammes of fat, whence
n c.c. of acid are equivalent to 7iE milligrammes. Since this quantity = w,
162 OILS, FATS, WAXES, ETC.
and the total acid number (Kcettstorfer number = permillage of
potash, or tenfold the percentage, requisite for saponification) by
the equation
K = — x 56,100.
w
The determination of the total acid number is generally com-
bined with that of the free acid number ; the weighed quantity
of fat, <fcc., mixed with a little warm alcohol, is titrated with
alcoholic alkali, using phenolphthalein as indicator, so as to
determine the free acid number (see p. 116); excess of alkali is
then added and the determination of the total acid number pro-
ceeded with. Thus, suppose that 2-501 grammes (2,501 milli-
grammes) of Japanese wax contain sufficient free fatty acid to
neutralise 2 '5 c.c. of seminormal alkali (equal to 1-25 c.c. of
normal solution) ; whilst after adding excess of alkali, saponify-
ing, and back-titrating, 19-0 c.c. of seminormal fluid (equal to
9-5 c.c. normal) are neutralised in all; then the free acid and
1-25
total acid numbers are respectively--— , x 56,100= 2S'04, and
9.5
9 x 56,100 = 213-1 ; whilst the saponification equivalent is
2'SOI _
~W '3'
If A be the free acid number, and K the total acid number
(Koattstorfer number), the quantity K - A is a measure of the
proportion of compound ethers (esters, glycerides, &c.) present
in the substance examined, and may be conveniently termed the
ester number (Esterzald* JEtherzaliT) } thus in the above instance
the ester number is 263-3 - 28-04 - 235-26. In general, if
m c.c. of normal alkali are consumed in neutralising the free
acid present in iv milligrammes of substance, and n c.c. in
neutralising the total acids, the value of the ester number,
K - A, is given by the equation
K - A = m x 56,1CO - — x 56,100
w w
= ^L^X 56,100.
In the case of triglycerides, the quantity of glycerol theoreti-
cally obtainable from a given weight of substance is readily
it results that E = — . On the other hand, 1 c.c. of normal acid represents
56*1 milligrammes of KOH, whence n c.c. are equivalent to n x 56 1 milli-
grammes. Then w : n x 56 '1 : : 1,000 : K = -- x 56,100.
ESTER NUMBER. 163
deduced from the ester number : 3 x 56*1 parts of potash
neutralised by the acids liberated from the triglycerides, represent
92 parts of glycerol set free : hence, if S is the ester number, the
92
glycerol produced is Y~^Q^J x S = 0-5466 x S per mille, or
Ibo'o
•05466 x S per cent.; thus, a sample of groundnut oil, yielding
the total acid number 195-0, and the free acid number 5-0, and
consequently the ester number 195*0 — 5-0 = 190-0, would
theoretically yield 190-0 x -05466 * 10-39 per cent, of glycerol.
Proportion of Patty Acids formed by Saponifieation. —
Just as the average molecular weight of a mixture of triglycerides
or other compound ethers will depend partly on the molecular
weights of the fatty acids formed by saponification, and partly on
those of the alcoholic or glyceridic constituents, so will the
percentage of fatty acids obtainable vary in like manner. In the
case of a mixture of glycerides, where some of the fatty acids are
of low molecular weight, obviously a smaller percentage of fatty
acids will be formed than would be were all the fatty acids
of higher molecular weight. Thus, 100 parts of butyrin,
C3K5(O.C4HrO-)3, would theoretically yield 87 '4 of butyric acid;
whilst 100 parts of stearin, C3H5(O.C18H35O)3, would similarly
furnish 95 "7 parts of stearic acid.
In certain cases, useful information is obtainable by deter-
mining the total percentage of fatty acids actually produced,
more especially when, in addition to the total percentage, the
amounts respectively soluble and insoluble in water are also
deduced ; the information being in some cases further supple-
mented by determining the amount and nature of alcoholic or
glyceridic complementary products.
The total percentage of fatty acids can be reckoned from the
amount of alkali requisite for saponification (the Kcettstorfer
number determined as indicated on p-.'161) if the mean equivalent
of the fatty acids is known ; more usually, however, the latter is
the principal point to be examined, and the percentage of acids
requires to be directly determined ; from which value, together
with the quantity of alkali used, the mean equivalent weight of
the fatty acids is deduced. Thus, if 100 parts by weight of
substance yield a weight, wv of fatty acids (i.e., if wl be the
percentage of fatty acids found), and w<, parts of potash, KOH,
be required to neutralise these acids, the mean equivalent weight
of the acids is given by the proportion —
wa: 56-1 ::wi'.x = — x 56'1.
wa
If K be the total acid number (permillage of KOH, or ten times
the percentage) the mean equivalent weight of the fatty acids
will obviously be —
56>1 = x 56L
164
OILS, FATS, WAXES, ETC.
The term neutralisation number of the fatty acids (Versei-
fungszahl der Fettsauren) is conveniently employed to indicate
the quantity of potash (KOH = 56-1) neutralised by 1000 parts
,of the free acids. This value and the mean equivalent weight of
the free acids are related to one another in a fashion similar to
that exhibited by the total acid number, and the saponification
equivalent of the original fat or oil ; if N be the neutralisation
number of the free acids, and F their mean equivalent weight
(value of x as above), then
whence
and
S" : 56-1 :: 1000 : F,
_ 56,100
F
^ 56,100
F = T-
The following table represents the average neutralisation
numbers of the free fatty acids obtained from various kinds of
oils, &c. — i.e., the quantities of potash (KOH = 56-1) neutralised
'by 1,000 parts of mixed free fatty acids (Schadler) : —
Name of Oil, &c.
Almond, .
Arachis,
Cotton seed,
Castor,
Cod liver (med cinal),
Charlock,
Colza, .
Linseed,
Lard, .
Nut (walnut),
Olive, .
Palm, .
Palm kernel,
Poppy,
Suet (ox), ,
Sesame",
Sunflower,
Tallow (sheep)
Neutralisation Number.
204-205
196-197
204-205
187-188
202-204
180-181
181-182
198-199
215-217
208-209
199-200
206-207
265-266
204-205
205-206
197-198
201-202
206-207
In the case of a triglyceride, the calculated saponification
equivalent of the glyceride always exceeds the equivalent weight
of fatty acids produced from it by saponification by 12-67; for the
general reaction of saponification being equivalent to
CsH5(OrOs + 3H20 - C3H5(OH)3 + 3HOR
where R is a fatty acid radicle, it results that the molecular
weight (three times the equivalent) of the glyceride, G, plus
3 x 18 = 54 parts of water, is identical with the molecular
NEUTRALISATION NUMBER OF FATTY ACIDS. 165
weight of glycerol = 92, plus three times the equivalent weight
of the fatty acid formed by saponification, 3F ; whence,
G = 3F + 92 - 54,
and ^ - F + 12-67.
o
In similar fashion, in the case of a mixture of a triglyceride ,
and the fatty acid contained therein (e.g., tri stearin and stearic
acid), the mean saponification equivalent of the mixture will
exceed the equivalent of the fatty acid by a fraction of the
number 12 '6 7, expressing the proportion of fatty acid contained
as glyceride to the total fatty acid present. If S be the ester
QJ
number, and K the total acid number, this fraction is ^ ] whence,
, -K.
the mean saponification equivalent of the mixture, M, is given
by the equation
'M = F + - x 12-67.
Jv
Thus, supposing the free acid number to be 5 per cent. (^V) °f '•
the total acid number, so that the ester number is 95 per cent.
(^J) thereof, the relationship between M and F will be
M = F + II x 12-67,
= F + 12-04. ,
Similarly, if the free acid number be 10 per cent. (TTff) of the
total acid number,
M = F + 11-40.
Hence, as in the case of most oils and fats, the amount of free
acid is only a few per cents, of that of the total acids, it may be
taken as a general rule that the mean saponification equivalent of
a natural oil or fat exceeds the mean equivalent of the fatty acids
contained therein by about 12 ; and by a proportionately less
amount when the quantity of free fatty acid present increases
beyond a few per cents.
This relationship enables comparisons to be readily instituted
between the values deduced by the saponification of a fat or oil,
and by titrating of the fatty acids separated therefrom, when
expressed as equivalents ; whereas, such comparisons are much
less readily made by means of the potash permillages directly
obtained, viz., the "total acid number" of the glyceride, and
" neutralisation number" of the free acids thence derived (p. 164).
Since the saponification equivalent of a triglyceride exceeds
the equivalent weight of the fatty acid contained therein by
166 OILS, FATS, WAXES, ETC.
12 '6 7, it results that for fatty glycerides, where the equivalent
weight of the fatty acid contained lies between 250 and 330, the
percentage of fatty acid yielded by the glyceride lies between
950 33Q
°°' between 95'2
25CTT1W ' 330 + 12-67 '
and 96 -3 ; so that, for the great majority of natural oils and fats
containing only small quantities of free fatty acids, the rest being
glycerides, the yield of fatty acid per 100 parts of fat is close to
95 -75 parts. Fats containing a considerable amount of glycerides
of relatively low molecular weight, such as butter fat, cokernut
butter, and palm kernel oil, <fec., yield proportionately smaller
percentages of fatty acids ; on the other hand, if much free fatty
acid is present in the fat or oil examined, the percentage yield of
fatty acids from the mixture is proportionately increased.
REFINER'S TEST.
This test consists in determining that fraction of the fatty
acids formed on saponification and acidulation which remains
undissolved in hot water, repeatedly applied until no more acid
is dissolved. With most oils and fats this quantity differs but
little from the total percentage (about 95-5 to 96 per cent, as a
rule, supra] — i.e., only minute quantities of soluble fatty acids
are present ; but with cow's butter, cokernut butter, and some
few other substances the difference is much greater. Thus with
butter fat the total percentage is usually from 93 to 94, whilst
the percentage of insoluble acids (the Hehner number) is only
87 to 88. With the fatty glycerides employed in the manu-
facture of oleomargarine, the soluble acids are present in
only very small quantity, so that the insoluble acids amount to
95-96 per cent. ; hence, any considerable admixture of oleo-
margarine with genuine butter is detected by the increment in
percentage of insoluble acids found.
The following table represents the proportion of genuine butter
fat and foreign fats (margarine) present in a sample of mixture
yielding a higher Hehner number than genuine butter fat,
assuming this to give the value 87 '5, and margarine to give
95-5.
The same result is also obtainable by means of the formula
x = (H - 87-5) x 12-5,
where H is the observed Hehner number, and x the calculated
percentage of margarine."55"
* When cokernut butter (or the stearine thence isolated by chilling and
pressing) is substituted for oleomargarine from beef suet, &c., the above
table does not hold good.
HEHNER'S TEST.
167
Ilehner Xumber Found.
Percentage Present of
Genuine Butter Fat.
Margarine.
87 '5
100
0
88
93-75
6-25
88-5
87'5
12-5
89
81-25
18-75
89-5
75
25
90
68-75
31-25
90-5
62-5
37-5
91
56-25
43-75
91-5
50
50
92
43-75
56-25
92-5
37-5
62-5
93
31-25
68-75
93 '5
25
75
94
18-75
81-25
94-5
12-5
87-5
95
6-25
93-75
95-5
0
100
Other tests depending on principles somewhat similar to those
involved in Hehner's test have been proposed by other chemists
for use in special cases ; thus the difference in solubility of
barium salts has been proposed as a criterion instead of the
difference in solubility of free acids for butter analysis, &c.
A modification of this principle is utilised as a means of deter-
mining the relative proportions of stearic and oleic acids in
mixtures of the two based on the different solubilities of their
lead salts in ether (vide p. 112).
PRACTICAL DETERMINATION OF THE AMOUNT OF
FATTY ACIDS FORMED ON SAPONIFICATION
(SOLUBLE AND INSOLUBLE IN WATER), AND
THEIR AVERAGE EQUIVALENT WEIGHTS.
The neutralised alcoholic solution left after determining the
saponifieation equivalent (or the product obtained by saponifying
& larger quantity of fat, say 10 grammes, with alkali without
titratioii) is evaporated to drive off alcohol, dissolved in hot
water, and treated with an excess of acid (standardised or other-
wise, according to circumstances — vide infra) ; a few minutes
boiling decomposes all soap present, so that a clear layer of fused
fatty acids swims up to the top on standing. A weighed filter
(weighed in a dish after drying in the steam bath) is prepared
and wetted with water (otherwise fatty acids may pass through),
and the acidified fluid filtered through, the oily fatty acids
168 OILS, FATS, WAXES, ETC.
remaining on the filter being washed with boiling water until
no more acidity is found in the filtrate. The filter is then dried
inside the weighed dish, and thus the weight of insoluble acids
determined. If w grammes of oil give n grammes of insoluble
acids, the "Hehner number," H, or percentage of insoluble acids,
is obviously
H = n - x 100.
w
The fatty acids thus formed are dissolved in pure alcohol and
titrated with standard alcoholic alkali precisely as in the deter-
mination of the "free acid number" of an oil, &c. (p. 116). The
quantity of potash (KOH = 56*1) neutralised by the insoluble
fatty acids obtained from 1,000 parts of original substance is
conveniently referred to as the " insoluble acid potash per-
millage," or "insoluble acid number" of the oil, etc., examined.
The difference between the quantity of potash neutralised in
the determination of the saponification equivalent (total acid
number) and that thus found as the insoluble acid number, is
obviously the potash equivalent to the acids present that are
soluble in water ; this difference is conveniently referred to as
the "soluble acid number" of the oil, &c., tested. If the composi-
tion of these soluble acids is known or assumed (e.g., regarding
them as butyric acid in the case of butter fat), their weight is
reckoned from the alkali neutralised as percentage on the original
fat examined, and by adding this value to that deduced as above
for the insoluble acids, the percentage of total acids formed is
obtained.
For example, suppose 2,500 grammes of butter fat to be
saponified with 25 c.c. of seminormal potash, and that on
titrating the excess of alkali 4 '9 c.c. are found to be unneutralised
by the acids formed on saponification ; then the total acids
formed are equivalent to 25 — 4'9 = 20*1 c.c. of serainormal
alkali, or 10 '05 c.c. of normal alkali. Hence the total acid
number is
56,100 = 225-5,
and the saponification equivalent is
2,500
After separation of the insoluble fatty acids, these are found to
weigh 2-187 grms., and to neutralise 16 '6 c.c. of seminormal
alkali = 8'3 c.c. of normal alkali \ hence the insoluble acid
number is
2,500 x5f'10) = U6-5;
the percentage of insoluble fatty acids (Hekner number) is
PRACTICAL DETERMINATIONS. 169
=87 '48;
and their average equivalent weight is
i.e., 1 c.c. of normal alkali neutralises 263'5 milligrammes of the
mixed acids. Since the total acids neutralise lO'Oo c.c. of normal
alkali, and the insoluble acids 8-3 c.c., the difference = 1'75 c.c.
represents the soluble acids. This corresponds with the soluble
acid number
If it be supposed that the soluble acids are essentially butyric
acid (equivalent = 88), 1 c.c. of normal alkali will neutralise
88 milligrammes, and consequently 1'75 c.c. will neutralise 154
milligrammes = 6*16 per cent, of the 2,500 grms. of butter fat
employed. Hence the total percentage of fatty acids formed on
sapomfication is
Insoluble acids (Hehner number), . . 87 '48
Soluble acids (reckoned as butyric acid), . 6'1G
Total, . . . 93-64
The mean equivalent weight of the total acids is deduced thus —
Weight of insoluble acids, . . 2,187 milligrammes.
,, soluble ,, . 154 ,,
2,341
Since these neutralise 20*1 c.c. of seminormal alkali, equivalent
to 10*05 c.c. of normal alkali, the mean equivalent weight is
O QJ.1
w'°*1 _ 009-0
10-05
The soluble acids may also be directly estimated by employing
a known quantity of standard acid to decompose the soap left
after determination of the saponifi cation equivalent, and deter-
mining the acidity of the watery nitrate, using phenolphthalein
as indicator. Thus, in the above case, suppose that 25 c.c. of
seminormal acid were used to decompose the soap, and that 8 '4
c.c. of seminormal alkali were neutralised by the watery filtrate :
since the alkali present in the neutral soap represents 20 -1 c.c.,
25 - 20-1 == 4'9 c.c. of the acid used would remain unneutralised
in the filtrate; whence, 8'4 — 4*9 = 3-5 c.c. of seminormal acid,
equal to 1'75 c.c. normal, would represent the soluble acids as
before. In practice, this method is less accurate than the other,
as the dilution of the fluid and the unavoidable absorption
of carbonic acid from the air (which interferes with phenol-
ci CP i mo />
170 OILS, FATS, WAXES, ETC.
phthalein as an indicator) generally prevent so sharp a valuation
being obtained.
With the exception of butter fat and allied animal fats, and
cokernut and palmiiut oils, the amount of soluble acids present
in ordinary oils and fatty matters is usually so small as to be
negligible, so that the total acid number and the insoluble acid
number are sensibly identical — i.e., the amount of alkali
neutralised during saponification is practically identical with
that neutralised subsequently by the liberated fatty acids,
insoluble in water.
Correction for Anhydro derivatives, e.g., Stearolac-
tone. — Certain distilled oleines, Turkey red oils, &c., contain
stearolactone, the "inner" anhydride of 7 oxystearic acid (p. 39);
when this is heated with alcoholic potash, it forms potassium
oxystearate, which neutralises an equivalent of alkali (C18H36O3
= 300); but when the resulting soap is decomposed by a mineral
acid, stearolactone is reproduced. If the mixed fatty acids, &c.,
thus formed be titrated without heating, an insoluble acid
number, corresponding with only the free fatty acids, will be
indicated, the stearolactone not being converted into potassium
oxystearate instantaneously in the cold; so that an apparent
existence of soluble fatty acids is indicated by the difference
between the total acid number obtained at first, and the value
obtained during the titration of the free fatty acids — i.e., their
apparent neutralisation number. The difficiency, however, is
made up if the neutralised fatty acids, &c., be heated with excess
of alcoholic potash, and then back-titrated, so as to determine the
alkali neutralised by the formation of oxystearate ; from the
.amount thus neutralised the stearolactone can be calculated,
1 c.c. of normal acid representing 282 milligrammes. Or the
stearolactone may be dissolved out from the neutralised fatty
.acids by means of ether or benzoline, and directly weighed *
(p. 119).
Corrections for Free Fatty Acids and for Unsaponinable
Matters. — If the substance examined contain free fatty acids or
unsaponifiable matters the above methods require certain
rtH
corrections ; thus, the value E = — found as above for the
n
saponification equivalent, does not represent the true equivalent
of the glyceride or other compound ether present along with
other matters, but only the mean equivalent of all the substances
present (infinity in the case of non-saponifiable substances). If,
as is usually the case, the unsaponifiable matters present are
insoluble in water, the weight of substances obtained on saponi-
fying and weighing the liberated fatty acids, is too great by the
amount of unsaponifiable substances present ; and also by the
* Benedikt, Monatshefte fur Chemie, 11, p. 71.
CORRECTIONS. 171
weight of fatty acids originally present in the free state : these
are determined as described on pp. 116, 119.
Suppose that a weight of substance, W, when saponified with
alkali, neutralises n^ c.c. of normal fluid ; and, as the result of a
previous titration before saponifying, suppose that n.2 c.c. represent
the normal alkali equivalent to the free fatty acids present in the
same weight, W, and that w1 milligrammes is the weight of
these fatty acids. Further, let the weight of unsaponifiable
matter contained in W of substance be iv.2 milligrammes. Then
the saponifiable compound ethers, glycerides, &c., present weigh
W — iv -^ — w,-) milligrammes ; and the normal alkali neutralised
by them on saponification is n-^ - n.2 ; hence the corrected
saponificatioii equivalent of the saponifiable matters free from
impurities is
w " w ~ w
and the potash permillage for these saponifiable matters free from
impurities is
K' = "i-"2 x 50,100.
Sometimes it happens that during saponification products are
formed that are insoluble in water and consequently swim up to
the top when the resulting soaps are decomposed by a mineral
acid so as to separate the fatty acids formed by saponification ;
e.g., in the case of cetacean oils, waxes, &c., where alcohols of
high molecular weight, and not glycerol, are set free; in such
cases, in order to obtain a correct valuation of the fatty acids,
the quantity of such alcohols, &c., mixed with them must be
determined. * This is usually conveniently effected by evaporat-
ing to dryness the alcoholic solution obtained when the weighed
impure acids have been titrated (p. 164), and dissolving away the
alcohols, &c., with ether or benzoliiie, so. as to separate them from
the soap ; the filtered solution thus obtained is then evaporated,
and the residue weighed and subtracted from the weight of crude
fatty acids.
The equivalent weight of the fatty acids then will be
where iv is the weight in milligrammes of crude fatty acids,
tv that of alcohols, etc., admixed therewith, and n the number of
c.c. of normal alkali neutralised.
* Owing to saponification changes occurring on keeping or during
refining, it sometimes happens that considerable quantities of ,cet37lic,
dodecylic, &c., alcohols are contained as such in sperm oil, spermaceti,
beeswax, and similar substances, in addition to those existing as compound
ethers ; as much as 40 to 50 per cent, has been found in extreme cases
{Allen and Thomson).
172 OILS, FATS, WAXES,; ETC.
Mean Equivalent of Fatty Acids Contained in Soap.—
In the examination of soap it is often required to determine the
mean equivalent of the fatty acids present therein as potash or
soda soap; methods of calculation analogous to the above are
then used. In such cases the analytical methods used (Chap,
xxi.) usually give the following data : —
Percentage of total alkali present (reckoned say as Xa20), = a
,, alkali not combined with fatty acids (so
called "free alkali "), . . . . — b
,, free fatty acids formed on decomposition of
the soap by mineral acids (together with
unsaponified fat and neutral bodies, &c.), = c
,, unsaponified fat and neutral bodies, &c., . = d
Then 100 parts of material contain a — b per cent, of alkali
(reckoned as Na2O) combined as soap with fatty acids, which
soap again yields, on decomposition by a stronger acid, c - d per
cent, of fatty acids free from unsaponified fat and neutral bodies.
The mean equivalent E of these fatty acids is then given by the
proportion (31 being the equivalent of sodium oxide, Na.,0)
a - 6 : 31 : : c - d : E,
whence E = • x 31.
a - o
The fatty acids yielded by cokernut oil have an average equi-
valent weight of not far from 200, whilst those from tallow,
palm oil, and olive oil have much higher values, near 275, still
higher equivalent weights being possessed by the mixtures of
acids yielded by castor oil (near 300) and oil of ben and rape
oil (near 330°) ; cerotic and melissic acids from beeswax have
equivalent weights of 410 and 452 respectively. Hence in
many cases the numerical value of the equivalent weight of the
fatty acids affords a useful indication as to the nature of the oils,
&c., used in manufacturing the soap examined.
Calculation of Composition of a Mixture of Two Fatty
Acids from their Mean Neutralisation Number. — In certain
cases where a substance is examined known to be a mixture of
two different fatty acids, the relative amounts of the two consti-
tuents can be at least approximately calculated from their mean
neutralisation number. Thus in the case of a mixture of palmitic
acid (molecular weight = 256) and stearic acid (284), let the
neutralisation number of the mixture be n ; the mean molecular
weight of the mixture will accordingly be — — (p. 164). Hence
the following table gives the relative proportions of the two
acids : —
REICHERT'S TEST.
173
Percentage of
Mean Molecular Weight.
Palmitic Acid.
Stearic Acid.
256
100
0
258-8
90
10
2S1 -6
80
20
264-4
70
30
267-2
60
40
270-0
50
50
272-8
40
60
275-6
30
70
278-4
20
80
281-2
10
90
284-0 0
100
The following formula gives the same result :— Let S be per-
centage of stearic acid, and M the mean molecular weight ; then
S = (M - 256) x —
x&
= (M - 256) x 3-5716.
In similar fashion the relative proportions of any other two fatty
acids in a mixture thereof can be calculated.
REICHERT'S TEST.
Various natural oils and fats yield on saponification the alkali
salts of mixtures of acids, some of which are readily volatile with
the steam of water at ordinary pressure, and others practically
non- volatile. Reichert * has based on this a useful method for
the examination of butter as regards adulteration with other
kinds of fatty matter (oleomargarine, &c.), these adulterants
furnishing much smaller proportions of volatile acids. In prac-
tice, it is not convenient to continue the distillation until all the
volatile acid present has passed over, so that a particular method
of manipulation is employed, in order that an approximately
constant fraction of the volatile acids may be distilled off. For
this purpose 2-5 grammes of the fat to be examined are heated
with 25 c.c. of approximately seminormal alcoholic potash in a
flask with reflux condenser, until saponification is complete ; the
alcohol is evaporated off (by transferring to an evaporating dish),
and the residue dissolved in water, slightly acidulated with
dilute sulphuric acid, and made up to 70 c.c., of which 50 are
distilled offf The distillate is filtered if solid acids insoluble in
* Zeits. Anal. Chem., 18, p. 68.
t To avoid bumping, pumice stone with platinum wire coiled round should
be placed in the distilling vessel.
174
OILS, FATS, WAXES, ETC.
cold water have passed over, and titrated with decinormal alkali,
using phenolphthalein as indicator. Working in this way about
-| of the total volatile acids, soluble in water, of genuine butter
are obtained in the distillate.
The following table is given by A. H. Allen,* representing
the collected results obtained by himself and other analysts
employing this method of manipulating :—
C.c. of Decinormal
Substance of which 2'5 grammes are used.
Alkali neutralised by Percentage of KOII
Distillate (filtered neutralised.
when necessary).
MILK FATS —
Cow's butter, ....
12 -5 to 15 "2 2 -SO to 3 -41
Ewe's butter, ....
13-7
3-07
Goat's butter, ....
13-G
3-05
Porpoise's butter,
11-3
2-51
ANIMAL & VEGETABLE OILS & FATS—
Cokerimt oil,t ....
3-5 to 37
078 to 0-83
Palmnut oil, ....
2-4
0-54
Palm oil,
0-8
0-18
Cacao butter, ....
1-6 0-36
Butterine and oleomargarine, .
0-2 to 1-6
0-04 to 0-36
Whale oil, ....
37 to 12-5
0-83 to 2 -SO
Porpoise oil, ....
11 to 12
2-47 to 2-69
Sperm oil, ....
1-3
0-29
Bottlenose oil, .... 1*4
0'31
Menhaden oil, ....
1-2 0-27
Cod liver oil, ....
1-1 to 21 0-24 to 0-47
Sesame oil, ....
2-2
0-48
Cotton seed oil,
0-3
0-07
Castor oil, ....
1-4
0-31
Meissl i slightly modifies Eeichert's test by using 5 grammes
of fat instead of 2 -5; the evaporated alcoholic soap is dissolved in
100 c.c. of water, and acidified with 40 c.c. of 10 per cent,
sulphuric acid solution. 110 c.c. are distilled off, of which 100 is
filtered through a dry filter and titrated, the decinormal alkali
consumed being increased by one tenth, to allow for the 10 c.c.
not used. The results are usually somewhere about double those
obtained by Reichert's method of manipulation — i.e., are much
the same per given weight of butter, taking into account the
doubled weight of fatty matter used.
The following table is given by Schadler, representing the
number of c.c. of decinormal alkali neutralised by the volatile
* Commercial Organic Analysis, vol. ii., p. 46.
t By adding more water and continuing the distillation, a large amount
of solid fatty acid, mostly insoluble in water (chiefly lauric acid), can be-
distilled over in the case of cokernut oil.
J Dingier s Poly. Journ., 233, p. 229.
REICHERT'S TEST.
175
acids distilled off when the Reichert-Meissl test is employed
(5 grammes of material used) : —
Xame of Oil, &c.
Arachis, .
Almond,
Cotton seed,
Cokernut, .
Cod liver, .
Castor,
Colza, crude,
,, refined,
Lard,
Linseed,
Nut (walnut),
Olive,
Palm,
., kernel,
Poppy,
Seal oil,
Sesame',
Sunflower, .
Tallow (ox),
„ (sheep),
Several other modifications of Reichert's mode of manipulating
have been proposed by different chemists with the object of
obtaining greater accuracy ; thus Wollny * employs special
precautions to avoid the presence of carbon dioxide in the
distillate and eliminate its disturbing effect, and prescribes that
the distillation (using 5 grammes of butter fat) should always
last the same time, 30 minutes. Similarly, Leffmann and Beam
use a solution of caustic soda in glycerol instead of alcohol, to
diminish possible formation of volatile acids by the action of the
alkali on the alcohol. Methylic alcohol is used by others for
the same purpose. Admitting that pure butter fat gives a
Reichert-Wollny number = 27, and that the corresponding
number for average margarine is 2, then a sample of butter fat
mixed with margarine and giving the number R will contain
x per cent, of margarine, where
C.c.
of Decinormal Alkali.
0-4
0'55
0-95
7-3
0-4
4-0
0-90
0-58
MO
0-95
0-92
1-5
0-5
3-4
0-6
2-6
1-2
0-5
1-0
1-2
x = 100 x
— = 4 (27 -
The term "Reich ert number" (Reichert 'sche ZaJtl) is frequently
given to the figure expressing the number of c.c. of decinormal
alkali neutralised by the distillate obtained when operating in
the way prescribed by Reichert, using 2*5 grammes of substance;
and similarly the terms "Reichert-Meissl number" and "Reichert-
Wollny number "(IteicJwrt-MewsrscfoZahl and JReichert- Wollny' sche
ZaliT) to the corresponding figures obtained when Meissl's or
"Wollny's modification of Reichert's process is used (employing
* The Analyst, 1887, p. 203, et sea.; from the Milch Zeitung, 1887,
Nos. 32-35.
176 OIL?, FATS, WAXES, ETC.
o grammes of substance). The two latter numbers are each
approximately double the first on account of the larger weight of
material. To avoid confusion between these different values, it
is convenient to translate them into terms of caustic potash
(KOH = 56-1) neutralised by the volatile acid obtained from
1,000 parts of substance, to which value the term "volatile acid
number" (or volatile acid potash permillage) may be conveniently
applied ; this translation is effected by means of the formulae —
Volatile acid number = Reichert number . . x 2 '244
,, ,, = Reichert-Meissl number x 1'122
,, ,, = Reicherb-Wollny number x l'J22
The volatile acids thus indicated are usually considerably below
the total amount actually present; according to Allen, the defi-
ciency is somewhere about one-fifth in the case of butter fat, and
presumably in about the same proportion in other cases. When
a nearer approximation is requisite to the total volatile acid
present, water must be added to the residue in the retort and
distillation recommenced, and so on as long as acid vapours pass
over ; or more conveniently, steam may be blown through the
liquid from a separate boiling vessel.
BROMINE AND IODINE ABSORPTION.
Organic compounds containing a group of the character
— CR = CS - tend to combine with two atoms of a given
halogen such as bromine or iodine, forming a group of formula
- CKBr - CSBr - , or - CRI - CSI - . Accordingly, organic acids
thus constituted are capable of uniting directly with halogens to
an extent dependent on the number of times that such " doubly
linked " carbon groups occur ; thus oleic and ricinoleic acids,
which contain one such doubly linked pair of carbon atoms,
unite with Br.,.
Oleic Acid. Dibromostearic Acid.
C17H33.CO.OH + Br2 = C,7H33Br2 . CO .OH
Ricinoleic Acid. Dibromoxystearic Acid.
P TT fOH TC p TT -R /OH
Ci7H32 1 CQ OH C17H32Br2 j CQ OH
Similarly, linolic acid combines with Br4, as it contains two * such
doubly-linked pairs of carbon atoms.
Linolic Acid. Tetrabromostearic Acid.
C]7H31.CO.OH + Br4 = C17H31Br4. CO. OH
Whilst linolenic acid, containing 3 such pairs,! unites with Br0 —
Linolenic Acid. Hexabromostearic Acid.
C17H29.CO.OH + Br6 = C17H29Br6. CO . OH
* Or possibly a trebly-linked pair of carbon atoms, forming the group
— CJ— C -, which, by uniting with Br4, produces a group of formula
- CBr^- CBr,-.
t Or possibly one trebly-linked pair, and one doubly-linked pair.
BROMINE ABSORPTION. 177
In certain cases, the bromine addition products thus formed
are crystallisable, and thus afford the means of separating organic
acids from one another (pp. 27, 35, 36); in any case, by determining
the quantity of halogen fixed by a given acid or mixture of acids,
useful information is often obtained as to the nature of the fatty
acids present ; for instance, if a mixture of stearic and oleic acids
took up, say, 45 per cent, of its weight of iodine, since stearic
acid takes up no iodine, and oleic acid 90 per cent, of its weight,
it would result that the mixture contained the two acids in
approximately equal quantities. Methods for the determination
of the amount of oleic acid in mixtures of this kind are of
considerable practical utility; in particular, the author has
found the method useful in determining the proportion of oleic
acid contained in the " stearine " used for candle making.
Precisely the same remarks also apply to the glycerides of the
fatty acids, with the sole difference that their combination with
halogens generally takes place more slowly than is the case with
the fatty acids contained, or with the parent hydrocarbons of
these fatty acids.
As far back as 1857, attempts to utilise the reaction with
bromine for the practical discrimination of fats were made by
Cailletet, and subsequently by A. H. Allen, Mills, and others;
but although in certain cases useful results are thus obtainable,
in practice it is found that the use of iodine is preferable, more
especially when applied in the modified form proposed by Hiibl
(vide infra), where mercuric chloride and iodine are dissolved in
alcohol, and the compound solution allowed to act on the fat.
in this case, the product formed is not simply an iodine
addition product ; the mercuric chloride appears to be ntore or
less transformed into mercuric iodide, with formation of chloride
of iodine, so that the addition product contains both chlorine and
iodine; thus oleic acid, C18H34O2, treated with this reagent
becomes mostly converted into chloriodostearic acid, C18H34C1IO2,
and similarly in other cases. The chlorine thus added on is in
practice never reckoned as such, but as its equivalent in iodine ;
so that 282 parts of oleic acid, when treated with Hiibl' s reagent,
are regarded as combining with 2 x 127 = 256 parts of iodine,
although usually the compound produced is formed by taking up
127 parts of iodine + 35-5 parts of chlorine.
Bromine Process. — The bromine absorption process, as im-
proved by Mills and Snodgrass,* and Mills and Akitt,f consists
in dissolving bromine in carbon disulphide, or preferably carbon
tetrachloride, to a solution containing 0'6 to O7 per cent, of
bromine, and adding this to a solution of a weighed quantity
of oil in the same solvent, until no more combination takes place.
In the earlier experiments with carbon disulphide a slight excess
of bromine was added, and the colour, after standing 15 minutes,
* Journ. Soc. Chem. Industry, 1883, p. 435. t Ibid., 1884, p. 366.
12
178
OILS, FATS, WAXES, ETC.
Substance.
Percentage
of Bromine
absorbed.
Specific
Gravity at
ll°-12e.
Melting
Point.
Remarks.
Almond oil,
26-27
•9168
...
Expressed from bitter
almonds.
.
53-74
•9154
...
Expressed from sweet
almonds ; yellower.
Beeswax,
0-54
63-9
English, a few months
old ; very yellow.
>» •
0
632
Scotch, 8 years old ; pale.
0
...
62-9
,, 2 ,, yellow.
, , • •
0
...
63-3
" *• ' > »
Ben oil, .
52-95
•9198
...
Much solid fat.
.
50-89
•9161
...
No solid fat.
Camauba wax,
33-50
...
84-1
Cod liver oil, .
83-12
•9269
Scotch, 7 years old ; ran-
cid ; clear portion used;
1 hour's absorption.
»»
84-03
•9292
...
Norwegian, refined, 2
years old.
82-94
•9257
...
Japanese, 2 years old.
.
81-61
•9277
Scotch, 2 years old.
<
86-69
•9281
...
Crude, from liver refuse ;
a few months old.
.
83-01
•9318
...
Norwegian, 1 year old.
.
82-07
•9278
Scotch ,,
Croton oil,
46-66
•D441
...
20 hours' absorption.
Eucalyptus oil,
94-09
•8691
...
...
Horse fat,
35-67
...
...
Pasty ; well mixed.
Japan wax,
2-33
...
50-5
,, (another sample),
1-53
...
50-8
Java nut oil, .
30-24
...
...
...
Ling liver oil,
82-44
•9295
...
2 years old ; 1 hour's
absorption.
Maize germ oil,
74-42
•9262
4 years old.
Mustard seed oil,
46-15
•9152
East Indian.
Myrtle wax, .
6-34
...
44-3
...
Neat's foot oil,
38-33
•9147
...
Thick.
Niger seed oil,
35-11
•9244
...
Olive oil,
59-34
•9266
...
Thick brown ; ' ' best
sulphocarbon."
?9 * *
60-61
•9382
...
Thinner greener ; ' ' low
quality sulphocarbon."
Palm oil,
35-44
...
...
Crude old Calabar.
5 ) • *
34-96
...
...
,, Lagos.
Peach kernel oil,
25'40
•9175
...
...
Poppy oil,
Besin. (common),
Seal oil, .
56-54
112-70
57-34
•9244
•9241
...
Turbid; filtered.
Light colour.
Pale; 1 hour's absorption.
J 5 • • •
59-92
•9216
Dark.
Sesame oil,
47-35
•9250
...
...
Shark liver oil,
84-36
•9293
...
A few months old ;
1 hour's absorption.
Sunflower oil, .
54-32
•9391
Colourless ; about 16
years old.
Whale oil,
30-92
•9199
...
Norwegian white whale;
very thick.
>»
48-69
•8780
...
Bottlenose whale.
HUBL'S IODINE TEST. 179
compared with that of a known amount of bromine dissolved in
carbon disulphide, so as to obtain a colorimetric valuation of the
excess ; or the excess of bromine was estimated by adding
potassium iodide and titrating with thiosulphate. In the later
experiments with carbon tetrachloride, about Ol gramme of
oil was dissolved in 50 c.c. of tetrachloride, an excess of bromine
solution added, and after 15 minutes the excess back-titrated,
either by the coloration method,* by iodide and thiosulphate,
or by a standard solution of j3 naphthol in carbon tetrachloride.
The table on p. 178 gives the results of a number of deter-
minations thus made.
Iodine Process — Hiibl's Test. — The iodine absorption pro-
cess of Baron Hubl is thus worked, f An alcoholic solution of
mercuric chloride and iodine in pure 95 per cent, alcohol is pre-
pared by dissolving 50 grins, iodine in one litre of spirit, and
60 grms. corrosive sublimate in another litre, filtering the latter
if necessary, and mixing the two solutions ; preferably they are
kept apart and only mixed a day or two before use ; J the com-
pound solution rapidly loses strength (as regards free iodine) if
fusel oils are present in the alcohol, methylated spirit being wholly
inadmissible; in any case the liquid should be allowed to stand at
least a day before use, so that any small quantity of iodine-
consuming impurities may be eliminated as far as possible ; the
actual iodine strength must be determined from time to time to
allow for depreciation. From -2 to *3 grm. of drying oils, '3 to '4
of non-drying oils, or -8 to 1 -0 grm. of solid fat, is dissolved in
10 c.c. of pure chloroform (i.e., containing no iodine-destroying
impurity), and to the solution 30 or 40 c.c. of iodine solution
added, more being added if on standing awhile the brown colour
lightens materially ; enough solution must be added in all to
give a large excess of free iodine when the action is complete
after several hours standing. The excess of iodine is titrated by
adding some aqueous potassium iodide solution (10-15 c.c. of
10 per cent, solution, along with 150 c.c. of water), and then
standard sodium thiosulphate (about 24 grms. to litre, standard-
ised by means of pure sublimed iodine, or by pure potassium
dichromate) until the blue colour with starch paste is just
decolorised, the starch being only added when nearly all the free
* When the oil is yellow, as with certain fish oils, the redness due to
excess of bromine is best examined by viewing through a solution of
potassium chromate.
t Dingler's PolytecJt. Journal, 1884, pp. 253, 281 ; in abstract, Journ*
Soc. Chem. Intl., 1884, p. 641.
£ According to Say tzetf, mercuric bromide is preferable to corrosive sub-
limate, the solution being more stable. Some chemists only mix the two
solutions at the moment they are wanted ; but according to the author's
experience, this considerably increases the chances of error. If mercuric
chloride be not added at all (e.g., if a solution of iodine in carbon tetra-
chloride be used), the quantity of iodine absorbed is in some cases largely
diminished as compared with that taken up with Hiibl's fluid.
180 OILS, FATS, WAXES, ETC.
iodine is destroyed. As the excess of iodine is dissolved partly
in the aqueous liquor and partly in the chloroform, the whole
must be well agitated. Unless a considerable excess of free
iodine is present, and the whole allowed to stand for several
hours, defective results are apt to be obtained with glycerides, as
the assimilation of iodine with these bodies is not always rapid ;
free fatty acids combine with iodine more quickly. A good rule
is to use an excess of iodine approximately equal to the amount
absorbed, * and to allow the whole to stand until the next day
before titration of the uncombined iodine ; one or more blank
experiments being simultaneously arranged to allow for possible
depreciation in strength of the iodine solution during the period ;
this lengthened time is more especially requisite in the case of
oils absorbing large amounts of iodine. Thus the following
figures illustrate this point (Thomson and Ballantyne) : —
Iodine Number found.
Time of Absorption.
—— -,
— .
Seal Oil.
Linseed Oil.
2 hours.
136-6
175-5
4 „
140-8
1797
6 „
145-1
184-1
8 „ 145-8
1877
18 „ 145-8
187-7
Similar figures have been published by various other observers in
the case of glycerides absorbing large proportions of iodine, whereas,
with free fatty acids and glycerides absorbing but little iodine, the
reaction is ordinarily-found to be practically complete in 2 hours.
When the iodine absorption of free iatty acids is to be
determined," it is unnecessary to dissolve in chloroform ; the
alcoholic mercury-iodine solution may be added directly to the
weighed fatty acids, previously thinned a little by warming
with a small quantity of pure alcohol. The following table
represents the amounts of iodine theoretically taken up by 100
parts of the several acids and their respective triglycerides : —
« • • Iodine Absorption.
Acid.
Giyceride.
Hypogieid acid, ' - : .
Oleic acid,
CieH3002 • 100*00
Ci8H3402 9007
95-25
86-20
Erucic acid, . ; • - . ,'
. C22H4202 75*15
72-43
Ricinoleic acid,
Cj8H3403 85*24
81-76
Linolic acid, . - - C]8H3202
173-57 :
Linolenic acid, C]gH3002 • j 274'10
262-15
* In the case of oils absorbing large quantities of iodine, a still greater
excess is preferable, about twice the quantity absorbed. In all cases the
quantity of iodine used for the blank experiment should be approximately
equal to the excess employed.
IODINE TEST.
181
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182
OILS, FATS, WAXES, ETC.
In actual practice, Hiibl found that pure oleic acid took up
8 9 '8-90 '5 per cent, of iodine, and obtained the values quoted 011
p. 181 on examining a variety of fats and oils by different pro-
cesses simultaneously, the substances being divided into 7 classes,
according to the magnitude of the iodine absorption.
Schadler gives the following values as those most generally
found pertaining to various oils and fats, &c. : —
Name of Oil or Fat.
Iodine Number of
Oil, &c. Fatty Acids.
82-83
100-102
94-96
28-32
66 68
34
93-94
98-97
100-101
9-9-5
106-107
127
128-130
135-140
143-144
105
4-2
177-178
162
59-60
119-5
142-143
82-83
82
51-5
13-5-14
134-135
121
98-100
38-40
125-130
103-105
129
88
108
63
43-44
81-5-82
36
87-90
96-97
56-57
97-99
8-5-9-0
112-115
122-124
155
167
125
87-88
12
97-99
26-30
110-111
133-134
86-87
Apricot kernel,
Arachis,
Butter,
Bone, . .
Cacao butter,
Castor, . .
Charlock, .
Colza, . . .
Cokernut,
Cotton seed,
Curcas,
c-dlMS±r1> : :
Hedge radish,
Japanese wax,
Linseed,
Lallemantia (Gundschit),
Nut (walnut),
Olive (salad),
Olive kernel,
Palm, ....."
Palm kernel,
Poppy, ....
Pumpkin seed,
Rape seed, ....
Suet (ox tallow, beef tallow),
Seal, .
Sesam6, ....
Sunflower, ....
Sperm oil, ....
Spermaceti, ....
Tacamahac, . . "
Tallow (sheep), .
Ungnadia, ....
Wool grease,
The following tables represent the collected results published
IODINE TEST.
183
by numerous observers,* ' during the last few years, as the
amounts of iodine taken up by 100 parts of different oils and
fats : —
VEGETABLE OILS.
Name.
Minimum.
Maximum.
Average.
Fresh linseed oil, .
170
181
175
Commercial oil, .
148
181
170
Lallemantia oil, . . .
162
Hemp seed oil, . .
142
158
150
Nut oil, ....
143
152
146
Poppy seed oil,
134
142
138
Sunflower seed oil,
122
133
128
Curcas oil, ....
...
127
Pumpkin seed oil,
...
121
Maize oil, ....
...
120
Cotton seed oil,
102
Ill
108
Sesame oil, ....
103
112
108
Hedge radish oil, .
...
105
Rape seed oil,
99
105
101
Apricot kernel oil,
99
102
100
Almond oil,
96
102
98
Arachis oil, ....
87-3
103
96
Mustard oil,
...
...
96
Castor oil, .
83
85
84-5
Olive oil, .
81
84-5
82-8
Olive kernel oil, .
...
...
81-8
ANIMAL OILS.
Name.
Minimum.
Maximum.
Average.
Cod liver oil,
126
153
140
Seal oil, ....
127
128
127
Japanese cod liver oil,
...
...
120
Bottlenose oil,
...
...
99-5
Porpoise oil,
...
76'8
Neat's foot oil,
70-3
Bone oil, ....
66
70
68
Porpoise oil oleine,
30-9
49-6
40-2
Bottlenose oleine, .
...
32-8
* Hiibl, Moore, Dieterich, Wilson, Erban, Herz, Spiiller, Horn, Richter,
Kremel, Beringer, and Benedikt ; collated by Bsnedikt. — Analyse der Fette
und Wachsarten, 2nd edition, pp. 298 and 317.
184
OILS, FATS, WAXES, ETC.
SOLID FATS.
Name.
Minimum.
Maximum.
Average.
Cotton seed stearine,
89-6
Goose grease,
...
71-5
Hog's lard, ....
56
63
59
Macassar oil,
...
53
Bone grease,
46-3 55-5
52
Palm butter,
50-3 53-9
51
Oleomargarine. .
47'5 55-3 50
Laurel butter,
49
Ox tallow, ....
40
44 42
Sheep's tallow,
32-7 46-2 42
Wool grease,
36
Cacao butter,
34 37-7 36
Nutmeg butter, .
31
Butter fat, .
19-5
38-0
30
Palm kernel butter,
10-3
17-5
14
Coker butter,
7-9
9-4
9
Japanese wax,
...
4-2
Slightly higher values still for some of the drying oils have
been recently deduced by Holde in the course of an investigation
on the sources of error in the Hiibl test,* the cause being
assigned to more complete saturation with iodine through use
of a larger excess of solution. Thus —
Linseed oil, 179 to 180
Hempseed oil, 175
Poppy seed oil, 139 to 143
Sesame" oil, 106 to 109
Cotton seed oil, 110 to 115
Common rape oil, 100 to 108
Refined rape oil, 100 to 107
The following values have also been recorded for the mixed
fatty acids from various commercial oils : —
Morawski and Demski.
Williams.
Linseed oil acids, . . .
Hempseed oil acids,
Cotton seed oil acids, .
Sesame oil acids, . . .
Rape seed oil acids,
Arachis oil acids, . . .
Castor oil acids, . .
Olive oil acids, .....
155 -2 to 155 -9
122-2 to 125 -2
110-9 to 111-2
108-9 to 111-4
96-3 to 99-02
95-5 to 96-9
86 -6 to 88-3
86-1
178-5
115-7
105*6
93-9
90-2
Owing to the tendency towards absorption of oxygen exhibited
by drying oils and the fatty acids obtained from them, there is
* Journ. Soc. Chem. Ind., 1891, p. 954; from Mitth. Kcnigl. tech.
Vcrsuchs, Berlin, 1891, 9, p. 81.
IODINE TEST. 185
always a liability to obtain somewhat different results with free
fatty acids as compared with the original oils from which they
were obtained, owing to partial oxidation during isolation and
drying. As a rule, absorption of oxygen seems to diminish the
iodine absorption as might, a priori, be expected.
Neglecting this alteration, the amounts of iodine absorbed by
an oil, &c., and by the fatty acids thence obtainable, necessarily
stand to one another in the inverse ratio of their respective
mean equivalent weights ; for if E be the saponification equiva-
lent of an oil, and F the mean equivalent weight of the fatty
acids thence obtainable, quantities of oil and free acid in the
respective proportion of E to F will combine with the same
quantity of iodine ; so that the iodine taken up by 100 parts of
oil will be ^ times that taken up by 100 parts of fatty acids ;
.hi
i.e., if I be the iodine number of the oil and I' that of the fatty
;icids —
and
<•=!'•
If the oil, &c., consist wholly of triglycerides, E = F + 12 -67
(p. 165); whence
F + 12 67
~~
Hence for fatty acids of molecular weight between 250 and 330,
the iodine number of the fatty acids is between 5'1 and 3-8 per
cent, greater than that of the original oil ; so that for the great
majority of natural oils and fats, the iodine number of the free
fatty acids exceeds that of the oil by an amount sensibly close to
4-5 per cent, of the latter value.
Obviously, in some of the cases above tabulated, a notable
difference must have subsisted between the samples used for the
determination of the iodine number of a given oil, and of that of
the fatty acids derived from the same kind of oil, since the latter
values are, in some instances, less than the former ones instead
of exceeding them by about 4 '5 per cent, of their value.
The theoretical amount of iodine corresponding with 100 parts
of pure olein is 86-2 parts. From the numbers above tabulated,
it is obvious that many of the fluid vegetable oils, usually
regarded as non-drying (arachis, almond, apricot kernel, &c.),
contain some small amount of glycerides of the linolic or drying
class, since their iodine absorptions exceed 86 -2 ; a fortiori, with
oils of the intermediate class exhibiting a slight amount of
186
OILS, FATS, WAXES, ETC.
drying quality (cotton seed, sesame, sunflower, &c), a larger
iodine absorption is observed, corresponding with a still more
marked proportion of drying oil constituents.
ACETYLATION TEST — BENEDIKT AND
ULZER'S TEST.
When organic substances containing alcoholiform hydroxyl are
heated in contact with acetic anhydride, an action takes place
which may be regarded as the converse of saponincation or
hydrolysis ; the hydroxylated body, X . OH, acts upon the
anhydride in accordance with the equation —
Alcohol. Acetic Anhydride. Compound Acetic Ether. Acetic Acid.
X-OH + 8$$}° = X.O.C.H.O + C2H3o!0
giving rise to a compound ether. Polyhydroxylated bodies
behave in the same way, one acetyl group being taken up for
each alcoholiform hydroxyl group present ; thus glycerol treated
with acetic anhydride becomes transformed into triacetin in
accordance with the equation —
Glycerol. Acetic Anhydride. Triacetin. Acetic Acid.
CH2 . OH CH, . O . C,H30
CH . OH + 3(CoH30)oO = CH. 0 . aH30 + 3C.,H4O,
CH2 . OH CH2 . 0 . CoH30
On this reaction is based a method for the analytical examination
of commercial glycerol (Chap, xxn.) Benedikt and Ulzer have
also attempted to utilise this reaction to distinguish hydroxylated
organic acids (like oxystearic and ricinoleic acids) from non-
hydroxylated acids, such as stearic and palmitic acids. Their
method is based on the assumption that acetic anhydride exerts
no action on the hydroxyl of the CO . OH group of an organic
acid, but does act, in accordance with the above equation,
on any alcoholiform hydroxyl contained therein ; so that if, for
example, stearic acid be treated with acetic anhydride, and the
product heated wrih water so as to decompose excess of acetic
anhydride, simply unchanged stearic acid results;* whereas, if
oxystearic acid be similarly treated, acetyl oxystearic acid is
produced, thus —
Oxystearic Acid. Acetic Anhydride. Acetyl Oxystearic Acid. Acetic Acid.
OH C,H30 ) n \0. CoHsO
CO . OH C2H30 \ U ^ITUM j co . OH
The acetylated acids thus formed are stated to be moderately
stable, not being appreciably hydrolysed by the action of the hot
* This assumption is entirely at variance with the results obtained by
Lewkowitsch ; vide infra.
ACETYLATION TEST — BENEDIKT AND ULZER's TEST. 187
water requisite to decompose the excess of acetic anhydride pre-
sent. Accordingly, if after thus removing excess of acetic anhy-
dride, the resulting acetyl acid be titrated with standard alkali,
one equivalent of alkali will be directly neutralised ; whilst if it
be heated with excess of alcoholic alkali so as to saponify it,
reproducing oxystearic acid and acetic acid, thus —
Acetyl Oxystearic Acid. Water. Oxystearic Acid. Acetic Acid.
+ H,0 C17H34 + CoH40
two equivalents will be neutralised in all, the second by the
acetic acid formed. In the case of a mixture of acids containing
hydroxylated and non-hydroxylated constituents, the proportion
of the latter can be estimated by determining the extra amount
of potash neutralised on saponification, as compared with that
neutralised directly. The term " acetyl number " (acetylzahl],
is used to indicate the weight of potash (KOH = 56*1) neutral-
ised by the acetic acid formed from 1,000 parts of mixed
acetylated product.*
The acetylation process is carried out thus : — The free fatty
acids formed by saponifying a given sample of oil and decom-
posing the soap by a mineral acid, are boiled for two hours with
an equal volume of acetic anhydride in a flask with inverted
condenser attached ; the mass is then boiled for half an hour
with about 20 parts of water ; the acetic acid solution formed is
siphoned off, and the treatment with boiling water repeated three
times, so that finally the water is free from acidity after boiling
for half an hour. The acetylated product is then filtered through
a dry filter paper to remove water, and a weighed quantity
dissolved in pure alcohol. Standard alcoholic potash is added to
neutrality, and the amount neutralised noted; more than as much
again is then added, and the whole heated to boiling, whereby
the acetyl derivative is saponified ; the unneutralised alkali is
then back-titrated. Thus in the case of the fatty acids from a
sample of castor oil the following figures were obtained :f — 3-379
grammes of acetylated product neutralised 17 '2 c.c. of seminormal
potash, whence the " acetyl acid number " is 142-8. After
* Benedikt and Ulzer term the potash directly neutralised by 1,000 parts
of mixed acetylated product, the "acetyl acid number " (acetylsaurezahl),
and the total neutralised on saponification (sum of acetylzahl and acetyl-
fiiiurezahl) "the acetyl saponification number" (acetylverseifunyszahl).
Thus the theoretical values tor acetyl oxyoleic (ricinoleic) acid are —
Acetyl number, . . . 165'0
Acetyl acid number, . . . IGo'O
Acetyl saponification number, . 330 '0
t Benedikt, Analyse der Fette und Wacltsarten, 2nd edition, 1892, p. 114.
188
OILS, FATS, WAXES, ETC.
addition of 32 -8 c.c. more potash and boiling, 14*3 c.c. were found
to be unneutralised, whence 18 '5 c.c. represent the acetic acid
formed on saponification, giving the " acetyl number" 153-6, and
the "acetyl saponification number" 142-8 + 153-6 = 269-4.
Since the acetyl number exceeded the acetyl acid number, it would
hence result that some amount of a dihydroxylated acid was pre-
sent, especially as the mixed acids of castor oil contain a small
quantity of stearic (non-hydroxylated) acid to begin with (vide
infra}.
Operating in this way, Benedikt and Ulzer found the following
values for various oils : — *
Oil Used.
"Neutralisation
Number" of
Fatty Acids
before
Acetylation.
Acetyl Acid
Number.
Acetyl
Number.
Acetyl
Saponification
Number.
Arachis,
198-8
193-3
3-4
1967
Cotton seed, .
199-8
195-7
16-6
212-3
Croton, .
201-0
1957
8-5
204-2
Hemp seed, .
199-4
196-8
7'5
204-3
Linseed,
201-3
196-6
8-5
205-1
Almond,
201-6
196-5
5-8
2023
Poppy seed, .
200-6
194-1
13-1
207-2
Nut, .
204-8
198-0
7-6
205-0
Olive, .
197-1
197-3
4-7
202-0
Peach kernel,
202-5
196-0
6-4
202-4
Castor, .
177-4
142-8
153-4
296-2
Rape,
182-5
178-5
6-3
184-8
Sesame, .
200-4
192-0
11-5
203-5
"Soluble castor oil "
184-5
62-2
246-7
J. A. Wilson f found the following average values for castor,
olive, and cotton seed oils : —
Acetyl Acid
Number.
Acetyl Number.
Acetyl Saponification
Number.
Castor oil,
Olive oil, .
Cotton seed oil,
136-7
170-0
189-5
155-0
360
21-0
291-7
2060
210-5
Obviously these figures do not agree very sharply with the
preceding ones. If the results of the acetyl test could be re-
garded as perfectly trustworthy, these values would indicate the
existence of more or less considerable amounts of hydroxy acids in
all the samples examined, amounting, in the case of the cotton seed
and sesame oils examined by Benedikt and Ulzer, to 6-8 per cent,
of the total acids present, and to much larger amounts in the
* Monat'hefte f. Chemie, 1S87, S, p. 41.
•\Journ. Soc. Chem. Intl., 1892, p. 495.-
ACETYLATION TEST. 189
case of the olive and cotton seed oils examined by Wilson. The
figures, however, do not exhibit such concordance as to be
unexceptionable ; the effect of acetylating the hydroxylated con-
stituents of a mixture of acids containing only a small proportion
of hydroxylated acids would be to cause the neutralisation number
of the acetylated fatty acids (the acetyl acid number) to be only
slightly less than their neutralisation number before acetylation,
whereas the observed differences are materially larger. Thus
the neutralisation numbers of oleic, oxyoleic, and acetyl oxyoleic
acids are respectively 198-9, 188-25, and 165-0; whence a
mixture of 90 parts oleic acid and 10 parts oxyoleic acid would
have the neutralisation number 197*9 ; and after acetylation
would furnish a mixture of oleic and acetyl oxyoleic acids having
the neutralisation number (acetyl acid number) 195'5, or only
2*4 less than the original mixture. Similarly a mixture of
9o parts oleic acid and 5 parts oxyoleic acid would have the
neutralisation number 198-4 before acetylation, and 197*2 after,
giving the difference 1-2. The actual differences deduced from
the above figures obtained by Benedikt and Ulzer with oils other
than castor oil, vary between — 0*2 (olive oil) and +8-4 (sesame
oil), but in most cases amount to from 5 to 6; strongly suggesting
that some cause is at work abnormally diminishing the " acetyl
acid number " by some units, and in consequence giving an ap-
parent " acetyl number " of some units in magnitude, the result
of this cause, and not of the existence of hydroxy acids in the fatty
asids examined. The same conclusion also results from the figures
obtained with castor oil acids, as the supposition that a consider-
able percentage of dihydroxylated acids is present is manifestly
untenable.
Lewkowitsch has made some observations that throw light on
the probable cause of these discrepancies.* His results indicate
that by the action of acetic anhydride in excess the higher acids
of the acetic family (such as lauric, palmitic, and stearic acids,
&c.) become more or less completely converted into the corre-
sponding anhydrides.f When the products freed from the
excess of acetic anhydride by the action of water are neutralised
by alkali, a diminution in the apparent amount of free acid is
noticed proportionate to the amount of fatty anhydrides present
not decomposed by the water treatment ; and when the neutral-
ised substance is heated with excess of alcoholic alkali, and
subsequently back-titrated, a quantity of alkali is neutralised
proportionate to the fatty acid formed by the hydration of the
* Proceeding* of the Chemical Society, 1890, pp. 72 and 91.
t Anschiitz found [Aimalen d. Chem. Pharm. (1884) 226, p. 6] that when
acetic anhydride and benzoic acid were heated together in a sealed tube at
220° benzoic anhydride was produced ; whilst the dibasic acids, succinic,
camphoric, orthophthalic, and diphenic acids were largely transformed into
their respective anhydrides by heating with acetic anhydride at 120°
to 150°.
190
OILS, FATS, WAXES, ETC.
fatty acid present; so that an apparent "acetyl number" is
obtained even when no alcoholiforin hydroxyl whatever is present
in the body examined. Thus he obtained the following figures
with samples of capric, lauric, palmitic, oleic, stearic, and cerotic
acids in a state of only approximate purity so far as chemical
identity is concerned, but any rate free from any notable amount
of hydroxy acids :—
NeutraHsutio
n Number.
Acetyl
Fatty Acid Used.
Theoretical
Acetyl Acid
Number.
Acetyl
Number.
Saponification
for pure
Found.
1
fatty acid.
Capric,
326-2
318-05
176-40
174-00
350-40
Lauric,
280-5
273-02
161-50
132-49
293-99
Palmitic,
219-1
213-4
143-53
82-60
222-13
Oleic, .
198-0
183-0
116-50
125-55
242-05
Stearic,
197-5
203-0
138-89
82-29
221-18
Cerotic,
13t>-8
1284
73-87
68-23
142-10
From these figures it obviously results that but little reliance
is to be placed on the result of the acetylation test for alcoholi-
form hydroxyl in fatty acids when based simply on the titra-
tioii process above described. Better results, however, can
be obtained by modifying the test in the way proposed by
Lewkowitsch •* the acetylated product is saponified with alcoholic-
potash, the alcohol boiled off, and the residue distilled with
dilute sulphuric acid, much as in Reichert's test (p. 173). Any
acetic acid formed by hydrolysis of acetyl derivatives is thus,
distilled over, and may be titrated by means of standard alkali
and phenolphthalein. In this way dioxystearic acid (from oleic
acid by alkaline permanganate) was found to form the anhydride
O TT /Q p TT r\\ rir\ \
of diacetyloxystearic acid, p17TT84 /Q ' p2TT8O»2 TO I ^' on ^rea*~
ment with acetic anhydride ; from this acetic acid was obtained
on saponificatioii and distillation in quantity but little below
the theoretical amount. A revision of the fatty acids obtainable
from oils and fats, &c. (as regards the amount of hydroxylated
constituents present), based on the acetyl test thus applied
would be desirable, but as yet does not appear to have been
made.
On the other hand, the acetylation test gives good results with
bodies not of an acid character, containing alcoholiform hydroxyl,
more especially in the case of the higher homologues of ethylic
alcohol : thus in the examination of waxes and bodies generally
that give rise to higher alcohols, the amount of hydroxylated
substances present may be measured by conversion into com-
* Journ. Soc. Chem. Ind, 1890, p. 842.
METHYL IODIDE TEST — ZEISEI/S TEST. 191
pound ethers by means of acetic anhydride, and determining the
permillage of potash neutralised on saponifying the product.
Thus pure cetylic alcohol, C16H33 . OH, furnishes an acetyl deri-
vative, cetyt acetate, C16H33 . O . C2H3O, of molecular weight 284—
i.e., 284 milligrammes of cetyl acetate will furnish 60 milligrammes,
of acetic acid on saponification, neutralising Ic.c. of normal potash
solution containing 56'1 milligrammes of potash (KOH); whence
the "acetyl number" of cetyl acetate is ^ . x 1000 = 197'5.
If a given sample of cetyl alcohol (known to be admixed with
foreign matter not capable of forming acetyl derivatives) furnish
an acetyl derivative of which the acetyl number is found to be 98,
obviously about one half of the substance is cetylic alcohol. A
more exact value is obtained by determining the quantity of
foreign matter present, subtracting that from the weight of
acetylated product, and reckoning the acetyl number on the
difference as 1000, in a way similar to that adopted in the parallel
case of the determination of the Koettstorfer number of a saponi-
fiable body after correction for unsaponifiable matters present
(p. 171).
In the case of impure glycerol the acetylation test is employed
in a similar way ; 92 parts of pure glycerol would furnish 3 x 60
= 180 parts of acetic acid on saponification of the triacetiii
formed therefrom, capable of neutralising 3 x 56 '1 =-- 168 -3 parts
of potash. If a given sample of impure glycerol were found to
neutralise n parts of potash per 92 of substance, the percentage
M
of glycerol present would be TgcTTo x 100. Or otherwise, 92 milli-
grammes of pure glycerol would furnish acid neutralising 3 c.c.
of normal alkali solution ; hence if a weight w milligrammes of
impure glycerol furnish acid neutralising x c.c. the percentage
I x 92
of glycerol would be x 100 •»— . x 3066-7.
IV W
Iii the examination of the unsaponifiable matters left 011 treat-
ing oils and fats, &c., with alkalies (p. 121), the substance may
conveniently be converted into acetyl derivative by treatment
with acetic anhydride, boiled with water to decompose excess of
anhydride, crystallised from alcohol, and examined as to the
acetyl number obtained on saponification of the product ; choles-
terol acetate (006H43 . O . C.,H3O) and its isomerides thus give the
number 135 -5.
METHYL IODIDE TEST— ZEISEL'S TEST.
Compound ethers of methylic alcohol and its next higher
homologues do not appear to have been hitherto recognised as
192 OILS, FATS, WAXES, ETC.
important constituents of natural fixed oils and fats, although
the corresponding compounds of the higher homologues of
methylic alcohol, such as cetylic alcohol, are well marked con-
stituents of certain cetacean oils, waxes, &c. Many essential
oils, however, contain constituents of analogous character —
e.g., oil of wintergreen, largely consisting of metliyl salicylate,
( OTT
C6H4 -j £Q Q £jT . Another class of essential oils containing
the methoxyl group (O . OH3) also exists, where the hydrogen
displaced by methyl is alcoholiform in character, and not con-
tained in the organic acid group CO . OH ; thus, anetkol or anise
oil camphor is the methylic ether of a phenoloid derived from
allyl-benzene, C3H5. C(.H4. 0. CH.,. When substances containing
a methoxyl group are heated in contact with hydriodic acid, a
reaction is brought about whereby the methyl group is elimi-
nated in the form of methyl iodide, thus —
Methoxyl Compound. Hydriodic Acid. Methyl Iodide. Hydroxyl Compound.
X . 0 . CH3 + HI CH3I + X . OH
A test for the presence of methoxyl in certain bodies (e.g.,
codeine) based on this action was employed by the author as far
back as 1871,* the methyl iodide vapours evolved being passed
through a red hot combustion tube containing lead chromate,
so as to burn the methyl iodide, the resulting carbon dioxide
being absorbed by potash bulbs in the usual way. Zeisel t has
modified the process by determining the iodine contained in the
methyl iodide produced instead of the carbon ; for this purpose
the vapours of methyl iodide evolved are carried off by a stream
of carbon dioxide and received in bulb tubes containing alcoholic
silver nitrate, intercepting vessels, &c., being employed to pre-
vent vapours of hydriodic acid or iodine from passing over also.
On standing, diluting with water, and adding nitric acid, silver
iodide is precipitated, the weight of which is a measure of the
amount of methyl iodide formed, and consequently of the pro-
portion of methoxyl-containing substances present.
Fig. 33 represents the arrangement employed by Benedikt
and Griissner ; a few decigrammes of substance are heated with
10 c.c. of hydriodic acid solution of sp. gr. 1'70 in the flask A,
warmed by means of a glycerol bath ; a current of carbon dioxide
is led through the flask, the issuing vapours passing through a
3-bulb condenser, bulb I. being empty to condense steam, &c. ;
bulb II. contains water to absorb hydriodic acid ; and III.,
red phosphorus and water to retain any traces of free iodine
* Proceedings of the Royal Society, xx., p. 8 (1871).
t Journ. Soc. Chem. Ind., 1886, p. 335; from Monatsh. f. Chemie, vi.,
p. 989. See also Journ. Soc. Chem. Jnd., 1889, pp. 735 and 923 (Benedikt
and Griissner).
ZEISEL S TEST.
193
evolved by decomposition of hydriodic acid by heat. After
passing through the bulbs the carbon dioxide, mixed with methyl
iodide vapour, is led into the flask B containing 5 c.c. of a 40 per
cent, solution of silver nitrate and 50 c.c. of 95 per cent, alcohol;
the safety flask D contains 1 c.c. of the same silver solution with
10 c.c. of alcohol, but is usually unnecessary, all methyl iodide
being retained in the first flask B.
Substances containing ethoxyl (O . C2H5) and homologues are
similarly affected ; as the molecular weight of the alkyl iodide
formed increases, slight differences in manipulation become
necessary, principally consisting in the employment of a higher
temperature to enable the alkyl iodide vapours to pass over \
for which reason the method is only applicable to the lower
members of the series and not to compound ethers of the higher
alcohols, such as cetylic alcohol.
Water
Water
Fig. 33.
The term " methyl number " is conveniently employed to
indicate the weight of methyl (OH3 =15) equivalent to the
silver iodide thus formed from 1000 parts by weight of sub-
stance: if a weight w milligrammes of substance give n milli-
13
194 OILS, FATS, WAXES, ETC.
grammes of silver iodide (equivalent to n x - - milligrammes
liOO
of CH3) the methyl number, M, is obviously given by the
equation —
AT n 15,000
M •== - x rt-_
w 235
= - x 63-83
M;
Thus, 296'3 milligrammes of oil of cloves gave 373-7 milli-
*>'""•> "
grammes of silver iodide, whence M = ]r '• x 63-83 = 80-5.
*2i\J\)'d
The theoretical methyl number for pure eugenof, C10Hr,O0, or
C.jH5 . C6H3 <^ Q pjT- is 91 '5 ; whence the sample examined con-
tained Q •- = 87'9 percent, of eugenol. Similarly, a sample of
y A "o
anise oil gave the methyl number 82'8 ; since pure anethol,
03H5 . 06H4 . 0 . CH3, corresponds with the methyl number 101-4,
82-8
the sample contained 77-7 = 81*6 per cent, of anethol.
The results of the various quantitative tests above described
may be conveniently tabulated as follows : — •
L— VALUES RECKONED PER 1,000 PARTS OF OIL,
FAT, OR WAX, &c., EXAMINED, OR DEDUCED
FROM FIGURES THUS CALCULATED.
Total acid number = Saponification number — Koettstorfer
number = Total acid potash permillage ( Verseifungszahl).
The weight of potash (KOH = 56-1) requisite to saponify
completely 1,000 parts by weight of substance, including that
neutralised by any free acids present.
Saponification Equivalent. — The number of milligrammes of
substance capable of furnishing on saponificatioii fatty acids
sufficient to neutralise 1 c.c. of normal alkaline solution (con-
taining or equivalent to 56'1 milligrammes of potash, KOH) ;
any free fatty acids present being also included. When the
total acid number is K, the sponification equivalent, E, is given
by the equation
50,100
Free acid number = Free acid potash permillage (Saiirezahl).
The weight of potash (KOH = 56-1) requisite to neutralise the
RESULTS OF QUANTITATIVE TESTS. 195
free acids present in 1,000 parts by weight of substance. If K
be the total acid number, and A the free acid number, then
j^ •
-^ x 100 represents the proportion of free acids present per 100
of total acids, assuming the mean equivalent to be the same in
each case.
Ester number = Compound ether potash permillage (jEtlierzahl ;
EsterzaliT). The difference between the total acid number and
the free acid number, or value of K - A ; expressing the weight
of potash (KOH = 56'1) requisite to neutralise the acids formed
by the saponification of the compound ethers, glycerides, &c.,
present in 1,000 parts of substance.
The yield of glycerol, theoretically obtainable from an oil or
fat consisting of triglycerides (with more or less free fatty
acids), is 0'05466 x S per cent., where S is the ester number
= K - A.
Insoluble acid number = insoluble acid potash permillage.
The weight of potash (KOH = 56*1) required to neutralise the
fatty acids, insoluble in boiling water, obtained from 1,000 parts
of substance.
This figure must not be confounded with the " Hehner
number " (Nekner'sche Zahl) expressing the percentage (not per-
millage) of insoluble acids yielded by the substance.
Soluble acid number = soluble acid potash permillage. The
weight of potash (KOH = 56 -1) required to neutralise the fatty
acids, soluble in boiling water, obtained from 1,000 parts of
substance.
Obviously the total acid number, K, = the sum of the insoluble
acid number and the soluble acid number. In practice, the
soluble acid number is usually best determined by subtracting
the insoluble acid number from the total acid number (p. 168) —
i.e., the soluble acid number is K — N, where N is the insoluble
acid number.
Volatile acid number — volatile acid potash permillage. The
weight of potash (KOH = 56'1) requisite to neutralise the vola-
tile fatty acids obtained from 1,000 parts of substance.
The Reichert number (Reiclierf sche Zahl} being the number of
c.c. of decinormal alkali required to neutralise the volatile acids
obtained from 2*5 grammes of substance by employing the
particular mode of operating described by Reichert (p. 173), if n
be the Reichert number, the corresponding " volatile acid potash
permillage" will be n x ^— - = n x 2-244. This value is neces-
lJ'0
sarily somewhat below the true " volatile acid number" obtain-
able by continuing the distillation until the whole of the
volatile acids have passed over.
If Meissl's modification .of the Reichert test be employed
(p. 174), 5 grammes of substance being taken instead of 2*5, if
196 OILS, FATS, WAXES, ETC.
m be the Reichert-Meissl number (Reichert-MeissVsche Zahl), the
corresponding volatile acid potash permillage will be m x 1-122 ;
as before this value will be below that corresponding with the
total amount of volatile acids present.
If K be the " total acid number," and V the " volatile acid
y
number," then • - x 100 represents the percentage of volatile
iv
acids (expressed in terms of some given acid) reckoned per 100
of total acids present free and combined as glycerides, &c.,
(similarly expressed) — i.e., the percentage of acids that are vola-
tile, reckoned on the sum of the volatile and nonvolatile acids,
and assuming these to have the same equivalent weight.
Methyl N^lmber. — The weight of methyl (CH3 =15) equivalent
to the silver iodide formed from the alkyl iodide vapours evolved
on heating 1,000 parts by weight of substance with hydriodic
acid.
II.— VALUES RECKONED PER 100 PARTS OF OIL,
FAT, OR WAX, &c., EXAMINED.
Iodine number = iodine percentage = Hiibl number (lodzald}.
The maximum weight of iodine capable of combining with 100
parts of substance ; or the weight of iodine equivalent to the
sum of the chlorine and iodine (or bromine and iodine) requisite
to saturate 100 parts of substance.
Hehner number = Ifehner'sche Zald. The weight of fatty acids
insoluble in boiling water yielded by 100 parts of substance.
III.— VALUES RECKONED PER 1,000 PARTS OF THE
FREE FATTY ACIDS FORMED ON SAPONIFI-
CATION, OR DEDUCED FROM FIGURES THUS
CALCULATED.
Fatty acid neutralisation number = potash permillage requisite
for neutralisation of mixed free fatty acids, reckoned per 1,000
parts of fatty acids ( Verseifungszahl der Fettsailren). The weight
of potash (KOH = 56'1) required to neutralise 1,000 parts of
the mixed fatty acids obtained by saponification of a, fat or oil,
&c., and separation of fatty acids from the resulting soap.
Mean Equivalent of the Fatty Acids. — The number of milli-
grammes of mixed fatty acids requisite to neutralise 1 c.c. of
normal alkaline solution (containing or equivalent to 56-1 milli-
grammes of potash, KOH). If N be the neutralisation number,
the mean equivalent F is given by the equation
_ 56,100
N '
RESULTS OF QUANTITATIVE TESTS. 197
In the case of an oil, &c., consisting wholly of triglycerides
(i.e., where the free acid number is so small as to be negligible),
the saponificatioii equivalent of the oil, E, and the mean equi-
valent of the fatty acids obtainable therefrom, F, are related
thus —
E = F + 12-67.
If, however, the oil contain free acids in measurable quantity the
relationship is
E = F + 1 x 12'67'
where S is the ester number and K the total acid number of
the oil.
The fatty acid neutralisation number, N, and the total acid
number of the original oil, K, are related thus —
»-•*
IV. VALUES RECKONED PER 100 PARTS OF FREE
FATTY ACIDS FORMED ON SAPONIFICATION.
Iodine Number of Free Fatty Acids (lodzahl der Fettsaureri).
— The maximum weight of iodine (or iodine equivalent to the
sum of chlorine and iodine or bromine and iodine) capable of
combining with 100 parts of free fatty acids.
If I be the iodine number of the original oil, &c., and I' that
of the fatty acids thence obtained, then
In the case of an oil, &c., consisting substantially of tri-
glycerides, so that E = F + 12-67, and where the mean equi-
valent of the free fatty acids lies between 250 and 330, the
F
value of „ lies between 1*0507 and 1-0384 — i.e.. the iodine
.b
number of the fatty acids exceeds that of the original oil by
close to 4*5 per cent, of the latter value.
V. VALUES RECKONED PER 1,000 PARTS OF
PRODUCT OF ACETYLATION OF FREE FATTY ACIDS.
Acetyl Number = Acetyl potash permillage (Acetylzahl}. — The
weight of potash (KOH = 56 -1) neutralised by the acetic acid
formed on saponification of 1,000 parts of the productof the
action of acetic anhydride on the
108 OILS, FATS, WAXES, ETC.
The acetyl number as thus defined includes both the titratioii
value obtained by Benedikt and Ulzer, conveniently referred to
as the titration acetyl number ; and the result of applying the
distillation process so as to separate acetic acid, as proposed by
Lewkowitsch, conveniently distinguished as the distillation acetyl
number. Like the volatile acid number, this latter value is
always apt to be more or less erroneous in defect on account of
the difficulty of distilling off and titrating every trace of acetic
acid.
On the other hand, in the case of free fatty acids very little
dependence can be placed on the former number, although for
alcoholiform substances this objection does not apply.
EARLIER FORMS OF PRESS. 199
4. Processes Used for Extracting, Rendering,
Refining, and Bleaching Oils, Fats, &c.
CHAPTER IX.
EXTRACTION OF OILS FROM SEEDS, &e., BY
PRESSURE OR SOLVENTS.
EARLIER FORMS OF PRESS.
THE use of olives and various kinds of seeds and nuts as sources
of oil has been known from at least the commencement of the
historic period, the earliest appliances for the expression of the
fluid consisting of " mills " somewhat after the fashion of the
primeval corn grinding hand mills, where a rounded stone was
made to revolve in a basin shaped stone vessel by means of
projecting handles, worked usually by two women seated on the
ground on opposite sides of the mill ; * the pulp thus produced
was then placed in sacking and pressed by means of planks
weighted with stones, very much as grape juice was expressed
in the earliest forms of wine press ; or a powerful lever was
applied, somewhat after the style of an enormous lemon squeezer.
Yarious forms of lever press have been in use at different times,
some of more complex order than the simple lemon squeezer type
of machine, a bent lever working a cam pressing upon the upper
board so as to force it downwards ; or the pressure board being
arranged vertically, and the sacking being compressed between
it and a stout vertical standard, such as the stump of a tree.
Double action presses of this kind, working alternately, have also
been constructed. A further improvement in oil pressing appli-
ances was the introduction of wedges between the pressure
boards, actuated by levers and cams or by percussion ; in the
latter case, the press consisted of a stout framework of beams,
inside of which the pressure boards and seed bags were arranged,
so that by hammering in wedges between adjacent pairs of
boards, or between the boards and the framework, the seed bags
were gradually compressed and finally subjected to considerable
* " There shall be two women grinding together ; the one shall be taken,
and the other shall be left." — Luke xvii. 35.
200 OILS, FATS, WAXES, ETC.
pressure. Even at the present day lever presses and wedge
presses of a more or less rude manufacture, but of considerable
practical efficiency, are still in use to a considerable extent
amongst those nations and in those districts to which improved
machinery and engineering appliances have not yet penetrated —
e.g.] in China and some parts of Japan* — whilst improved modifi-
cations of the older lever press, constructed with elbow levers
actuated by steam or water power, are employed with advantage
for various oil and grease expression purposes (p. 202).
Screw presses have also been extensively used, and are still
largely employed in the smaller factories ; but of late years
they have been mostly superseded by hydraulic presses in the
larger and more modern seed oil mills. In similar fashion
various forms of appliances have been successively introduced
and used for the crushing of oleiferous material, and otherwise
treating it previously to expression, so as to render the flow of
oil more easy and complete ; thus pairs of crushing rollers
working on parallel axes so as to squeeze the olives, seeds, &c.,
introduced between them, and " edge runners " (Fig. 48)
arranged like a mortarmill, are more recent developments which
have, for the most part, superseded the older form of " stamps "
where mechanically worked pestles pounded the seed, &c., to be
crushed in large basins or mortars.
Even at the present . day a considerable amount of oil of
various kinds is manufactured (on the small scale) by a process
probably of greater antiquity still than any mechanical expres-
sion method. In most tropical and subtropical countries oleifer-
ous seeds and nuts of various kinds abound ; in order to extract
the oil these are simply pounded or crushed and then boiled with
water, the oil rising to the top and being skimmed off. Experi-
ence has generally guided the natives to the use of a previous
roasting of the nuts or beans, the effect of the heat being to
coagulate and solidify mucilaginous and albuminous matter,
rendering the after separation of the oil by means of water
much more easy and complete. Castor oil, for example, is thus
largely extracted for local use in India ; palm oil and palmnut
oil, until comparatively recently, were almost wholly prepared
by this method, all the oil shipped from Africa having been
extracted by a water-boiling process applied to the pulp and
roasted kernels ; of late years, however, it has been more usual
to separate the kernels from the pulp and export them untreated,
the oil being subsequently extracted by the ordinary expression
or solvent processes.
In the rural olive producing districts a considerable amount
of oil is prepared by a sort of combination of the two methods,
* For a description of a peculiar form of wedge press used in Formosa for
the extraction of olive oil, see Report by Consul Warren on the trade of
Taiwan, Journal Soc. Chem. Industry, 1S91, p. 556.
HOT WATER PROCESSES. 201
the appliances being somewhat rude and primeval in the smaller
oil factories, but more modern in the larger ones. The crushed
pulp is washed by agitation with water, the oil as it separates
from the husks and rises to the top running off along with water
to separation tanks ; the residual wet oil-containing husks are
strained and boiled down to a kind of porridge or soft pulpy
dough, and the oil mixed with water then separated by pressure
in some sort of rough screwpress. In some cases the resulting
marc is ground up again by heavy edgerunners of granite, &c.
(worked by water or cattle power), boiled up afresh with water,
and subjected to further pressing.*
A somewhat analogous process is sometimes used in the
extraction of the fat or " butter " of the tallow tree (Stillingia,
sebifera), and other vegetable semisolid oils or fats ; the crushed
seeds, nuts, etc., are placed in wicker or bamboo baskets, weighted
with stones under boiling water, so that the melted fat gradually
separates and rises to the top ; the remaining oil is then-
extracted by pressure applied to the still hot material. This
method is more particularly suited to those nuts, ttc., where the
kernel is surrounded with a highly oleaginous pericarp, which is.
thus melted away by a process closely akin to that whereby
animal fats are " rendered " by means of steam or boiling water
(vide Chap, x.) Processes closely analogous in general character
are in use in various countries for the extraction of oil from fish
of various kinds (e.g., sardines), and from fish and shark livers,
whilst the mode of preparation of most kinds of wax is very
similar ; thus in the case of Chinese wax (Peh-Ia), the insect
producing the wax is a species of coccus (possibly several different
species), the young brood of which sticks to, and punctures the
bark and twigs of the trees (Fraxinus chinensis, Liyustrum
lucidum, &c.,) selected as domicile. A waxy material is secreted f
covering the bark, in which the insects ultimately imbed them-
selves, forming chrysalides. To obtain the wax, the branches
are scraped, some of the cocoons being reserved for breeding, the
rearing of the insects being a special industry like silk growing ;
the scrapings are heated with boiling water so as to melt off the
waxy matter, which is separated by skimming from the dirt, dead
insects, &c.
The different kinds of vegetable wax (myrtle wax, Japanese
wax, carnauba wax, <tc.), are mostly obtained by similarly treat-
ing with boiling water the berries, bark, £c., in or on which
the material is naturally secreted or deposited, and separating
the melted wax as it rises. Bees' combs, &c., are similarly
* Descriptions of the appliances in use in the Maritime Alps and in
Southern Sicily for the preparation of olive oil are given in the Journal
Soc. Arts., Nov. 20, 1891, and June 16, 1893.
t As with beeswax, opinions differ somewhat as to how far the wax is
precontained in the sap of the trees serving as food, and how far it is formed
or altered by animal life action.
202
OILS, FATS, WAXES, ETC.
treated to obtain beeswax, and separate it from adherent
honey and solid impurities.
Elbow Press. — Although the older rude forms of lever press
and wedge press are rapidly being superseded by more modern
devices, more especially by hydraulic pressure, they are still by
110 means extinct amongst those peoples where advancing
Fig. 31.— Elbow Press.
civilisation has not yet entirely improved away the ancient
methods and customs, whilst improved machines of these classes
are still in active use to some extent even in Europe and
America. Fig. 34 represents a form of " elbow press," largely
used in the United States for expressing hot melted tallow, &c.,
from animal adipose tissue. As the screw is worked (by hand
WEDGE PRESS.
203
wheel or band and pulley) the two powerful elbows are
straightened, and the ram depressed ; owing to the mechanical
nature of the action, the pressure is automatically increased
towards the end of the operation as the elbows straighten.
Wedge Press. — An improved form of wedge press is repre-
sented by Figs. 35 and 36 (from Schtidler) in front and side
elevation, Fig. 37 indicating the longitudinal section of the lower
portion. Inside each of a pair of troughs, J J, is placed an
arranges e:it of wooden wedges and planking, B L S K B,
Press — Front and Side Elevation.
together with two bags containing the crushed seed, ttc., to be
expressed, O O, each enclosed between cast iron frames, T P. The
" loose -wedges," L L, are suspended by ropes, and serve to lock
the whole arrangement together, the loosening when the pressure
is completed being effected by casting off the ropes and allowing
the suspended vertical beams, C C, to descend, pile-driver fashion,
so as to drive these wedges, L L, down ; A A, B B represent a
stout timber frame supporting the driving beams. The pressure
is obtained by similarly forcing downwards the "press-wedges,"
204
OILS, FATS, WAXES, ETC.
K K, by the beam drivers, D D. These drivers are raised by
means of stout teeth, G, projecting from a horizontal axle work-
ing on studs, E and F, attached to the beams respectively, a
system of ropes, b, c, bent lever, a, and studs, d, d, being attached,
so that when the ropes are pulled, either of the drivers can at
will be raised so as to bring it out of the reach of the teeth, and
keep it suspended out of action. The oil bag, being placed in
position between the plates, T P, of the iron frames, L, is adjusted
at a convenient height by means of the attached rope. The
drivers, D, being then set in action, the press wedge, K, is
forced down, and the oil bag consequently strongly compressed.
When the oil ceases to run and the wedge is driven home, D is
thrown out of action and C allowed to hammer on the loose
wedge (the rope attached being slackened) ; the loose wedge, L,
soon falls, and the bags with exhausted oilcake are then removed
and fresh ones substituted.
Fig. 37. — Wedge Press— Longitudinal Section of Lower Portion.
In some of the Marseilles oil factories an arrangement is in
use known as the " Estrayer Cylinder,"* the action of which is
somewhat akin to that of the wedge press. The apparatus con-
sists of two cylinders, one inside the other, of which the outer
acts upon the inner by means of a series of inclined planes, the
inner cylinder being composed of eight segments which either
close up tightly or separate slightly according as pressure is
exercised or removed by the position of the outer cylinder.
Screens made of esparto grass and horsehair are employed
instead of oilbags of the same material ("scourtins ") such as
are employed in other forms of press ; these are subject to much
less wear and tear than the scourtins, whereby an economy of
80 to 90 per cent, in the cost of the scourtins is effected. An
*Jonm. Soc. Chcm. Ind., 1893, p. 49.
SCREW PRESS.
205
interior movement allows of the cylinder being enlarged in
diameter, so that the cakes can be readily removed. The appa-
ratus will withstand a pressure of 500 kilos per square centimetre
(63^ cwts. per square inch) ; half of this is as much as can be
safely applied to the ordinary bags without great risk of bursting
them. A cylinder holding 80 to 100 kilos of seeds can be dis-
charged and refilled in 7 to 8 minutes, the pressing occupying
30 to 35 minutes.
Fig. 38.
Screw Press. — In districts where more modern machinery
has not been extensively adopted (e.g. many parts of Spain,
China, West Indies, South America, Africa, &c.), rude screw
presses are still largely in use in the comparatively small oil
mills where oil is expressed in much the same fashion as has
been practised for centuries ; these mostly work on the principle
206
OILS, FATS, WAXES, ETC.
of an ordinary copying press, the sacking (or wicker or straw
basketing, &c.) containing the material to be expressed being
placed between the two plates of the press, and the screw (fre-
quently of wood) turned by means of a long lever so as to bring
the plates nearer together and express the oil, much as a wet
sponge would be squeezed in
handle.
copying press by turning the
Fig. 39.
Fig. 38 represents an English improved form of screw press
for expressing oil, tfec., from fish or similar materials where only
a moderate pressure is required. Motion is communicated by
HYDRAULIC PRESS. 207
belts from shafting to a horizontal axle carrying a worm which
gears into a toothed wheel, the revolution of which raises or
depresses the screw passing concentrically through the wheel,
and consequently elevates or lowers the plunger. According as
a straight belt is used connected with one pair of fast and loose
pulleys on the axle, or a crossed belt connected with the other
pair, the plunger moves in one direction or the other. The
material to be pressed is placed in bags between loose metal
plates, the press itself being enclosed in a wrought iron steam
casing (stayed to resist pressure) provided with a steam-heated
door of similar construction, so that when requisite the temper-
ature inside the press can be elevated up to that of the steam or
nearly so.
Fig. 39 represents a screw press of German make. The mate-
rial to be expressed is placed inside the perforated cylinder B,
Avhich is then placed inside the cylinder, C, and mounted 011 the
platform, A ; the ram, D, attached to the screw, F F, being raised
to a convenient height. On turning the horizontal wheel, G, the
screw and ram descend and the material is strongly compressed
in the inner cylinder. The expressed liquid passes through the
perforations in the walls of B and runs out through others at the
base of C into a circular groove in the platform, A, and thence
by the spout to a vessel placed to receive it. A small hydraulic
arrangement is attached at the base, such that by turning the
handle, E, a piston is screwed slowly inwards, thus raising a
hydraulic ram on to the top of which the platform, A, is fixed,
and so obtaining at the end of the operation a more powerful
pressure than would be possible by means of the screw, F F, alone.
Hydraulic Press. — The ordinary form of hydraulic press as-
adapted for oil expression consists of a ram raised by admission
of water into its cylinder, either intermittently by pumps (worked
by hand or power) or continuously from an accumulator. The
former method is preferred for many purposes, since the pulsating
pressure obtained by means of a pump appears to be better
adapted for the expression of oil from most kinds of seeds, &c.,
than the continuous steady pressure of an accumulator. Presses
in which the ram works horizontally instead of vertically are
sometimes preferred. Fig. 40 represents a German form of
hydraulic press, empty before charging, and Fig. 41 the same
after the ram has risen. The bags are placed in the cavities of
the shelves or press boxes, E E E, and the ram started working.
As it rises each bag is strongly compressed between the base of
the press box containing it and the projecting lower portion of
the box next above it ; the oil runs out into the circular grooves,
F F, and thence to delivery spouts, J J, and so through the pipes,,
G G, to the vertical oil shoot, H, leading to the oil well or tank^
The headpiece of the press, C, is supported by stout pillars, D D,,
to resist the strain.
208 OILS, FATS, WAXES, ETC.
Fig. 40. —Hydraulic Press (German Form).
HYDRAULIC PRESS.
209
Fig. 41,
210
OILS, FATS, WAXES, ETC.
Fig. 42 represents an English handworked hydraulic press,
specially suitable for light work such as that in a small olive oil
mill. The press being filled, the larger of two differently sized
pumps attached to it is worked by means of the detachable lever
handle, until the bulk of the oil is expressed ; to obtain a
stronger pressure for the extraction of the remainder, the lever
Fig. 42.
handle is then applied to a second smaller pump arranged by
the side of the first one, whereby a considerable increment in
power is obtained.
Fig. 43 represents a press arranged for working on the "Anglo-
American System " (vide infra). The plates are corrugated, and
arranged at such distances apart as just to allow of the moulded
cakes of hot ground seed, &c., from the kettle and moulding
HYDRAULIC PRESS.
211
machine (p. 221) being introduced, preferably from each opposite
side alternately. Usually sixteen cakes are pressed simultaneously
in one press, whilst four such presses are worked together in one
block, all four being erected inside the same wrought iron oil
tank, which serves as a foundation and collects the expressed
oil in a most efficient man-
ner. The pressure employed
usually rises from 700 or 800
Ibs. per square inch at first
up to 2 tons at the end.
Fig. 44 represents the plan
and longitudinal section of
one of the press plates, Fig.
45 indicating the cross-sec-
tion.
The dimensions of the oil-
cakes produced vary con-
siderably with the size of
the oil mill, the system of
working, and the nature of
the seed, £c., used ; the
cakes are always made to
taper somewhat so as to
facilitate withdrawal from
the cake boxes. Thus with
the smallest mills the cakes
may weigh about 3 Ibs., and
the dimensions may be 14
inches long, and 6i- inches
wide at one end and 5| at
the other, the press being
constructed to take from 4
to 6 such cakes at a time ;
whilst with somewhat larger
mills the cakes may weigh
about 4 Ibs., being 20 inches
long, and 1\ wide at one end
by 5J at the other. Still
larger cakes (up to some 30 inches long, and 10 or 11 wide at one
end and 7 or 8 at the other) are made in mills of greater magnitude
(especially when working linseed), where the scale of manufacture
is large enough to enable full-sized presses, <fec., to be employed.
Such a linseed cake generally weighs from 6 to 13 Ibs., averaging
about 8 or 9 Ibs., varying with the source and richness in oil of
the seed used ; the weight of the pressed oilcake obtained from
a given quantity of seed is obviously the less the larger the yield
of oil. When working on the older system the press usually
contains only four cake boxes, three such
j
UNIVERSITY
212
OILS, FATS, WAXES, ETC.
by one man and a boy, including paring and storing the cakes ;
the presses are charged from three to six times an hour, accord-
ing to the seed used (cotton seed about four times, linseed five).
With some kinds of seed (e.g., rape and gingelly) the crushed
seed is worked over twice, two presses being employed for the
first^ expression and three for the second — the press cake pro-
n
Fig. 44.
duced by the first treatment being reground before the second
expression, usually by means of edge runners (p. 219). Seeds
less rich in oil than linseed and cotton seed yield proportionately
heavier cakes for the same weight of seed ; as a rule, with the
less oleaginous seeds, &c., a better yield is obtained by pressing
proportionately smaller quantities at a time, so as to form in all
cases oilcakes of about the same thickness.
Fig. 45.
With certain kinds of seeds furnishing " salad " oils of finest
character, the expression is carried out in three stages : — First
of all cold pressure is applied to a moderate extent, whereby a
" cold-drawn " oil is obtained of the purest quality (after refining,
i.e., removal of mucilage, &c.). Then the cake is again ground,
slightly moistened with water, and pressed a second time, using
somewhat higher pressure ; the oil thus obtained is cold-drawn
oil of second quality. Finally, the cakes are again ground and
OILCAKE. 213
heated and pressed hot ; the oil thus obtained is far inferior to
either of the former runnings. The oilcake thus left often
retains a sufficient quantity of oil to render it worth while to
treat by some solvent extraction process (p. 231), whereby a still
lower grade of oil is ultimately obtained. This mode of treat-
ment in several stages is more especially adopted in the case of
higher class edible oils — such as those from the arachis nut, and
from sunflower seed ; or in the production of the more highly
priced oils used for other purposes— e.g., almond oil. Coarse oils,
such as linseed, are usually expressed but once, the pulp being
heated to commence with as described below, partly to render
the oil more fluid, and partly to coagulate albuminous matter.
Some kinds of seeds, however (e.g., sesame and rape), are gener-
ally treated in two stages — i.e., pressed twice successively so as to
obtain two qualities of oil. When the cakes are removed from
the press, the cloths are stripped off and the edges pared off;
the parings contain a notable amount of oil, and are therefore
ground up and mixed with fresh crushed seed for another
batch.
In some cases mixtures of seeds are intentionally prepared arid
crushed and treated together ; in others the seed as harvested is
a mixture, two or more kinds of plants being grown together ; so
that, excepting when the seeds differ sufficiently in size to be capable
of separation by sifting, the oil ultimately obtained is necessarily
of a mixed character. Partly from causes of this kind, and partly
on account of subsequent adulteration, it is difficult, if not impos-
sible, to obtain an absolutely pure oil of any given kind in
commerce, the only practicable method of procuring a perfectly
pure sample being to hand-pick the seeds and express the oil
in a small press kept for such purposes. Accordingly, a small
press for the purpose of preparing samples of genuine seed oils
from time to time is an indispensable part of the equipment of
a laboratory where oil examinations are made by comparison of
the substances tested with specimens of oils and mixtures of oils
known to be themselves unadulterated.
Composition of Oilcake. — The analyses quoted on p. 214
are given by Schadler.as representing the average composition of
oilcakes of various kinds.
According to Yoelcker, linseed cake made by the older system
usually contains from below 10 to about 16 per cent, of oil, and
cotton seed cake from 6 per cent, (undecorticated) up to 16 per
cent, (decorticated). Oilcakes made by the Anglo-American
system of working are usually more completely expressed, so as
to contain distinctly smaller percentages of residual oily matter
than cakes prepared without the aid of a moulding machine. If,
however, the expression be carried too far, the value of the cake
as cattle fodder is greatly diminished, so that in extreme cases it
may be rendered unsaleable.
214
OILS, FATS, WAXES, ETC.
Oilcake from
Water.
Cellulose
Fatfcv anc* ^on~
ivf tt r- nitrogenous
Matter. Vegltable
! Matter.
Ash.
Proteids.
Nitrogen.
Arachis nuts, .
11-50
8-80 ! 31-10
7-25
41-35
6-80
Cotton seed,
13-00
7'50/ 51-00
8-50
20-00 *
2-90
Rape seed, . .
10-12
9-23 41-93
6-84
31-88
5-00
Colza, . . .
11-35
9-00 42-82
6-28
30-55
4-50
Sesame seed, .
10-35
10-10
38-80
9-80
31-93
5-00
Beechnuts, . .
11-40
8-50
49-80
5-30
24-00
3-20
Linseed, . . .
10-5(5
9-83
44-01
6-50
28-50
4-25
Cress seed, . .
12-23
7-68
47-00
12-50
20-50
3-00
Camelina seed,
9-60
9-20
50-90
7-00
23-30
3-60
Poppy seed,
Sunflower seed,
9-50
10-20
890
8-50
37-67
48-90
11-43
11-40
32-50 5-00
21*00 2-40
Madia, . .
11-86
7-90
50-00 I 12-24
18-00
2-50
Hemp seed,
10-00
8-20
48-00 12-24
21-50
3-30
Palm kernels, .
9-50
8-43
40-95
10-62
30-40
4-50
Cokernuts, .
1000
9-20/
40-50 .
10-50
30-00 •*
4-50
Nordlinger has found (p. 115) from 6 to 15 per cent, of total
fatty matters contained in rape, poppy, earthnut, sesame, palmnut,
cokernut, linseed, and castor bean cakes ; of which the free acids
constituted fractions varying between less than Ti^ and above -£.
According to B. Dyer,* linseed cake, as made at the present
day, contains, on an average, about 10 per cent, of oil, varying
between 7 and 16 per cent.; of this a quantity varying between
one-thirteenth and one-fifth, usually consists of free fatty acid,
the proportion being less the purer the linseed. With some
freshly expressed cakes, free acid is practically absent ; on the
other hand, with cakes that have "heated" on keeping, the
greater portion of the glycerides originally present is decom-
posed, producing free fatty acids. Obviously, the proportion of
free acid formed chiefly depends on the extent to which hydrolytic
actions have taken place during storage.
OIL MILL PLANT.
The plant in use in modern oil mills varies somewhat in
details according to the nature of the material to be treated, and
according as the substance is intended first to be submitted to a
preliminary cold pressing so as to obtain a portion of the oil as a
product of finer quality, and then to hot pressings to obtain lower
grades; or to be treated hot at one operation only. Further,
the climate somewhat modifies the character of the process,
inasmuch as many substances can be sufficiently completely
^expressed in a tropical climate, without any extraneous heat
* Journ. Sec. Ckem. Ind., 1893, p. 8.
OIL MILL PLANT. 215
being requisite, that would require to be artificially warmed in a
colder climate to render the oil sufficiently fluid to exude properly
by pressure. Again, the scale on which the operations are to be
conducted, and considerations as to relative cost of labour, fuel,
animal power (horses or bullocks, &c.), value of oilcake when
expressed as far as practicable, or only to a lesser extent, and
whether to be subsequently treated by solvent processes or not,
and so forth, have also to be taken into account. In general
terms, however, the plant may be described as essentially con-
sisting of boilers and engines for steam raising for heating pur-
poses and power ; crushing machinery (rolls, edge runners, &c.)
for breaking up the material so as to rupture the walls of the
cellular tissues in which the oily matter is contained ; heating
appliances whereby the material (either as delivered from the
crushers, or after a preliminary cold pressure, and subsequent
disintegration of the partly expressed cake) is subjected to heat
for the twofold purpose of rendering the oil more fluid, so as to
facilitate expression, and of partially coagulating albuminous
matter so as to obtain a purer product ; hydraulic presses
whereby the expression is effected; and finally, filter presses,
refining tanks, settlers, and analogous appliances, whereby the
crude oil is refined and more or less completely separated from
watery and organic matters accompanying it when first ex-
pressed. What is now generally known as the " Anglo-American
system '"' substantially consists in the use of a selection of par-
ticular appliances for the above purposes conjoined with a special
feature — viz., that the crushed material, after damping and
heating in a suitable "kettle," is subjected to a preliminary
moulding operation so as to shape and compress it into compact
thin blocks or " cakes," which are then expressed.
The chief advantages of this system, as employed in the plant
constructed by Messrs. Rose, Downs & Thompson, of Hull, are
claimed to be as follows, when contrasted with older systems of
arranging and working oil mill plant : — •
All the machinery is belt-driven ; whereby not only is greater
economy secured in the cost of gearing and greater facility in
erection, but also a considerable saving (about 20 per cent.) in
driving power.
The weight of the machinery requisite to work a given
quantity of seed is materially reduced, whilst the process is
equally applicable to all oil seeds and nuts, slight variations in
the nature of the rolls, &c., being made in some cases, according
to the nature of the seed, &c., treated.
The plant is less bulky, a great economy in space being
effected ; whilst a large saving (50 per cent. ) of labour in the
press room is also brought about.
The oil is more perfectly extracted; thus linseed cakes made
on the old system usually contain about 10|- per cent, of oil, and
Fig. 46
OIL MILL PLANT. 217
those made by the modern process only about 7 per cent., giving
an extra yield of oil to the extent of about 3J per cent, of the
weight of the cake.
The bagging requisite for moulded cakes is subjected to less
severe wear and tear than that used in the ordinary process ;
whilst the costly hair envelopes are altogether abolished. More-
over, the cakes produced have a better surface and fracture, and
are better branded when the crushing is effected by rollers than
when done by means of edge stones in the ordinary way.
In what is termed a " unit " mill on this system, the plant is
capable of crushing from 160 to 200 cwts. of linseed or rape
seed per day, or 155 to 190 cwts. of cotton seed. The seed
passes down a shoot to a series of crushing rolls (usually five in
number), thence by an elevator to the kettle, where it is heated;
a moulding machine forms it into cakes, which are placed in
presses (four standing in one oil tank) and expressed. A paring
machine cuts off the oil-containing edges of the pressed oilcakes ;
these are ground up under small edgestones and returned to
the kettle to be worked over again with a fresh batch of
crushed seed. One set of four presses requires three men in the
pressroom and about 45 actual horse power to work it. For
larger mills, this "unit" set of plant is simply doubled, trebled,
or quadrupled, and so on, each additional set requiring a further
addition of about 35 actual horse power. In. very large
installations, where more than two sets (eight presses) are used,
a system of accumulators is preferable rather than separate
pumps for each set of four presses ; accumulators at a lower
pressure being also used for the moulding machines, cake hoists,
ike., whereby a considerable saving is effected in gearing and
space. Fig. 46 exhibits the ground plan of a 16-press installation
containing the following plant : —
1 High pressure accumulator.
2 Low ,,
16 Hydraulic presses, each with a hydraulic gauge.
1 Set of hydraulic pumps.
4 Sets of accumulator stops.
4 ,, seedrolls (5 rolls in each).
4 Seed kettles.
4 Moulding machines.
2 Paring ,,
4 Sets of elevators.
2 Sets of edgestones.
2 Oil pumps and cisterns.
4 Seed screens.
Oil cisterns to hold 200 tons of oil.
Engine to work up to 200 actual horse power.
Boilers ,, 250
together with gearing, elevators, sack lift, pipirg, &c.
Such an installation requires twelve men in the press room,
which should measure 66 ft. by 44 ft., the whole building being
218
OILS, FATS, WAXES, ETC.
275 ft. by 44 ft., four floors. From 640 to 800 cwts. of linseed or
rape seed, or from 620 to 760 cwts. of cotton seed can then be
treated per day of 1 1 hours.
Crushing Rolls and Edge Runners.— Fig. 47 represents a
set of four superposed rolls used as above described ; these are
42 inches long and 16 inches diameter, and are so arranged that
the seed is delivered from the hopper above (by means of a fluted
feed roller the same length as the crushing rolls, and a slanting
.shoot), between the two uppermost rolls ; having passed between
Fig. 47.
these, another curved shoot or guide plate on the other side
delivers it between the second and third rolls, which crush it
further; in similar fashion it passes by another guide plate
between the third and fourth rolls, where it receives the final
grinding. The seed is thus crushed three successive times in its
passage through the rolls, which are brought into contact by a
combination of a screw and india-rubber springs, thus giving a
smooth and easily regulated pressure; a much more complete
EDGE RUNNERS.
219
and perfect grinding is thus effected than is possible with single
pairs of rolls and edgestones of the older construction. When
five rolls are employed in the same train, the arrangement is
precisely similar, four successive crushings being effected. For
small installations the rolls used are similar in character, but of
proportionately smaller size ; thus a set of four rolls (crushing
the seeds thrice successively), each 15 inches long and 12 inches
diameter, suffices for a steam driven mill of about half the
capacity of a " unit ;' and one of three rolls (giving two suc-
cessive crushings), each 8 inches long and 8 inches diameter,
for smaller sizes still, driven by bullock power.
In some oil-crushing establishments heavy edge runners are
preferred to rolls for certain kinds of material — e.g., Egyptian
cotton seed and coprah. Fig. 48 indicates a belt-driven pair of
stones, 8 feet diameter and 20 inches thick (the face being
220
OILS, FATS, WAXES, ETC.
chamfered to 16 inches); with these, about 6 tons of Egyptian
cotton seed may be crushed in eleven hours. The best stones
are made of well dressed Derbyshire gritstone, free from all
sandholes, cracks, shells, and other imperfections, the bedstone
(6 feet 6 inches diameter and 22 inches thick) being of the
same material.
Smaller sized stones suffice for grinding cake parings ; for the
4-press "unit" installation above described one set of stones
suffices, 4 feet diameter and 12 inches thick (face 9 inches). For
this purpose, two carfe plates are used instead of one, as shown
Fig. 49.
in Pig. 48, the upper one being perforated, so that the material
that is being ground' may pass through 011 to the lower one as
soon as it is sufficiently pulverised ; from the lower plate it is
gathered together and discharged through a shuttle at any
convenient point. The texture of the material thus ground is
regulated by the fineness or coarseness of the perforations. In
KETTLE AND MOULDING MACHINE.
221
some mills working coprah, slicing or rasping machines are em-
ployed to cut up the material before grinding ; but so much
damage is done to the knives by stones mixed with the coprah
that this previous treatment is now but seldom employed, special
disintegrators being used instead (p. 225).
Kettle. — The " kettle " used in the Anglo-American system
•consists of a steam-jacketted circular castiron vessel, furnished
with an agitator (Fig. 49) driven by a belt; a steam damping
apparatus with perforated boss is fixed inside, so that the crushed
seed delivered into the kettle by an elevator is moistened by the
condensation of steam from the damping arrangement, and
heated up uniformly as the mass is stirred by the agitator. By
means of a slide at the bottom the heated substance is delivered
into a box supplying the moulding machine. The kettle body is
fitted with a wooden frame, and covered over with felt or slag
wool enclosed within iron sheeting to keep in the heat. In order
to save space, the crushing rolls are sometimes arranged vertically
above the kettle ; but in addition to the inconvenience caused by
this elevation as regards inspection and adjustment, the steam
from the kettle is apt to condense on the rolls and clog them ; so
that this disposition is generally abandoned in the newer mills,
the crushed seed being delivered into the kettles by means of
elevators (Fig. 55) or screws, and not by gravity.
In the older system of working where moulding machines
are not employed, the kettles used for heating the crushed seed,
<kc., are of similar character, but are usually not supplied with a
damping arrangement, as the necessity for moistening the
material in order to mould it better does not then arise.
Moulding Machine. — The use of this appliance is the most
distinctive feature of the Anglo-American system ; the differences
between this and the older
method of procedure may be
thus stated. In the old system
from 11 to 16 Ibs. of seed are
placed by a boy in a woollen bag ;
the press man takes up the bag,
doubles it back so as to close the
mouth, and then places it on the
lower half of a " hair " or other
envelope (Figs. 50 and 5.1 *)
Fig. 51.
Fig. £0.
* Envelopes of vulcanised fibre, paper, and other materials are frequently
employed instead of the more expensive "hairs."
999
OILS, FATS, WAXES, ETC.
that he has previously placed on a table in front of the press.
He then smooths the bag with his hand until the seed is distri-
buted throughout the interior as equally as possible. The envelope
is then closed over the bag, and the whole taken up and placed
in the press. This process is continued until the press is filled,
each cake, together with its box, occupying a vertical thickness
of upwards of 10 inches. When the moulding machine is used,
Fig. 52.
each cake with its plate only occupies 3 inches, thereby greatly
increasing the capacity of the press ; whilst the cost of labour is
considerably lessened. The moulding is thus effected ; the work-
man begins by raising a measuring frame and placing underneath
it a sliding frame holding a tray with a piece of woollen cloth
about double the length of the tray placed thereon centre to
centre, the ends of the cloth hanging down ; the measuring frame
PARING MACHINE. 223
is now brought down on the top of the tray and cloth, and
crushed seed introduced from a box (fed automatically from the
kettle as required) until the frame is full. The frame is then
thrown back, the loose ends of the cloth folded over the seed,
and the sliding frame carrying the tray, seed, and cloth pushed
forward over the pressing plate. This motion of the frame sets
the machine at work, the pressing plate ascending and squeezing
the seed into a compact mass about li inch thick, after remain-
ing in contact with it about a quarter of a minute. The pressing
plate then falls, and the machine stops, enabling the press man
to remove the compressed cake to the press, carrying it 011 the
tray which is withdrawn as soon as the cake is in position.
During the time that the cake is being compressed, the moulder
is engaged in forming another one on a tray in front of the
machine as before ; so that cakes to the number of 240 may be
thus moulded in an hour.
Fig. 49 represents a moulding machine actuated by steam in
position with respect to the kettle ; other forms are sometimes
used worked by hydraulic power.
Paring Machine. — The cakes obtained in the hydraulic press
are usually oily at the edges where the oil exuded, so that the
edges require to be cut off, not only to trim the cakes, but also
to save the oil with which they are impregnated, the parings
being ground up and returned to the kettle. In mills working
on the older systems the press cakes are generally trimmed by
hand ; but the simple form of machine indicated in Fig. 52 not
only enables the parers to do much more work in a given time,,
but also to cut the edges far more regularly and neatly. The
cake to be pared is placed with one edge over a central longi-
tudinal trough ; a cutter block with attached knife passes along^
and shears off the portion of the cake projecting beyond a given
line, being driven by the excentric working a bar jointed to the
upper part of the frame. The other side and ends of the cake
are trimmed in the same way, two knives being attached to the
cutter block, one cutting when the motion is in one direction,,
the other when in the opposite direction. A screw works in the
trough, so that as the parings fall they are carried onward by the-
screw and delivered on to the upper carfe plate of a pair of edge-
stones (Fig. 48), whereby they are reduced to meal, which is then
taken up and distributed to the kettles by elevators and screws.
Supplementary Appliances. — In. addition to the preceding-
principal appliances, various other minor arrangements are re-
quisite in a well appointed oil mill. Thus, screens of various
sizes of mesh are necessary in order to sift out stones, &c., and
to partially separate different kinds of admixed seeds when their
respective dimensions renders this practicable. Machines for
decorticating seeds are also employed. Fig. 53 represents cotton
seed treated by such a machine. A, ordinary Egyptian seed
224
OILS, PATS, WAXES, ETC.
coated with "cotton filaments ; the machine cuts through the
husk and kernel, B ; a separator then divides the husks, C, from
Fig. 53.
the oily kernels, D, the latter being crushed and expressed, and
the former used for manure, Arc. Similarly, castor beans are
contained in an outer shell (Fig. 54, A) ; a special castor seed
decorticating machine removes the outer shell, B, leaving the
white kernel, C, ready for the press. Analogous machines are
employed for decorticating arachis nuts and for splitting coker-
nuts, cutting through husk, shell, and kernel at one opera-
tion ; and for grinding and disintegrating coprah. Pulverising
machines for this purpose, where the action is brought about by
a series of blows from rapidly moving flat beaters, answer better
than those where the grinding is effected between parallel iron
CHEMICAL DECORTICATION.
225
discs by friction. Fig. 55 illustrates the arrangement used when
such a disintegrator is mounted directly over the kettle, and fed
by an elevator.
Dudley <fe Perry have patented a process* for chemically
decorticating cotton seed. The seeds, after linting, are subjected
to the action of gases containing nitrous anhydride and sulphur
dioxide, with enough air to " regenerate " the higher oxides of
nitrogen as fast as they are reduced. After a few seconds
Fig. 55.
exposure the fibre has changed but little in appearance, but its
structure is completely destroyed, so that the slightest friction
causes it to fall to an impalpable powder, leaving the seeds
perfectly smooth, and showing no signs of corrosion. A slight
acid reaction is perceptible on the outside, easily removable by
washing ; but no acid penetrates into the interior.
*U. S. Patent 344, 951.
15
226
OILS, FATS, WAXES, ETC.
The crude expressed oil carries with it more or less watery
matter, together with mucilaginous and albuminous organic sub-
Fig. 56.
.
Fig. 57.
Fig. 58.
FILTER PRESS.
227
228 OILS, FATS, WAXES, ETC.
stances, requiring processes to be adopted for their removal.
Formerly these generally involved long continued standing, so as
to enable the solid impurities to form and settle, the process being
in some cases hastened by heating to coagulate albuminous matter,
or by the use of chemicals (vide Chap, xi.) In many cases, how-
ever, it is found that a degree of clarification sufficient to render
the oils immediately saleable, can be rapidly effected by simply
pumping the oil (either just as it runs from the press into the oil
well, or after heating to a temperature somewhat short of 100° C.
to coagulate mucilage, &c.) through a filter press ; the matters
thus filtered out from the oil are generally returned to the kettle-
Fig. 60.
and worked over again with a fresh batch of crushed seed, so
that the only products finally obtained are filtered oil and
pressed cake, no "foots" of any kind being made. In the case
of many kinds of oil this simple treatment suffices to refine the
oil sufficiently for most purposes ; in other cases, although subse-
quent refining methods are still requisite, yet on account of the
previous removal by filtration of a large proportion of the
impurities, the rest of the refining process is much facilitated
and shortened. Accordingly, in the newest installations suit-
able filter presses form an important part of the subsidiary
appliances employed.
Fig. 56 represents a hydraulic filter press with self-contained
SEPARATION OF STEARINES. 229
engine and pump, made by Messrs. S. IT. Johnson £ Co., of
Stratford ; the plates are " recessed," so that the raised rims of
the consecutive plates enclose a space when they come together,
which finally becomes filled with the solid matters taken from
the material filtered. Figs. 57 and 58 represent the front eleva-
tion and sectional elevation of the plates, which are provided
with adjustable tension hooks to carry the cloths, and stay boss
projections so as to prevent fracture of the plates when work-
ing under high pressure, each plate supporting the next adjoin-
ing one from end to end of the machine. Figs. 59 and 60
Fig. 61.
represent a different type of plate surface (" Pyramid drainage "
surface), whereby washing of the cakes produced is more readily
effected, and the efficiency of the press largely increased in the
case of viscid liquids. Fig. 61 represents a miniature pattern
of hand-worked press for small operations and experimental
purposes.
SEPARATION OF SOLID STEARINES FROM OILS, &c.
Many oils when allowed to stand for some time at a sufficiently
low temperature deposit more or less copious amounts of solid
matter, sometimes becoming semisolid or buttery in so doing.
If the temperature be raised the whole mass melts again to a
fluid oil ; but by " bagging " (or straining off the liquid portion
through canvas bags forming rough filter-strainers) without apply-
ing heat, the solid matter may be collected ; and by applying
pressure to the " bagged " mass the remaining liquid may be
squeezed out. When the solid matter thus collected is sufficiently
granular, the ordinary method of cold pressing may be conve-
niently applied, the process being carried out in much the same
230 OILS, FATS, WAXES, ETC.
way as that above described in the case of crushed seed pulp,
excepting that the pressure is applied more gradually and gently ;
but in many cases the solid particles are so fine that they are
largely forced through the interstices of the press cloth (even
when specially made cloths are employed) and thus lost in the
liquid runnings. In cases where the solid matter is present in
too small quantity for ordinary cold pressing filter presses may
often be conveniently employed to collect and consolidate the
solidified constituents. Thus olive oil when cooled for some time
deposits a considerable fraction of the more solid glycerides con-
tained (palmitin, stearin, arachin) ; these when collected by the
filter press furnish an "olive stearine," whilst the filtered oil is
proportionately less liable to thicken and deposit in cold weather.
Similarly cotton seed oil furnishes a considerable amount of
" cotton stearine " and a more fluid liquid oil, known in conse-
quence as winter oil. Animal oils, such as cod liver oil and whale
oil, furnish analogous stearines ; from sperm oil, spermaceti is
similarly separated.
In the manufacture of paraffin wax for candle making, &c.,
certain fractions of the distillates obtained consist of mixtures of
hydrocarbons of different melting points, some fusing at con-
siderably above the ordinary temperature. On chilling such
" oils," by means of a suitable frigorific machine, the hydro-
carbons of higher fusing point mostly separate in the solid
form ; so that by straining the magma, or subjecting it to filter
pressure, the solid paraffins are separated from those yet liquid.
The solid matters thus obtained (paraffin scale), when refined,
redistilled, and subjected to further pressings at regulated tem-
peratures, ultimately furnish " paraffin wax " of melting point
the more elevated the higher the temperature at which the last
warm pressing has been effected, this temperature being regu-
lated by the nature of the material dealt with, some kinds of
distillates furnishing paraffin wax of higher melting point than
can be isolated from others.
Similar operations are gone through in various other manufac-
tures connected with the coaltar and mineral oil industry ; thus
the separation of carbolic acid from mixtures of that substance
and its homologues and other bodies accompanying it, is effected
by chilling by means of an ether or ammonia freezing machine,
and draining off the unfrozen liquid from the mass of crystals
that gradually forms. Similarly " anthracene oils," obtained at
a certain stage of coaltar distillation, become more or less pasty
and semisolid on cooling and standing ; so that by straining
off the liquid portions (by filter pressing or otherwise) and sub-
sequently expressing the remaining liquid by more powerful
pressure, a solid residue is ultimately obtained, consisting of
anthracene intermixed with other solid hydrocarbons, &c.
In the manufacture of "stearine" for candles (stearic and
EXTRACTION OF OIL BY SOLVENTS. 231
palmitic acids, &c., p. 110), similar operations are gone through
for the purpose of isolating mechanically the solid fatty acids
that have crystallised into a honeycombed mass, the interstices
of which are filled with the liquid acids (" red oils."). Hydraulic
pressure of the spongy solid mass in sacking serves to effect a
first separation of matters respectively solid and liquid at the
ordinary temperature. Further " hot pressing " at a more
elevated temperature brings about a more complete elimina-
tion of liquid acids from the crude once-pressed stearine ; whilst
by chilling the red oils, a separation of part of the solid acids
dissolved in them takes place, so that by filter pressing the
mass fluid red oils run through, whilst an additional quantity of
impure solid acids is retained on the filter cloths.
Manufacture of Lard Oil, and Allied Products. — At the
ordinary temperature of 15° to 25° C., lard constitutes a soft
mass consisting of two kinds of matter, one solid and one fluid;
it is, in fact, an exaggerated case of the mechanical separation
from one another of two constituents of a mixture possessing
different solidifying points when the temperature is maintained
between the two temperatures of fusion, chiefly differing from
the partial solidification of fluid oils on cooling and standing
in that the solid constituent has a higher melting point, and is
present in larger quantity. By placing the lard in close textured
woollen bags supported by wickerwork frames, and subjecting
it to long continued cold pressure (about 10 cwts. per square
inch, lasting for some 18 hours), the fluid constituent is grad-
ually expressed and the solid retained. The former is known as
"lard oil," and constitutes about three-fifths of the whole; the
latter is "lard stearine," and is a valuable material for the pre-
paration of the better kinds of soaps.
Coker butter (cokernut oil kept at not too high a temperature)
and other analogous vegetable semisplid oils or butters, can, in
like manner, be separated by pressure into a fluid " coker oleine,"
and a solid " coker stearine ; " and in similar fashion, the more
fusible fats obtained in the first process for the manufacture of
butterine, solidify at a suitable temperature to a semisolid mass,
which, when carefully pressed, yields a fluid portion becoming
of a buttery consistence when cooled a little further, and a solid
stearine suitable for candle and soap making. Fats of greater
.solidity at ordinary temperatures, such as tallow, when similarly
expressed, also separate into two portions — e.g., liquid " tallow
oil " and solid " tallow stearine."
EXTRACTION OF OIL FROM SEEDS, OIL CAKE, &c.,
BY SOLVENTS.
Most oily matters are extremely freely soluble in benzene,
light petroleum distillate, ether, chloroform, carbon disulphide,
232 OILS, FATS, WAXES, ETC.
and other readily volatile solvents ; so that by bringing such
fluids in contact with the material to be treated, the oleaginous
matter is dissolved, whilst the other constituents are mainly
unaffected. By drawing off the solution and subjecting it to
distillation the solvent is volatilised, and with proper condens-
ing arrangements can be regained with but little loss for use
over again, whilst the oil remains in the still.
A large number of different arrangements have been proposed,
and many are in actual use (more especially on the Continent)
for effecting this purpose, differing in various respects according
to the nature of the material to be treated and the solvent
employed, £c. When the material is rich in oil — e.g., when
palm kernels (ground to meal) are used, and similar substances
not already largely deprived of oil by expression, the apparatus
employed essentially consists of a cylinder or other closed tank
of boiler plate, provided with a manhole for charging and dis-
charging the meal, which is supported on a perforated false
bottom. Into this carbon disulphide is run by gravitation, or
pumped from a well, entering at the bottom and passing upwards
through the mass (or vice versa when light petroleum spirit is
used) • the fluid dissolves out the oil, and runs away at the exit
either direct to the distilling apparatus, or to another similar
cylinder where it dissolves out more oil, furnishing a stronger
solution. With substances less rich in oil, such as oilcakes,
several cylinders are usually worked in succession, the fluid
percolating through each, and ultimately yielding a largely con-
centrated fatty solution, much as in the methodical lixiviation
apparatus employed in dissolving crude sodium carbonate from
black ash in the Leblanc soda process. The supply of disulphide
to the first cylinder is kept up until a sample of the issuing fluid
is found to contain little or no oil in solution. The connection
with the disulphide supply is cut off, and then by means of a
current of compressed air or of steam, the fluid in the first
cylinder is forced onwards into the second, which is then
coupled to the supply, becoming the first of the series. The
disulphide still adherent to the exhausted material in the first
cylinder is volatilised by means of steam, let in under the false
bottom (or at the top), the vapours being carried to a condensing
worm, where a mixture of water and disulphide is condensed.
The exhausted material is then discharged, the cylinder refilled,
and coupled to the series at the far end, so that the disulphide
passing in has already a considerable amount of oil in solution.
In this way the nearly exhausted material is fed with fresh
disulphide, whilst the newly refilled cylinder is supplied with
comparatively strong solution ; the liquid ultimately passing out
is led away to a distilling apparatus, where the volatile disulphide
is steamed off, and the residual fat finally collected.
Fig. 62 (Schadler) illustrates a set of four steam-jacketted
EXTRACTION OF OIL BY SOLVENTS.
233
cylinders thus used in series. A1? A2, A3, A4, are the four vessels
so connected by pipes D1? D2, D3, D4, that the liquid passing off
at the top of each is supplied to the bottom of the next, Al being
reckoned as next to A4. These connections are opened and
closed as required by means of the cocks EI} E0, E3, E4 ; H15 H2,
H3, H4 are pieces of glass tubing serving as gauges. B is the
carbon disulphide supply pipe ; by means of the two-way cocks,
Cj, C2, C3, C4, fresh disulphide can be supplied to any one of the
four vessels as required. N is a steam pipe from which steam is
blown in to any vessel by means of the cocks O15 O2, O3, O4, or
into the jackets through the cocks Pj, P2, P3, P4. F is the
saturated carbon disulphide main, the final solution flowing into
it through the cocks Q-v G2, G3, G4. J is a pipe into which the
liquid contents of the cylinders can be blown off through the
cocks K1? K2, K3, K4. L is a compressed air main from which
air can be supplied to each cylinder by the cocks J\J v M2, M3, M4.
Fig. 02.
Suppose all four vessels filled with material to be exhausted;
by opening the cock C15 connection is established between the
disulphide main, B, and the cylinder A2, through the pipe D,,
and cock E2 ; disulphide then flows into A0, percolating through
the material until the level of the cock C2 is reached ; this is
set so as to shut off the disulphide main and open the connection
with A3 through D2 and E0, consequently the disulphide passes
onwards into Ar In similar fashion it passes successively into
A4 through C3, D3, and E4, and into Al through C4, D4, and Er
Finally, it is drawn off through Gl into the saturated solution
main, F, whence it flows to the still (or an intermediate store
tank). The progress of the extraction is judged by the colour
visible at the gauge, H2 ; when the liquor is seen to be devoid of
colour, all available oil has been dissolved. The cock Cj is
then closed so as to shut off the disulphide supply, E2 is closed,
234
OILS, FATS, WAXES, ETC.
and M2 and K2 opened, so that compressed air enters A9 and
forces the liquid contents out through the discharge pipe, j"; the
steam cocks O2, P2 are then opened, so that the cylinder and
contents are heated, the disulphide vapour thus produced being
driven out along with some water vapour through J to a con-
densing apparatus. To avoid loss of disulphide vapours not
completely condensed but carried away with the escaping air,
this is made to pass through an absorbing vessel containing oil
which dissolves out the disulphide, forming a liquid from which
the disulphide is recovered by distillation when strong enough.
The cylinder A2 being exhausted and all disulphide steamed off,
the manhole is opened, the exhausted charge withdrawn, and
a new one introduced. A2 is then coupled on in front of A1 and
the whole operation recommenced, the order in which the fresh
disulphide passes through the series being now A3, A4, A1? A0,
J J
1C
Fig. 63.
instead of A9, A3, A4, Ap as at first. In similar fashion, A3, A4,
and A! are in turn exhausted and recharged.
Fig. 63 represents a Heyl's distillation apparatus for boiling
off the carbon disulphide from the fatty solution thus obtained.
A is a boiler-plate vessel furnished with a steam jacket, B, at
the base. Steam is let in at C, and the condensed water drawn
off at D. The disulphide solution is supplied at E, the gauge F
enabling the right level to be attained. L is the draw-off pipe
EXTRACTION OF OIL BY SOLVENTS.
235
for the oil finally left ; J J exit leading to condenser ; H an
agitator worked by a handle, G ; K, a tube through which
steam can be led in to a circular pipe at the base inside, per-
forated with a number of minute orifices. The solution being
run in, steam is turned on when boiling soon commences, the
disulphide vapours being led away through J to the condenser.
The agitator, H, facilitates the evaporation ; at the end steam
is blown in through K, so as to pass through the residual' oil in
a multitude of fine streams, and so drive off the last traces of
disulphide vapour. Finally, the oil is drawn off through L, and
a fresh charge introduced.
Fig. 64 represents a simpler form of extraction apparatus
(Deitz's), consisting of an extraction tank, B, into which disul-
phide is pumped at the bottom from the well, A, by the pipe, h,
the fatty solution passing off at the top through the pipe,j^ to
the still, D ; the vapours here evolved are led away through
the pipe, ee, and condensed by the worm, C, the condensed
disulphide returning to the well, A. When the extraction is
complete, the disulphide supply is shut off and steam injected
into B through a coil at the base below the false bottom, d d ;
Fig. 64.
the residual fluid in B is thus forced back into A, and as the
heat becomes greater, the disulphide still remaining in the ex-
hausted mass is volatilised and carried to the worm, C, through
the pipe, e e. The heat is supplied to the still, D, by means of a
steam coil inside ; finally, steam is blown through the residual
oil to remove the last traces of disulphide, and the oil drawn off
through the discharge pipe, i. A series of these extractors is
generally employed, worked in couples alternately.
Carbon disulphide being heavier than water is comparatively
readily protected from evaporation by a layer of that fluid on
its surface ; on the other hand, its vapour is very - readily
236 OILS, FATS, WAXES, ETC.
inflammable, and when breathed for long periods produces a
peculiar form of poisonous action, culminating in a species of
insanity. Light petroleum spirit is cheaper, but, owing to its
being lighter than water, cannot be so well protected from
evaporation and consequent danger of fire and of explosion when
a mixture of its vapour and air is ignited ; moreover, its solvent
action is less rapid. The former solvent is more generally used
in Europe, the latter in America. Grills & Schrceder have
patented the use of liquefied sulphur dioxide at 30° to 40° C.
under a pressure of some six atmospheres as a solvent for oils
for extraction purposes (Patent No. 19,948, Dec. 11, 1889) ; and
Lever & Scott have similarly patented the use of carbon tetra-
chloride, which is said to yield a purer product than carbon
disulphide (Patent No. 18,988, Nov. 26, 1889).
Extraction of Grease from Engine Waste, &c. — The
greasy cotton waste, rags, &c., that accumulate where machinery
is largely used from the wiping of spindles and cleansing of metal
work, &c., and similar materials are sometimes treated with
solvents for the • purpose of recovering the oily matter, after
which the material is more or less cleansed by boiling with
alkalies, &c., and washing, so as either to be capable of use over
again or to be suitable for paper making. The plant used for this
purpose differs little from that above described. An old boiler
or some similar vessel is erected, a false bottom, or grating sup-
plied at the base, and suitable manholes. The solvent liquid is
run in (from the base, if carbon disulphide, because that liquid
becomes lighter by dissolving fatty matters ; from the top, if
light petroleum spirit, for the opposite reason), so as to percolate
through the greasy rags, tfcc., the solution obtained being distilled
so as to recover the solvent and separate the grease. Owing to
the prevalent use of hydrocarbons in preparing lubricating oils,
the grease thus obtained is rarely available for soap making,
except when largely admixed with other fatty materials.
Fig. 65 represents an arrangement used in Lancashire for the
purpose of cleansing engine waste, and recovering grease there-
from. It consists of a vessel of boiler plate, about 9 feet high
and 6 diameter, with a grating, F, forming a false bottom, and a
gooseneck leading to a worm condenser, C ; G is a pipe supplying
steam, and E a cock for withdrawing grease. The grating, F, is
fixed about 2 feet above the bottom, and consists of a disc of
i-inch boiler plate pierced with numerous slightly conical holes,
1J inch diameter on the upper side, 1 inch diameter on the
under side. Some 3 tons of greasy waste are shovelled in
through the upper manhole, A. Coaltar benzene, boiling not
higher than 100° C., or benzoline (light petroleum distillate)
is then pumped in through A, and percolating through the mass
dissolves out grease, accumulating under the false bottom. A is
then closed and made vapour tight with lime paste.
EXTRACTION OF GREASE FROM ENGINE WASTE.
237
Steam is then blown in through the pipe, G ; the vapours
evolved at first become condensed in the comparatively cool mass
of waste above, and thus serve to wash out the remaining greasy
solution adhering thereto ; by and bye the vapours pass over into
the condensing worm, C, made of 2 to 3-inch leaden or iron
piping, arranged so as to form 10 to 12 turns 6 feet in diameter;
a plentiful supply of cold water is admitted at the base of the
cistern in which the worm is set, passing off by an overflow pipe
at the top. Finally, when all volatile matters are expelled from
the still, and nothing but water is condensed in the worm, the
steam is shut off, and the waste extracted through the lower
manhole, B. To complete the cleansing it is boiled in a kier
with soda, washed plentifully with water in a dash- wheel, soaked
in dilute hydrochloric acid to dissolve out oxide of iron, again
Fig. 65.
washed in the dash- wheel, drained in a centrifugal machine, and
hung up to dry. From 50 to 60 per cent, of cleansed waste is
usually thus obtained from the greasy raw material.
The recovered benzene runs along with the condensed water
through D to a covered cistern (conveniently an old boiler),
where the two separate by gravitation ; the lighter hydrocarbon
is pumped up again into the extraction vessel for a new charge,
whilst the water is run away from time to time as it accumulates,
by means of a cock at the bottom of the cistern. The grease thus
recovered is generally too impure to be used directly for anything
but cart grease or other coarse lubricating purposes. By distil-
lation with superheated steam, it may be partially purified
and rendered serviceable for various other purposes.
Somewhat similar methods are in use for the extraction of
" woolfat " from raw wool (vide Chap, xv., lanolin).
Determination of Fat in Seeds, &c. — When it is required
to determine analytically the amount of oleaginous matter
238
OILS, FATS, WAXES, ETC.
present in a solid substance chiefly containing non-fatty con-
stituents (e.y.t crushed seeds or oilcake, the residue left on
evaporating milk or cream, and such like materials), the process
adopted is substantially an application on the small scale of the
general principles involved in the large-scale extraction methods-
above described. When the fatty matter predominates, the
weighed portion of substance is stirred up with ether, chloroform ,
light petroleum spirit, carbon disulphide, or other convenient
solvent, and the whole poured into a weighed paper filter, the
undissolved matters being thoroughly washed out, and examined
as found requisite after drying and weighing (p. 123). When,
however, the fatty constituents are in the minority, the process
is slightly modified : the coarsely powdered material is placed
inside a piece of glass tubing, the lower part of which is
constricted and blocked with cotton wool, glass wool, or asbestos
fibres, &c., so as to form a strainer; the solvent is poured into
the tube, percolates slowly through the pulverised material, and
passes out at the lower end (filtered clear. by the cotton WTOO!)
into a vessel placed to receive it, the dissolved fatty matters
being obtained in weighable form by evaporating off the solvent.
Solution of fatty matter takes place more rapidly under such
circumstances if the solvent be warm; to effect this, as well as
to economise labour and solvent, various devices are in use,
essentially modifications of the
arrangement described bySoxhlet,
and generally known as "Soxhlet's
tube." Fig. 66 represents one of
the earliest forms, and Fig. 67 an
improved form, less fragile. The
substance to be exhausted is placed
.in the wider tube, A (Fig. 66), the
lower part of which is stopped
with a loose plug of cotton wool,
&c., or it is wrapped in filter paper
so as to form a cylindrical package,
fitting loosely into A. No con-
nection subsists between the inte-
rior of B and A except through
the side pipe, C. The lower end
of B is made to pass through a
perforated cork into a weighed
flask ; the upper end of A is
similarly connected with a reflux
condenser, preferably of Allihns
form, Fig. 68. A suitable quan-
tity of solvent being placed in the flask, on heating this (by
a waterbath, <fcc.) the liquid is vapourised, and passes upwards
through B and C to the condenser; the condensed fluid drops
Fig. 66.
Fig. 67.
LABORATORY FAT EXTRACTION PROCESSES.
239
down into A on to the substance to be exhausted ; when the
fatty solution accumulates to the level, h, the siphon, D D D,
begins to act, and draws off the fluid into the flask. After some
20 or 30 siphonings, all trace of fatty matter is dissolved out;
by disconnecting the flask, and evaporating off the remaining
Fig. 68.
solvent, the dissolved oil is obtained. In this way the solution
is effected by means of solvent appreciably warmed by contact
with the hot vapour in the upper part of A, whilst the operation
goes on automatically. v
Figs. 69 and 70 represent an improved form of
Soxhlet tube, arranged by B. Friihling •* the sub-
stance to be examined is placed in the vessel A,
Fig. 69, provided with an internal siphon ; this,
when weighed, is' placed inside the Soxhlet
reservoir, Fig. 70, connected at the top with the
lower end of the reflex condenser, C, and at the
bottom, 6, with the flask for receiving the fatty
solution. The weight of substance left after
removal of oil can thus be determined by simply
reweighing A.
Many other forms of extraction apparatus have
been devised and recommended by various experi-
menters for the quantitative determination of but-
ter fat in milk residues, and such like purposes.
Fig. 71 represents a convenient arrangement on the principle
of Soxhlet's tube for the laboratory extraction of oleaginous
matter from somewhat larger quantities of material.
Fig. 72 represents a modification useful for extracting unsapo-
nifiable matters from liquids — e.g., the alcoholic soap solutions-
obtained by saponifying oils with alcoholic potash. The liquid
is placed in the extraction vessel, A, which contains a number of
glass beads ; the condensed solvent (light petroleum spirit) drops
into the funnel, B, rises up between the beads, washing out
soluble matters from the liquid, and overflows into the distilla-
tion flask, E, down the side tube, h.j
* Zeitsckrift fur anyewanflte Chemie, 1889, p. 242.
t Hcnig & Spitz, Journ. Soc. Chem. Imt., 1891, p. 1039 ; from Zeitsch. f,
angziu. (Jhertue, 1S91, 19, p. £05.
Fig. 69.
240
OILS, FATS, WAXES, ETC.
Some kinds of seeds contain a notable proportion of substances
soluble in ether, other than fatty matters — e.g., phytosterol
(p. 17) and lecithin (or a mixture of lecithins) ; the latter, con-
Fig. 70.
Fig. 71.
Fig. 72.
taining phosphorus, may be estimated by determining the quan-
tity of that element contained in the ether extract (p. 124).
The following table is abbreviated from a larger one given by
Schadler,* representing the usual proportions of total oily or
fatty matter yielded by seeds, nuts, etc., of various kinds on
extraction by solvents : —
* [7nlerxucJtitngen der Fette Ode und Wachsarfen, 1889, p, 4.
PROPORTION OF FATTY MATTER CONTAINED IN SEEDS, ETC. 241
243
OILS, FATS, WAXES, ETC.
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PROPORTION OP FATTY MATTER CONTAINED IN SEEDS, ETC. 243
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244
OILS, FATS, WAXES, ETC.
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ANIMAL FATS. 245
CHAPTER X.
ANIMAL FATTY TISSUE : EXTRACTION OF OILS AND
FATS THEREFROM.
THE " adipose tissue " (ordinarily known as " fat ") of the higher
animals varies considerably in consistence in different cases, but
uniformly consists of a cellular or honeycomb-like structure of
nitrogenous non-fatty matter, the interstices of which are more
or less filled with the true non-nitrogenous fatty material ;
hence mechanical or chemical processes are requisite to separate
the two, just as in the case of vegetable oil-containing seeds, &c.
In some cases the melting point of the animal fat or oil is so
low that processes of expression are applicable at the ordinary
temperature, as in the case of certain fish livers (cod liver oil, &c.) ;
either the fresh organ being used, or livers that have been stored
until partial decomposition has set in, more or less rupturing the
oil cells. In other cases, the temperature requires to be raised
in order that the fatty matter may become sufficiently fluid to
exude, as in the "rendering" of tallow and lard; for this
purpose the adipose tissue may either be subjected alone to
heat, or may be steamed or boiled with water at the ordinary
pressure or in digesters, or may be treated with hot or cold
solvents for the fat, or with substances acting chemically on the
nitrogenous matter of the cell- walls, and thus tending to liberate
the fat. When the nitrogenous matter is required to be saved
in a solid form for manure making, the manufacture of dog-
biscuit, pig feeding, or other purposes according to its quality,
the first method may be employed, care being taken to prevent
burning by overheating if free fire is used ; or the fatty tissue
may be heated in a closed vessel by means of steam and a
minimum of water ; or it may be minced fine and placed on
sloping trays in a chamber heated by steam, so that the' fatty
matter gradually runs away from the solid nitrogenous cellular
tissue. If, on the other hand, the saving of the nitrogenous
matter in the solid form is of no consequence, the comminuted
fat may be heated for some time with water in a digester under
4 or 5 atmospheres pressure ; by this means a considerable pro-
portion of the nitrogenous tissue is gelatinised and dissolved as a
sort of glue, utilised either as such or for manure making. In
extracting fat from bones this process is generally employed;
on the other hand, when the carcases of slaughtered horses, &c.,
are treated, long continued boiling in open pans under ordinary
246 OILS, FATS, WAXES, ETC.
pressure is more usually adopted, the fat being skimmed off from
time to time as it rises. Sometimes a small quantity of soda, or
of sulphuric acid, is added to the water with which rough fats
are boiled, with the object of attacking the cell walls, and
liberating the fatty matter more rapidly. A certain amount of
loss by saponification takes place when soda is thus used (unless
the impure soap formed is collected and utilised) ; whilst hydro-
lysis of glycerides (p. 7) is apt to be brought about by the
action of acid, so that the resulting fat contains free fatty
acids interfering with its use for certain purposes — e.g., the
manufacture of some kinds of lubricants. In the Mege-Mouries
process for preparing oleomargarine of best quality (vide Chap,
xiv.), a sort of artificial digestion of the nitrogenous matter
is brought about, chopped suet being warmed with minced
sheep's stomachs and a little potassium carbonate, so as to pep-
tonise the albuminoids of the tissue and liberate the fatty
matter; a much purer product is thus obtained, owing to the
comparatively low temperature employed (about 45° C.) than is
possible with any boiling process.
Rendering of Fatty Tissues by Dry Fusion. — W7hen rough
fats from the ox, sheep, pig, &c., are minced fine and gently
heated, the melted grease gradually runs away from the solid
cellular tissue. In the manufacture of butter substitutes (oleo-
margarine) finely chopped beef suet is sometimes thus heated to
a temperature only just sufficient to partially fuse the fatty
matter, and the runnings subsequently treated so as to separate
the mass into a solid stearine, and a buttery mass largely con-
sisting of oleine. Owing to the low temperature employed,
50° to 55° C., noxious vapours are not evolved at all during the
process, especially as none but the freshest fatty matter is used,
any admixture of slightly tainted material greatly depreciating
the value of the product.
When higher temperatures (above 100° C.) are used, the rough
fats being heated over a free fire with continual stirring, the
moisture present is evaporated, and the nitrogenous tissue
gradually dries up and shrivels ; the oil cells are thus ruptured,
and the melted fat escapes. The heat usually causes a con-
siderable amount of decomposition of the tissue, leading to the
evolution of most atrocious smells, especially if the fatty tissue is
stale, tainted, or partly decomposed. By straining off the melted
fat, and pressing the residual " greaves '; or " cracklings," in such
a press as is indicated by Figs. 34, 38, or 39 (pp. 202, 205, 206), the
majority of the fat present is extracted ; if the cracklings are in-
tended as food (for dogs or pigs) the presence of a little residual
fat therein is an improvement rather than otherwise; if required,
a further amount of grease can be extracted by boiling with dilute
sulphuric acid, or heating in a pressure vessel, so as partly to
gelatinise the solid animal matter and liberate the remaining fat.
RENDERING BY DRY FUSION. 247
An improved dry heat rendering arrangement has been
patented by Merryweather & Sons, in which the materials to
be rendered are placed in a steam jacketted pan into the jacket
of which superheated steam is passed, so that the danger of
" burning " the fat is greatly lessened, whilst the heat can be
much more easily regulated ; accidents from fire through the pan
contents suddenly foaming over can be minimised, whilst fuel is
economised, and the wear and tear of the pan lessened.
The blubbers of the whale, seal, dugong, porpoise, and other
cetacea, and the livers of the shark, cod, dogfish, kulp, and other
fish, are generally allowed to remain in baskets or other perfor-
ated vessels at the ordinary temperature for some time, so that a
first running of purer oil may be obtained spontaneously ; later
on heat is applied to facilitate the extraction. Formerly " boil-
ing down " whale blubber for train oil was an operation per-
formed on the whaling vessel shortly after the capture of the
animal ; at the present day the blubber is more frequently
brought ashore (either to port or to fishing stations for the pur-
pose) for treatment. A certain amount of oil is generally
collected by the simple process of placing the cut up mass in
racks, from which the oil drips gradually into casks ; later on
decomposition commences, and the oil then exuding is inferior in
quality. Finally, the remaining mass is "boiled" —i.e., sub-
jected to dry heat to extract the remaining oil. In some cases
wet steam heating (infra) is applied at first, whereby the process
is much shortened.
In order to mitigate the nuisance arising from the emanation
of foul smelling vapours during the dry process for rendering
fats, (fee., various contrivances have been tried from time to
time, such as passing the evolved vapours through layers of
charcoal or through scrubbers containing alkaline or acid solu-
tions, *&c. ; the only really effective method, however, depends on
the destruction by combustion of the malodorous emanations,
the fumes and vapours evolved being collected by a hood or pipe
and made to traverse the fireplace of one of the works' boilers ;
or otherwise similarly consumed. Preferably the vessels are
enclosed in a sort of casing, so that the vapours evolved are led
away by means of a pipe to the spot where they are consumed,
an indraught being maintained by means of a fan or steam jet.
Rendering of Fatty Tissues by Heating with Water or
Steam under ordinary Atmospheric Pressure. — The ex-
traction of fatty matter from adipose tissue is often greatly
facilitated by mincing the tissue fine, or crushing it between
rollers, and then placing it in a pan with water, the temperature
of which can be raised as required, either by injecting wet steam,
employing a dry steam coil or steam jacket, or by means of free
fire, &c. For the preparation of oleomargarine a process of this
description is often used as the first stage, selected fresh fat of
248 OILS, FATS, WAXES, ETC.
highest quality being chosen, and the temperature being kept as
low as possible, consistent with the melting out of the more
fusible constituents which rise to the top and are skimmed off.
Latterly, a higher temperature is used, whereby a more solid fat
(when cold) is obtained; and, finally, the heat is raised to 100*
to extract the last portions of fatty matter. This, however, is
rarely completely effected unless either a higher temperature
(under pressure) is applied so as largely to gelatinise the nitro-
genous tissue, or sulphuric acid is added so as to break up the fat
cells by its solvent action on the nitrogenous matter. In the
extraction of fat from bones boiling in open pans for some
twenty-four hours with simple water is often employed, the
bones being broken up into lumps so as to expose the fat cells
as much as possible; the fat is skimmed off as it rises, and the
liquor utilised for the preparation of size ; a larger yield of fat,
however, is obtained when high pressure vessels are employed
(vide infra, p. 251).
Various fish oils are extracted by similar processes ; thus, in
the preparation of cod liver oil, the fresh healthy livers are first
placed in open barrels, so that a certain proportion of oil
spontaneously exudes ; after a while they are transferred to
metal pans, heated gluepot fashion in a larger external hot
water vessel, or by a steam jacket ; here a further separation of
oil ensues, of second quality. Finally, the livers are boiled with
water, when a still lower grade separates. According to the
temperature employed in the first heating, the quality of the
second runnings varies ; when 40° to 50° C. is not exceeded, a
much finer oil is obtained than when 75° to 80° is reached, more
nearly approximating to the first runnings (" cold drawn" oil),
but possessing a more marked brownish yellow tinge. Oil
extracted by boiling with water is usually of a more or less deep
brown hue.
According to P. Moller, of Christiania,* the fishy unpleasant
flavour of cod liver oil is largely due to the absorption of oxygen
during its extraction, and may consequently be to a considerable
extent avoided by rendering the livers in vessels from which all
atmospheric air is excluded by means of a current of indifferent
gas, such as hydrogen or carbon dioxide.
Several species of fish of the herring and sardine class are
employed in different countries as sources of oil, the simplest
method of procedure adopted being to slice and mash the fish,
and pour boiling water over the mass, which is then stored
in barrels, &c., for some time ; decomposition sets in, and the fat
tissues become disintegrated, so that the oil floats up and is
skimmed off at intervals, A more systematic method, adopted
in the case of menhaden oil and other fish oils extracted by
means cf modernised appliances, consists in thoroughly boiling
* English patent, No. 13,803, 1890.
BOILING PROCESSES. 249
or steaming the fish (whole and unbroken, or sliced and mashed),
and then subjecting to comparatively gentle pressure ; the first
runnings thus obtained are considerably superior to the second
grade, prepared by boiling or steaming the residue a second time,
and pressing again with stronger pressure, and at a higher
temperature; the screw press heated by steam, shown in Fig. 38,
p. 205, is well adapted for this process. The ultimate residue is
utilised for manure : after being squeezed as dry as possible,
preferably by hydraulic pressure, the residual solid mass is
broken up and allowed to ferment, dried somewhat, ground and
.sifted, and finally dried further, so as to form a powder
convenient for transport. Large quantities of fish manure are
thus prepared from the residues of the extraction of oil from the
" menhaden " or " porgie " at numerous places along the North
American Atlantic coast.
D'Arcet's sulphuric acid process for rendering tallow consists in
melting the adipose tissue with from one fifth to half its weight
of water, and a few per cents, of sulphuric acid, keeping the
entire mass boiling until the separation of fat is completed, the
heat being applied by means of a free fire, by a steam jacket, or
by directly blowing in steam ; in the latter case, somewhat less
water is originally added, with a proportionate increase in
sulphuric acid strength, to compensate for dilution by condensa-
tion of steam. When this method is adopted, the vessel may be
simply constructed by lining a cask or tank with sheet lead;
whereas, for boiling over free fire, a copper vessel must be
employed, iron being too readily attacked by the acid. In
Evrard's process the sulphuric acid is replaced by caustic soda ;
the evolution of foetid smells is thereby lessened, but loss is apt
to be occasioned through the formation of soap by the action of
the soda on the fat.
When rough fats are rendered in a soapery for use therein, a
simple method of procedure is to place the tissues to be treated
in one of the soap "kettles" or "coppers" (Chap, xix.), and blow
wet steam through the mass ; a large proportion of the fatty
matter is then melted down, and is removed by skimming. To
extract the remainder, weak alkaline leys from other operations
are run in, and the whole boiled up with steam so as to convert
the fat into a kind of impure soap solution, which is run off and
worked up along with other inferior material in the manufacture
of lower grades of scouring soaps.
When partly decomposed tissues, (fee., are boiled to extract fat,
much the same kinds of noxious smells are apt to be evolved as in
the dry process (p. 247); accordingly, when it is essential to avoid
nuisance, it is usual to box in the pans, and lead the evolved
vapours to a condensing chamber where the steam is condensed,
the remaining air, itc., being drawn off to the main chimney
stalk of the works, by which means a continuous indraught is
250
OILS, FATS, WAXES, ETC.
set up, and outward leakage of malodorous vapours avoided. In
the case of putrid materials, the mere dilution of noxious vapours
with the chimney gases thus brought about is not always
sufficient, and destruction of smell by fire must be resorted to in
order to avoid nuisance in certain situations, such as crowded
towns, and the like.
Hendering under Increased Pressure. — Of all processes
Fig. 73.
for obtaining fats from their natural animal sources this one is
the most extensively used, as the higher temperature attained
leads to the more complete gelatinisation of nitrogenous tissue,
and consequently to the more thorough separation of fat. Fig. 73
represents a digester employed in Wilson's process for rendering
RENDERING UNDER PRESSURE. 251
tallow and lard ; a series of these is generally worked together,
each of 10,000 or 15,000 gallons capacity, or even more. In
large American slaughterhouses (e.g., at Chicago, St. Louis,
Cincinnati, <tc.), each digester is kept for the production of one
kind of fatty matter only, the adipose tissue being usually
worked up therein within a few minutes after slaughtering ;
hence injury through use of stale or decomposed fatty tissue is
avoided, and extremely uniform grades of lard and tallow ob-
tained, the various portions of the carcases being separately
treated in different vessels according to the part of the body
employed. The boiler is provided with a false bottom ; a dis-
charging orifice, E, covered when required by a plate, F, raised
or lowered as required by the rod, G, passing through a stuffing
box ; an internal steam coil at the base fed with steam from an
ordinary boiler by the pipe, "V, and steam cock, B ; and a series
of draw-off cocks at the side, TJ, p, j), p, p, R. A safety valve, O,
is also provided, and a manhole at the top, K. The discharging
valve being closed by lowering F, the fat to be rendered is
introduced through the manhole, K, until within 2 to 2^- feet of
the top ; the manhole being closed steam is admitted through
the cock, B, until the desired pressure is obtained (usually 3 to
4 atmospheres). Much water condenses during the heating up ;
if requisite this is drawn off from time to time by means of the
lowest cock, U, the progress of the fusion being tested and
regulated by opening the top cock, R, so as to see whether steam
only escapes, or melted fat. After ten to fifteen hours the steam
supply is shut off and the excess pressure relieved by opening
the safety valve ; the whole is then allowed to remain at rest
<i while so that the fatty matter and water may separate, when
the former is drawn off into coolers through the side cocks,
Pi Pi Pi Pi and the latter through the lowest cock, U. The aque-
ous liquor contains much nitrogenous 'matter in solution and is
utilised for manurial purposes. The boiler is finally discharged
of solid contents by raising the valve, F ; the matters ejected are
collected in a tub, T, and if not completely freed from fat are
returned to the boiler and worked over again with the next
charge.
Extraction of Fat from Bones. — Before bones are treated
for the preparation of manure, animal charcoal, &c., the fatty
matters contained therein are usually more or less completely
extracted by one or other of a variety of processes ; of these the
simplest consists in boiling the bones (preferably crushed into
coarse fragments) with water heated by a steam jet or otherwise;
the fatty matters are thus melted out and obtained by skimming
off as they rise to the top of the water. A large fraction of the
total fatty matter is thus left behind in the osseous tissue through
incomplete removal ; a better yield is obtained when the heating
is effected under increased pressure in a digester, the steam then
252
OILS, FATS, WAXES, ETC.
penetrating into the minute cavities and more completely dis-
placing the melted fat ; moreover, the nitrogenous cell wall con-
stituents are usually gelatinised to a greater extent than is
effected by open pan boiling, so as to facilitate the escape of fat ;
for this same reason, however, the bones thus treated are ren-
dered poorer in organic constituents, and, therefore, less suitable
as manure or for animal charcoal making ; on the other hand,
more soluble organic matter, suitable for glue making or for
manure, tfcc., is obtained in the watery liquor.
Various forms of digester are in use ; a useful variety consists
of a vertical wrought iron barrel or cylinder some 6 feet long and
3 feet 6 inches diameter, slightly
tapering at each end, and fitted with
flanges to which iron discs can be
bolted (Fig. 74). The upper plate,
b, serves as lid, so that when re-
moved fresh bones can be introduced ;
the lower one, .c, is slightly curved ;
when removed the boiled bones are
discharged. A charge of 2 to 2J tons
of crushed bones being introduced the
plates are bolted on steamtight, the
operation being facilitated by fasten-
ing the plates on with hinges so that
they are virtually doors. Steam at
3J to 4 atmospheres pressure (56 to
65 Ibs.) is then introduced for about
three-quarters of an hour ; wrhen shut
off the pressure is relieved, and the
whole allowed to stand for half an hour, when the condensed
water and melted fat are drawn off through a tap, /, in the
bottom plate or door. This door is then opened and the ex-
hausted bones removed, after which a fresh charge is intro-
duced and worked off as before. Even when operating in this
way a certain amount of fatty matter is still left in the bones ;
to avoid this, in some Continental factories solvents are used
(carbon disulphide, benzene, light petroleum distillate, &c.), the
mode of treatment being very much the same as that adopted
for the similar extraction of grease from vegetable marcs, engine
waste, &c. (vide p. 236) ; the crushed bones being placed in suit-
able vessels into which the solvent is run, preferably traversing
several in succession, and the fatty solution being subsequently
distilled to recover the solvent and obtain the grease.
Owing to the peculiar texture of bone as compared with
vegetable seeds, even this mode of treatment does not produce
a perfect solution and removal of all the fatty matters present ;
in order to obtain a larger yield, various modifications of the
plant have been introduced, whereby the solvents are made to
Fig. 74.
EXTRACTION OF FAT FROM BONES.
253
act on the crushed bones in the form of vapour. In one form of
apparatus, this is effected under increased pressure (after pump-
ing out all atmospheric air from the vessel employed), so that the
solvent enters thoroughly into the pores of the bone fragments,
and being attracted to and condensed by the fatty matters, forms
a fluid solution of fat which exudes and runs down to the
bottom, and is subsequently distilled (Seltsam's process). In.
another form the crushed bones are permeated with a mixture
of steam and vapour of solvent, which is condensed by a worm
so as to drop down again upon the bones and percolate through
them to a false bottom, where the solvent is again volatilised
by a steam coil, the whole arrangement being not unlike that
used for cleansing engine waste (Fig. 65, p. 237). Fig. 75 re-
presents Leuner's apparatus arranged on this principle (Schadler).
254: OILS, FATS, WAXES, ETC.
The crushed bones are placed in A above the perforated false
bottom, B. C is a steam pipe, by means of which the bones are
steamed as a preliminary, the surplus steam escaping through
the exit pipe D. After steaming, water and benzene are run in
from the reservoir, F, into the space under the false bottom, and
heated up by the steam coil, P. The evolved vapours are con-
densed in the worm, K, and at first run back over the bones
through the cock, L, the vapour passing upwards to the worm
through J, and the condensed liquid being divided into separate
streams by the spreading plate, O. After some time the cock,
G, is opened, so that the condensed liquid runs into the reser-
voir, F, instead of flowing back into A. When all the solvent
has been volatilised, nothing but water condenses in the worm,
which is known by means of a sampling cock attached to J ; the
draw off cock, E, is then opened, and the watery gelatine solu-
tion and oily matter run off into a suitable separating receptacle ;
A, is then discharged through a manhole and refilled, and the
whole operation repeated.
Another method of operating is to introduce the crushed bones
into a sufficiently strong false-bottomed vessel, from which the
air is then pumped. Benzene, carbon disulphide, or other con-
venient volatile solvent is then run in until the vessel is filled,
whereby the solvent fluid is driven thoroughly into the pores of
the bone tissues. By drawing off most of the fluid and then again
exhausting, the solvent is to a great extent volatilised ; and by
readmitting* air the vapour is again condensed by the increased
pressure so as to wash out the fat solution from the bone frag-
ments. This solution runs down to the base of the vessel, and
is ultimately distilled by working the air pump, leaving the fat
whilst the vapour of the solvent pumped out is condensed by
cooling and used over again.*
CHAPTER XI.
REFINING AND BLEACHING ANIMAL AND VEGETABLE
OILS AND FATS, WAXES, &c.
SUSPENDED MATTERS.
OILS and fats as obtained by many of the processes in ordinary
use contain various impurities partly in suspension, partly in
solution. Of these the most objectionable are the gummy
* For further details of bonefat extracting plant vide Schadler, Technologic
der Fette und Oete, 2nd Edition, edited by Lohmaun, p. 9_'8, et. seq. Also
for Seltsam's process, Journ. Soc. Chem. Ind., 1882, p. 112.
CLARIFICATION. 255
mucilaginous or albuminous matters which generally accompany
expressed oils and rendered fats to a greater or lesser extent,
because unless speedily removed they are apt to undergo
fermentative or putrefactive changes, which not only induce
hydrolysis of the glycerides (p. 10) but also charge the oil with
malodorous bye-products of decomposition, rendering the oil
"rancid." Substances of this kind are usually chiefly in suspen-
sion in the oil ; so that by passing the freshly expressed oil
through a filterpress (p. 228), a considerable proportion of the
suspended matter is removed, rendering the oil in many cases
sufficiently clear and free from visible impurities to be at once
saleable. Sometimes, however, the suspended matter is present
in a form where filtration alone produces only an insufficient
amount of purification, and where even prolonged standing does
not efficiently clarify the oil by subsidence ; this happens more
especially when the mucilaginous matter is disseminated through-
out the oil in a sort of highly diluted jelly-like condition, some-
what analogous to colloidal gelatine or thin starch paste, where
the constituent particles are mostly too fine to be stopped by
means of ordinary porous filtering media, or to gravitate rapidly.
In such cases special mechanical or chemical treatment must
be resorted to in order to coagulate the mucilaginous matter :
sometimes simply heating produces this effect, the albuminous-
substances being solidified and coagulated somewhat like white
of egg. This is conveniently effected by blowing steam through
the oil by means of a fine rose jet ; the condensation of water
facilitates the action as the coagulated albuminous matter attracts
moisture and becomes increased in bulk and deposits more readily
as a flocculent precipitate on standing. The addition of small
quantities of various chemicals often produces an analogous effect ;
thus a small percentage of sulphuric acid, or of concentrated zinc
chloride solution (sp. gr. 1*65), well agitated with the oil causes
on standing the gradual deposition of mucilage, along with most
of the acid, the rest being subsequently removed by agitation
with water. Oils containing resinous matter (e.g., cotton-seed
oil) as well as mucilage are preferably refined by similar treat-
ment with alkalies, the resin being thereby dissolved out and
removed as well as vegetable mucus.
The purely physical action exerted by particles of suspended
matter as regards attracting the colloidal mucilage often serves
to remove the latter ; thus clay, fuller's earth, sand, particles of
oilcake, powdered charcoal, and similar materials, when well
agitated with the oil or melted fat to be treated, tend to unite
with the mucilage, in such fashion that by allowing the whole to
subside, or by filtering it, the whole of the suspended matter is
simultaneously separated.*
* In many cases a very satisfactory degree of purification is readily
effected by b mply adding to the mucilaginous oil, as it runs from the press,
256 OILS, FATS, WAXES, ETC.
In certain cases the addition of chemicals that combine with
the albuminous matter forming precipitates answers the same
purpose ; thus oakbark infusion and other forms of tannin solu-
tion, when well agitated with the oil to be treated, cause the
formation of insoluble tanno-gelatinous matter which precipitates
on standing carrying down with it most of the colloidal suspended
matter. Various metallic salts (copper sulphate, manganese sul-
phate, lead acetate, <fec.) are sometimes used with a similar object.
A process of this kind sometimes used for cleansing rancid tallow
is to boil up with a small quantity of soda ley ; the melted
fat is removed from the soap produced by ladling off, and then
boiled up with a weak solution of alum ; after settling, the
purified tallow is again run off and heated by itself to 150° C.
and upwards, whereby it becomes greatly whitened and har-
dened.*
Dissolved Matters. — Other impurities are dissolved in the
oil, and the complete separation of these is in many cases imprac-
ticable. Resinous matters are the commonest impurities found
in solution ; these are generally of a feebly acid character, so that
agitation with small proportions of alkaline solution removes the
larger part or even the whole of these. For this purpose soda,
potash, milk of lime, and calcined magnesia are employed in
different instances ; carbonated alkalies and alkaline earths
(carbonate of soda, lime, &c.) usually act only imperfectly.
When the proportion of resin is at all large the saponaceous
compound formed sometimes separates only with difficulty from
the clarified oil ; agitation with saline solutions (sulphate of soda,
or common salt, <kc.) in such cases generally causes the mass to
separate into three layers on standing : the lowest one a watery
fluid containing chiefly inorganic salts in solution ; the upper-
most, clarified oil ; intermediately, a more or less frothy spumous
mass of " foots." Frequently this contains so much unaltered oil
mechanically entangled as to be a highly valuable material for
soapmaking, the resinous soap also present usually not interfering
with this application.
Bonefat extracted by boiling processes generally retains in
solution phosphate of lime and other calcium salts to an extent
greatly interfering with the preparation of soap from this mate-
rial : boiling with dilute sulphuric or hydrochloric acid converts
the lime into calcium sulphate or chloride, and completely
removes these inorganic dissolved impurities, the operation
being very simply performed by placing the fat in a tank lined
a small quantity of cake parings ground up by edgestones (p. 219), and then
passing the whole through a lilterpress ; the residue left in the filterpress
is returned to the kettle and worked up with fresh crushed seed, &c.
Still better clarification may often be effected by heating the mixture of
oil and parings, so as to coagulate albuminous matter, and then passing
through the filterpress.
*0il Trade Review, Oct. 1884.
DISSOLVED IMPURITIES.
257
with sheet lead along with a sufficient quantity of highly diluted
acid, and blowing wet steam through the mass so as to agitate it
thoroughly. Sulphuric acid has the advantage of cheapness and
of acting less on the lead than hydrochloric acid ; on the other
hand insoluble calcium sulphate forms and is deposited, whereas
calcium chloride, being readily soluble, does not separate in the
solid form.
Certain oils when chilled deposit the less readily fusible con-
stituents as " stearines " (p. 110) ; on subjecting these to nitration
and pressure, an oleine practically free from suspended albu-
minous matters generally results, any such impurities being
mostly retained along with the stearine. A partial separation
of stearine by allowing to stand at a relatively low temperature,
is accordingly sometimes resorted to as a means of clarifying and
refining oils, more especially the more expensive edible oils
(" salad " oils) ; the thickened mass being filterpressed whilst
chilled, or on the small scale being strained through rough filters
of moss, cotton wool, charcoal, &c., placed between the perforated
bottoms of two boxes, one just fitting inside the other. Oils
that have been thus treated are sometimes termed " winter oils "
— i.e., oils still remaining fluid in winter ; whilst untreated oils
that become turbid or partially solidify on chilling and are only
clear in warm situations are designated " summer oils."
Oil or Fat.
Percentage of
Unsaponiflable Matter.
Allen & Thomson
Schiidler.
Cotton seed oil,
1-64
1-85
Coker butter, .
0-80
Hempseed oil, .
1-00
Japanese wax, .
1-14
1-20
Cod liver oil (brown),
1-32
1-45
„ (light), .
0-46
0-50
Linseed oil,
1-10
Almond oil,
0-45
Poppyseed oil, .
Olive oil (yellow),
0:75
1-15
0-80
,, ,, (green),
1-50
Palm butter, .
1-25
Rapeseed oil (crude),
1-00
1-30
,, ,, (refined),
0-15
Hog's lard,
Tallow, .
0-23
0-30
0'50
Even after as complete a removal as possible of suspended
albuminous and mucilaginous matter and of dissolved resin, most
natural oils and fats contain in solution small quantities of non-
saponifiable nonresinous matters ; in some cases cholesterol or
17
258
OILS, FATS, WAXES, ETC.
isomerides thereof (isocholesterol, phytosterol, &c.) have been
identified as present — e.g., in olive oil. The figures quoted on
p. 257 are given by Allen and Thomson * and Schadler f as
representative ones in various cases.
The folio wing figures were obtained by Thomson and Ballantine|
in the course of an extended examination of numerous samples
of oils : —
Xame of Oil.
Percentage of
TJnsaponifiable Matter.
Olive oil (13 kinds), .
1-04 to 1-42
Cotton seed oil (crude),
1-12
,, ,, (refined),
TO?
Rape oil (Colza, 5 kinds),
•58 to '70
Arachis oil, .
•54 to -94
Linseed oil (4 kinds), .
1-06 to 1-28
Castor oil, .
•30 to -37
Southern sperm oil,
37-41
Arctic sperm oil (bottlenose ,
36-32
Whale oil (pale), .
1-82
Seal oil (4 kinds),
•42 to '51
Cod oil (3 kinds),
•87 to 1-87
Menhaden, .
1-60
In the analysis of soap (Chap, xxi.), as the unsaponifiable sub-
stances originally contained in the fatty matters employed for
the most part pass into the soap during manufacture, a correction
on this score is requisite when it is desired to determine the
mean equivalent of the fatty acids present (p. 172). According to
the author's experience the amount of matters of unsaponifiable
nature thus contained in 100 parts of fatty acids, &c., separable
from the soap by means of a mineral acid generally lies between
•25 and I'O part, averaging near to '5 to '75 — i.e., in the case of
soaps made from natural oils and fats, to which no additional
unsaponifiable matters have been intentionally added. When
woolgrease or Yorkshire grease (Chap, xn.) has been used, either
purposely as an ingredient, or unwittingly in the form of an
adulteration of tallow, &c., the proportion becomes markedly
increased ; with oleine soaps made from distilled oleine a,
few per cents, of hydrocarbons are often present, formed during
the distillation of the fatty acids, smaller quantities being often
found in soaps made from oleines prepared in the autoclave
without distillation. When paraffin oils have been intermixed
with the soap, as in the case of certain kinds of laundry soaps,
the percentage of unsaponifiable matters is largely increased.
* Chemical News, 43, 267.
t Technologic der Fette und Ode, p. 61.
$Journ. Soc. Chem. Ind., 1891, p. 233.
OIL REFINING — ACID PROCESS. 259
The fatty matters extracted by solvents from certain legu-
minous plant seeds (peas, lupins, &c.) contain relatively consider-
able proportions of glycerophosphoric choline derivatives of the
nature of lecithin (p. 121) : the existence of small quantities of
substances of this class in oils expressed for commercial purposes
is extremely probable, but little or no knowledge is extant as to
how far this is the case. The husk of the seeds of Lupinus luteus
yields to ether a crystallisable substance, lupeol, analogous to
cholesterol, but derived from a hydrocarbon poorer in hydrogen
(vide p. 17) ; whilst the seed husks of PJiaseolus vulgaris contain
a higher homologue of phenol (viz. pliasol, C15H24O) together
with paraphytosterol (p. 16); in all probability several such
substances akin to cholesterol and phytosterol are contained in
small quantities in seed oils.
SULPHURIC ACID PROCESS FOR REFINING OILS, &c..
(THENARD PROCESS).
In employing sulphuric acid as a clarifying agent it is requisite
that no large excess should be used otherwise a charring action
is apt to be set up on the oil itself, darkening its colour and
depreciating its value. In refining linseed oil from one-hundredth
to one-fiftieth part (1 to 2 per cent.) of acid* is thoroughly inter-
mixed with the oil in an efficient agitator at a temperature not
exceeding 40° (about 104° F.), and the whole allowed to rest for
24 hours. 60 to 70 per cent, of warm water at about 60° C.
(140° F.) is then well intermixed and the whole allowed to stand
some days ; a watery acid liquid separates at the bottom with a
layer of flocculent " foots," above which is the clarified oil, which
is drawn off and again agitated with warm water as before to
wash out any residual suspended acid vesicles. Another method
of operating (Cogaii's process) is to use 1 per cent, of acid diluted
with as much more of water ; this is well intermixed, and after
standing some hours is heated up to 100° C. by blowing in steam
through a fine rose jet at the bottom of a copper vessel. This
temperature is maintained for several hours, after which the
whole is allowed to stand at rest so as to separate the watery
acid and foots from the clear oil. In order to draw off the oil
without disturbing the water and foots, a conical separating
vessel is generally employed with taps at various levels so that
all clear oil above a given level can be drawn off without disturb-
ing that below.
Rape (colza) and linseed oils and certain fish oils are those most
usually refined by the acid process. Oils intended for lubrication
* Hartley recommends that the acid should be diluted with water before
mixing with the oil, so as not to contain more than 30 per cent, of actual
^60 OILS, FATS, WAXES, ETC.
are as a rule the least suitable for such treatment, inasmuch as
the presence of free fatty acids (and a fortiori of possible traces
of mineral acids) is a serious objection with most such substances,
corrosion of bearings and shafts, &c., being apt to be thereby
occasioned. For oils intended for burning in lamps the presence
of any considerable amount of free fatty acids is also objectionable
as tending to cause charring of the wick.
R. v. Wagner recommends the use of zinc chloride solution of
sp. gr. 1-85 instead of sulphuric acid, using about 1^ parts per
100 of oil. Albuminous impurities are equally destroyed or
coagulated, whilst there is less danger of injurious action on the
oil itself. Hartley finds that a strong solution of manganese
sulphate answers well.
ALKALINE REFINING PROCESSES.
As already stated, processes where alkalies are used as agents
for coagulating and removing mucus, albuminoids, &c., have
several advantages over the acid methods, notably that free fatty
acids and resins are also removed. The quantity and strength
of the alkaline ley employed varies with the nature of the oil to
be treated ; any undue excess is apt to lead to more or less
considerable loss, not only by producing more saponification but
also because the extra amount of saponaceous products gives rise
to the formation of more foots containing clarified oil entangled
therein. The requisite quantity of ley and the oil are well
agitated together by any suitable mechanical mixer (either in
the cold or heated to the requisite temperature, as the case may
require), and the whole then allowed to settle ; a heavier watery
fluid with soapy foots separates ; this is drawn off and the process
repeated with a much weaker alkaline solution, and subsequently
with plain water. When considerable quantities of resin are
present, as in the case of cotton seed oil, the ley may conveniently
be of sp. gr. 1-06 up to 1*10 ; in such cases it frequently happens
that the watery layer and foots will not separate thoroughly
from the oil without the subsequent addition of a little salt
or brine. To avoid the formation of emulsions Hageman
employs as purifying agent soda crystals heated to about
80° so as to fuse in their water of crystallisation ; after inter-
mixture by agitation the mass separates on standing into three
sharply defined layers of purified oil, soapy matters, and watery
fluid respectively, but without any notable production of emul-
sion.
Sometimes oils are required to be treated that have become
more or less rancid by keeping, owing to fermentative changes,
atmospheric oxidation, or other causes, but where most of the
mucilage, &c., originally present has been already removed. In
such cases thorough agitation with a weak solution of caustic
ALKALINE PROCESSES — FOOTS. 261
soda, or a somewhat stronger one of sodium carbonate, suffices
to remove the free fatty acids of low molecular weight (butyric,
caproic acids, &c.) that are present, as well as others, if already
formed by hydrolysis ; and to dissolve out most, if not all of the
malodorous non-acid products of decomposition, so as to sweeten
the oil. Diluted milk of lime and calcined magnesia are some-
times used in a similar fashion. As a rule oils that have once
become rancid, even if pretty thoroughly 'sweetened by such
refining, are more apt to turn rancid again on keeping than
fresh ones. In some cases agitation with water alone without
alkalies suffices to wash out the objectionable decomposition
products to a considerable extent ; thus rank butter is greatly
sweetened by simply being thoroughly worked about and washed
in water.
Cokemut oil of inferior quality may be greatly improved by
boiling up with about ^ of its weight of soda lye, specific
gravity 1 -03, for half an hour, skimming frequently. Some 4 or
5 Ibs. of salt per ton of oil are then added, and the boiling con-
tinued for another half hour. Another equal quantity of salt is
then added, and the whole boiled up : after standing till next
day the cleansed oil is run off from the brine and foots that have
subsided.
Crude spermaceti is generally refined by processes partly
involving the mechanical expression of fluid oil, somewhat
after the fashion of stearine pressing (p. 229), and partly
of a chemical nature, more especially boiling up with a small
quantity of potash ley ; this dissolves out free fatty acid formed
by the hydrolysis of the cetin or otherwise, and saponifies most
of the residual fluid oil, this being more readily acted upon by
alkalies than cetyl palmitate itself. Simultaneously, however,
some of the latter becomes saponified, and in consequence the
foots contain more or less considerable amounts of potassium
palmitate, etc., whilst the purified spermaceti contains an ad-
mixture of cetylic alcohol (p. 171).
Utilisation of " Foots." — The foots obtained from oils con-
taining considerable quantities of resinous matter (e.g., cotton
seed oil foots) are sometimes directly worked up into soap by
admixture with other materials in the soap boiling process.
When their colour or nature prevents this being done, they are
generally acidified so as to decompose the soaps present; the
mixture of fatty and resinous acids and more or less unde-
composed glycerides thus obtained is usually distilled by means
of superheated steam, whereby the glycerides present are hydro-
lysed; the fatty acids distil over, whilst the resinous matters
mostly remain behind as a pitchy mass. To some extent, how-
ever, the materials are generally broken up by the heat with the
formation of high-boiling hydrocarbons and water, the former of
which partly distil with the fatty acids ; the result of which is
262 OILS, FATS, WAXES, ETC.
that "distilled oleines" obtained from products of this kind
(p. 110) will not wholly dissolve in alkaline solutions to soaps,
the hydrocarbons remaining undissolved. On agitating the
liquid with an appropriate volatile solvent (ether, benzoline, <fec.)
a quantity of unsaponifiable matter can usually be dissolved out
from the soap solution to the amount of several per cents, of the
distilled oleine employed. The same remarks apply a fortiori
to the analogous products obtained when "Yorkshire grease"
(Chap, xii.), woolgrease, and similar materials are distilled by
means of superheated steam.
The appliances used for such distillation with superheated
steam essentially consist of a boiler for steam raising ; a super-
heater whereby the steam is heated considerably above the
temperature of the boiler, generally consisting of a coil of iron
tubing heated in a flue or some analogous arrangement; a
distilling vessel into which the material to be distilled is run, the
steam being then blown through it in numerous fine streams by
means of a rose jet at the bottom, or a coil perforated with small
holes ; and a condensing apparatus in which the evolved vapours
and the steam are condensed. In Chap. xvi. are described the
arrangements employed in the candle material manufacture for
the distillation of fatty acids and glycerol by means of super-
heated steam ; those used for the distillation of foots, recovered
greases, &c., do not greatly differ therefrom.
It often happens that the solidity of a grease, ifec., is greatly
increased by the process of distillation with superheated steam,
so that a comparatively soft grease after distillation gives a
product of much stiffer consistence, and capable of yielding
a considerable amount of solid "stearine" by pressure. The
cause of this is not absolutely certain ; but it is extremelv
probable that it is due to the conversion of oleic acid into
isomerides of higher melting point, isoleic acid, or stearolactone,
or both (p. 30) ; just as these products are formed by the action
of zinc chloride on oleic acid (p. 142), or during the decomposition
of glycerides by sulphuric acid and their subsequent distillation
with superheated steam in the "Wilson" process for obtaining
candle material (Chap, xvi.)
Precipitation Processes. — In some few cases mucilaginous
or albuminous matters are contained in oils and fats not readily
removable by mechanical means alone, such as subsidence or
filtration, but readily coagulable by means of certain metallic
compounds or substances containing tannin. Thus in " boiling "
linseed oil to improve its drying qualities (Chap, xiv.) sulphate of
zinc, acetate of lead, sulphate of manganese, and other metallic
salts are sometimes used not only for the purpose of facilitating
the incipient oxidation and physical alteration required to
make the oil dry to a varnish more rapidly, but also in order
to combine with, and remove by subsidence, the last portions of
BLEACHING OILS AND FATS. 263
vegetable mucilage, &c., not entirely removed by previous refining
operations. Some kinds of fish oils are similarly improved by
vigorous agitation with oakbark infusion or other liquors con-
taining tannin, conveniently effected by blowing a rapid current
of steam through the whole : gelatin is thus precipitated and
removed by deposition on standing, any excess of tannin taken
up by the oil being subsequently removed by agitation with lead
solution or other appropriate metallic salt. Copper sulphate
solution, alone or mixed with brine, when thoroughly inter-
mixed with fish oils, may often be used effectively for removing
gelatin, etc., therefrom by precipitating it as an insoluble com-
pound.
H. Nordlinger has recently patented * a process for refining
vegetable oils and precipitating mucilaginous matter consisting
of the preparation of "purification-oils" by dissolving in from
10 to 20 parts of oil the zinc, cadmium, iron, manganese, lead or
copper salts of the higher fatty aciols (metallic soaps), at a
temperature of about 150° C., and allowing to clarify by sub-
sidence. From 5 to 10 per cent, of the metallic soap solution
thus prepared is then added to the oil to be treated and the
whole allowed to stand some time, when precipitates are formed
by the interaction on one another of the mucilaginous matter
and the metallic compounds ; the clear supernatant purified oil
is drawn off when the action is complete.
Hartley and Blenkinsop have patented (No. 11629, 1890) the
use for refining linseed oil of a solution of manganese linoleate in
011 of turpentine or other suitable solvent : 1 part of manganese
salt to 800 of oil suffices. If much mucilage is present the oil
is previously treated with sulphuric acid of 30 per cent. By
blowing a current of air or oxygen through the mass at a tem-
perature of about 190° F. (88° C.), bleaching is readily effected,
the manganese salt acting as a carrier of oxygen.
BLEACHING OILS AND FATS.
The colours exhibited by certain oils and fats, as obtained from
their respective sources, are in general due to the presence of
natural organic colouring matters (xanthophyll, erythrophyll,
chlorophyll, &c.) in solution in the oil ; in some cases these are
mostly mechanically carried down by the mucilaginous matter
present during clarification by subsidence, &c., more especially
when heat is also applied to promote the coagulation of albu-
minous impurities, and particularly when oakbark or other
sources of tannin are employed as precipitants of these bodies ;
in some instances albumin or gelatin is purposely added along
with tannin, to precipitate the colour. Some colouring matters
are removable by treatment with animal charcoal and filtration
* German Patent, No. 58959.
264 OILS, FATS, WAXES, ETC.
somewhat after the fashion of sugar refining ; exposure to a
moderately high temperature destroys others ; whilst in yet
other cases chemical bleaching agents are requisite, such as
oxidation by the action of air blown through the heated oil,
either alone or in presence of oxygen carriers ; or chlorination
by means of small quantities of bleaching powder or chlorate
along with hydrochloric acid ; or both together by means of
potassium dichromate and dilute hydrochloric acid. With high
priced substances such as beeswax, bleaching by exposure to air
and light in thin cakes or ribbons, and in some cases treatment
with nitric acid or peroxide of hydrogen, is applicable, although
the cost of labour and chemicals is prohibitive of such methods
in the case of the cheaper oils, £c. On the other hand, reducing
agents, such as ferrous sulphate or sulphurous acid, answer better
than oxidising ones with some kinds of oils — e.g., linseed oil.
Hot Air Process. — Certain fats, especially tallow and palm
butter, can be pretty thoroughly decolorised by heating them
and passing a current of air through the dry mass (containing no
interspersed water) by means of a large rose with fine orifices, so
that many fine streams of air bubbles rise through the hot fat.
A temperature somewhat short of that of boiling wrater generally
suffices (80° to 90° C.) In the case of palm oil a somewhat
higher temperature, 125° to 130° C.,* also effects the destruction
of the colouring matter in the absence of air ; a considerable
amount of the glyceride is thereby decomposed with evolution of
acrolein, and formation of free palmitic acid. Many fish oils are
greatly lightened in colour by blowing air through the mass,
heated to near 100° in a steam jacketted vessel ; in these cases
the oil itself generally becomes more or less oxidised, increasing
in density and viscidity, especially if the air-treatment be
carried too far (vide "blown oils," Chap, xiv.) In. Hartley and
Blinkinsop's process for refining linseed oil (supra), the oxidising
action of the air is intensified by adding a manganese soap
which acts as a carrier of oxygen.
Instead of blowing a stream of air through the oil to be treated,
Teal f exposes rapeseed or linseed oil, &c., in a finely divided
stream to air at a temperature of about 170° F. (71° C.), in order
to " brighten " the oil.
W. Mills I bleaches and purifies nondrying oils and fats by
means of a mixture of hot air and volatilised sulphur trioxide,
S03, passed into a " mixer " capable of withstanding a pressure
of 2 atmospheres. The sulphur trioxide acts as an oxidising
agent, becoming reduced to sulphur dioxide, which also is
effective, especially whilst nascent.
* 240° C. , according to Pohl, who first introduced the process. Dingier
Polyt. Journ., cxxxv., 140.
+ Eng. Patent Spec., 18,744, 1892.
I Eng. Patent Spec., 18,224, 181)1.
BICHROMATE PROCESS. 265
Bichromate Processes. — Tn the bleaching of raw palm oil
by Watts' bichromate process, the oil is rendered quite fluid by
heating it to 40° to 50° C., and is intermixed with 1 to 1-25 per
cent, of its weight of potassium dichromate dissolved in hot
water (22 to 28 Ibs. per ton). Strong hydrochloric acid solution
to the extent of 2 to 2 -5 per cent, of the oil is then run in with
vigorous agitation, enough being used to ensure that a slight
excess of free acid shall finally be present in addition to that
neutralised by the chromium and potassium. The reddish orange
hue changes rapidly, first to a dark brown, then to a brownish
green, and finally to a light green, the operation taking only a
few minutes. The whole is then heated up by blowing wet
steam through, and allowed to stand at rest for some hours ; the
supernatant bleached oil is drawn off and used directly for
soapmaking, &c., or is washed by agitation with hot water, and
standing to remove traces of chrome liquor. The " green liquor "
resulting from the operation is sometimes worked up to recover
the chrome by adding milk of lime so as to form a precipitate of
chromium hydrate mixed with lime ; this is washed and drained,
and then roasted, whereby oxygen is taken up and calcium
chromate formed, used for a fresh batch instead of potassium
dichromate. When there are difficulties as to running waste
chrome liquors away into water courses, £c., this method of
regeneration is practically imperative ; but unless a proper
amount of scientific skill and supervision is exercised (not always
available in a soapery), the cost of labour and fuel, ttc., is apt to
materially outweigh the value of the potassium dichromate saved,
except when the price of this salt is unusually high.
Instead of hydrochloric acid, a mixture of two parts sulphuric
acid and three common salt may be employed, the latter being
dissolved along with the dichromate, and the former gradually
run in to the mass after having been diluted with about twice
its bulk of water. If the temperature be too high, the bleach-
ing is not always successful, a brownish " foxy " shade being
developed ; about 45° to 50° C. may be taken as a working
maximum ; the proportion of dichromate used need not exceed
28 Ib. to the ton (J^ part = 1'25 per cent.) in skilled hands.
A similar mode of treatment is available with many other oils,
the use of hydrochloric acid to generate nascent chlorine not
being necessary in all cases ; thus with various fish oils a few
pounds of dichromate to the ton, with about half as much
sulphuric acid, answer best, the oxidation being completed by
adding a small proportion of nitric acid largely diluted, and
boiling up with steam. In other instances, treatment with
dichromate improves the product, not so much by simply bleach-
ing as by oxidising and removing the small quantities of malo-
dorous substances present that communicate a foetid or rancid
odour — e.g., kitchen grease, horse grease, &c.
266 OILS, FATS, WAXES, ETC.
Beeswax is frequently bleached by boiling with a weak solu-
tion of potassium dichromate, acidulated with sulphuric acid.
The product is apt to retain chromium compounds, giving it a
greenish hue ; boiling up with oxalic acid solution appears to be
the best mode of dissolving out the chrome and furnishing a
white product. Instead of " chromic liquor," dilute nitric acid
is sometimes employed, taking care not to use too much or of
too great strength, otherwise more or less considerable loss is
apt to occur through oxidation of the wax itself.
Wax thus bleached by oxidising chemicals is generally more
•crystalline than air bleached wax, and consequently not so
well suited for the manufacture of wax candles. According to
Leopold Field, * whilst the solubility in alcohol of air bleached
\vax differs but little from that of the raw wax, that of
-chemically bleached wax is much greater, leading to the idea
that free fatty acids are largely formed during the bleaching
process, giving greater crystallimty.
Instead of potassium dichromate, manganese dioxide has been
employed for bleaching oils, especially palm oil ; the powdered
substance suspended in water is intermixed with the oil by
vigorous agitation, and hydrochloric acid added so as to generate
chlorine, whilst the whole is heated by blowing in steam. The
only advantage of the process seems to be the lessened cost,
against which several other inconveniences must be set off, the
action being far less regular. The same remark applies to the
process formerly used to some extent where manganese dioxide
and sulphuric acid were employed.
Chlorine Processes. — Chlorine evolved from substances other
than potassium dichromate and hydrochloric acid is sometimes
-employed as a bleaching agent ; thus tallow may be bleached by
boiling it on a solution of bleaching powder or potassium chlorate
to which hydrochloric or sulphuric acid is added; about 2 to 2 '5
Ibs. of chlorate per ton usually suffices. In all such processes,
when the fat is intended for soapmaking, excess of chlorine is
apt to produce a worse result than none at all so far as colour
is concerned (leaving deodorising out of the question) ; for if the
fatty glycerides themselves are sensibly attacked by the chlorine
after the colouring matters have been destroyed, the resulting
soap is apt to " work foxy "• — i.e., either to become brown in the
pan during boiling, or to darken in colour subsequently when
cut up into bars. On the other hand, the unpleasant odour of
rancid tallow and grease from tainted or putrid carcases, tannery
refuse, and suchlike materials is apt to be communicated in some
degree to the resulting soap unless the grease is previously
deodorised by chlorine, etc. In many cases a great improvement
in odour may be brought about by simply blowing steam through
* Journ. Soc. Arts, xxxi., p. 836.
CHLORINE PROCESSES. 267
the melted grease for some time, the volatile evil-scented matters
present being thus largely expelled.
With rank fish oils larger proportions of bleaching powder are
requisite up to 1 per cent, and upwards, with an equivalent
quantity of sulphuric acid ; the bleaching powder is made into
a milk with water and well intermixed with the oil, which is
slightly heated by blowing in a little steam ; the acid diluted
w^ith several times its volume of water is then run in with
vigorous agitation. Finally, steam is blown through and the
whole allowed to rest and subside.
Chlorine bleaches wax readily, but chlorosubstitution products
are apt to be formed, so that if the bleached wax is used for
making tapers or candles, hydrochloric acid vapours are evolved
when these are burnt, causing considerable annoyance.*
Cotton seed oil in the raw state contains a peculiar colouring
matter capable of being dissolved out along with resinous matters
by agitation with aqueous solutions of caustic alkalies (p. 260).
Sometimes this purification is only partly carried out, the
residual colouring matter being destroyed by boiling with a dilute
solution of bleaching powder and treatment with dilute sul-
phuric acid. The oils thus more or less completely refined and
decolorised by chemicals are, as a rule, only used for soapmaking
and similar technical purposes ; whereas those completely refined
by soda alone are used as edible oils, being largely used for
cooking purposes, and to a great extent intermixed with olive
and other high-priced "salad" oils. As a rule each oil refiner-
has his own particular special methods of effecting the final
clarification and finish of such superior products, which are looked
upon as valuable trade secrets.
Dark coloured soaps are sometimes bleached more or less com-
pletely by intermixing with the hot curd freed from ley, a solution
of " chloride of soda " (bleaching powder made into a cream and
treated with enough carbonate or silicate of soda to remove all
lime from solution). This may be effected in the pan itself, but
is best done by crutching the liquid into the soap in the frame
(A. Watt): the precipitated carbonate or silicate of lime need
not be previously removed. If made from coarse rank " goods,"
the soap will be largely deodorised by the process.
Peroxide of Hydrogen Process. — The bleaching action of
peroxide of hydrogen on certain forms of organic colouring
matters has long been known and utilised in certain cases where
the cost was not prohibitive — e.g., in the manufacture of various
*The important chemical discovery that "electropositive" hydrogen
could be replaced in organic compounds by highly "electronegative" chlorine
without materially altering the character of the substance affected was first
made in consequence of investigations carried out by Gay Lussac in order
to elucidate the cause of this occurrence in the reception rooms of the
Emperor Napoleon I., where wax candles were largely burnt.
268 OILS, FATS, WAXES, ETC.
high-priced toilet fluids for converting dark hair into substances
of golden hue, or even bleaching completely white. Notwith-
standing improvements whereby the cost of manufacture of per-
oxide of hydrogen is greatly reduced, this substance is still too
expensive for use on the large scale for low-priced oils, &c.,
although in many cases it is well fitted for the purpose. Drying
oils required for artists' varnishes are sometimes bleached by
floating them in a thin layer on the surface of hydrogen peroxide
dissolved in water, the whole being warmed and if possible
exposed to sunlight to facilitate the operation. By shaking up
repeatedly in a closed vessel Avith about ^ part of a 10 per cent,
solution of peroxide of hydrogen most oils can be rapidly
bleached, or at least greatly lightened in colour.
Wax Bleaching by Exposure to Air.— The effect of light
and air 011 beeswax in removing the natural yellowish tinge is
utilised thus : The wax is first melted and boiled up with water
acidulated with a small quantity of sulphuric acid (about 1 part
by weight of oil of vitriol per 1000 of wax); impurities are thus
washed out, and a clear bright melted wax obtained. This is
then run from a sort of cullender pierced with holes on to a
drum half immersed in a tank of cold water ; as the streams of
fluid wax come in contact with the cool wet surface they solidify
into thin ribbons which are scraped off the drum after they have
passed down under the water so as to complete their solidification.
.Filially, the ribbons are spread out in thin layers on canvas
sheeting, and placed in the open air so as to be exposed to the
sun and air. After a time, the partially bleached ribbons are
remelted and again cast into ribbons, and exposed for a further
period, the whole operation lasting several weeks according to the
weather and the nature of the wax, some kinds yielding much
more rapidly to atmospheric oxidation than others. Usually
only the outer portions of the ribbons become bleached, the action
not penetrating far into the interior ; so that to expose the whole
equally to light and moisture, the mass requires to be turned
over from time to time and sprinkled with water ; obviously the
thinner the ribbons are, the better.
In the purification of Japanese wax a very similar process
is adopted ; the crude wax as obtained from the dried berries
of the Rhus succedanea, is melted and strained, dripping into
water kept agitated so that it solidifies in thin flakes ; these
are then exposed to sun and air in trays, being now and then
sprinkled with water and turned over ; the vegetable colouring
matter present in the crude wax is thus readily blanched, an
almost white product being obtained. In the case of some
varieties of beeswax this result cannot be so readily secured, the
colour sometimes not yielding at all readily to atmospheric
influences. Addition of a small quantity of fatty matter to
beeswax often facilitates the bleaching action of the atmosphere
WAX BLEACHING.
269
under the influence of sunlight ; according to some authorities
the quality of the wax is not improved thereby, whilst the
presence of glycerides is usually regarded as proof of adulter-
ation ; on the other hand, A. & P. Buisine (infra] state that
the addition of 3 to 5 per cent, of tallow is universal amongst
French airbleachers in order to prevent the product becoming
brittle, and is not regarded at all as an adulteration. A small
percentage of oil of turpentine is sometimes used instead of fatty
matter ; the volatile hydrocarbon mostly escapes during the
process by exposure to air ; but a small quantity becomes
resinised by oxidation and retained by the wax ; probably this
oxidation gives rise to peroxide of hydrogen in minute quantity
which assists the bleaching action.
According to A. & P. Buisine * the chemical bleaching of
beeswax is always accompanied by an increase in the total
acid number, and a diminution in the iodine number, indicating
the direct addition of oxygen to the uiisaturated acids present;
thus the following figures wrere obtained in a long series of
experiments : —
Iodine absorbed
by 100 parts of wax.
Total acid
number.
Pure yellow waxes, ....
Pure airbleached waxes,
10 -87 to 11-23
6 to 7
91 to 95
93 to 100
Airbleached, with addition of 3 to 5 per
cent, of tallow, .....
6 to 7
105 to 115
Airbleached with addition of 5 per cent,
spirit of turpentine, ....
Bleached by hydrogen dioxide,
Decolorised by permanganate,
Decolorised by bichromate, .
6-78
6'26
2-64 to 5-80
1-08 to 7-94
100-4
98-4
92-2 to 103-3
98 -9 to 107 '7
On the other hand, decolorisation "by means of animal char-
coal caused no marked alteration in either the total acid number
or the iodine absorption.
An indirect method of bleaching by means of air is sometimes
practised, especially with linseed oil; the oil to be treated is
agitated at intervals with ferrous sulphate solution ; this has a
tendency to peroxidise by absorption of oxygen from the air,
whilst the resulting ferric compound parts with oxygen to the
colouring matter, oxidising the latter and blanching it, whilst
becoming itself again reduced to the ferrous state ; and so on
continuously.
* Bulletin Soc. Chim., Paris, 1890, iv., p. 465.
270 OILS, FATS, WAXES, ETC.
CHAPTER XII.
RECOVERY OF GREASE FROM "SUDS," &c.
IN certain textile industries, more especially the woollen manufac-
ture, and to a somewhat lesser extent the silk and cotton
industries, the materials are treated at particular stages of the
process with soap liquors for the purpose of washing out impuri-
ties of various kinds ; whilst in various dyeing operations soaping
is also resorted to for the purpose of clearing off superfluous
dyestuff, cleansing the undyed portions, and so on. Formerly,
the " soap suds " thus produced were thrown away by running
into the nearest available stream, &c.; but the great amount of
river pollution thus brought about has in many cases rendered
it imperative that at least some amount of purification of such
liquors should be effected before they are thus run away ;
whilst the value of the fatty matters saved by adopting proper
processes for such purification, often renders it profitable to
employ such methods, even when so doing is not otherwise
compulsory.
The methods adopted necessarily vary to some extent with the
nature of the materials to be dealt with ; in cases where coloured
waste liquors from dyeworks, (fee., constitute the great bulk of
the substance to be treated, the cheapest and most satisfactory
methods appear to be modifications of the precipitation processes
employed in similarly dealing with sewage ; thus by adding a
small proportion of milk of lime to the liquors, and simultane-
ously running in a solution of crude aluminium sulphate,* the
alumina and ferric oxide precipitated by the lime unite with the
colouring matters forming " lakes," which ultimately subside by
gravitation in suitable settling tanks, carrying down mechanically
with them various other impurities (albuminoid matters, fatty
acids, &c.), so as finally to yield a clear almost colourless effluent
containing in solution only non-precipitable matters such as
alkaline salts, (fee. The " sludge " thus resulting is usually of but
little value, even for manure. When, however, soap suds con-
stitute a sufficiently large proportion of the waste liquors, it is
preferable to collect and treat these separately so as to recover
* Aluminoferric cake containing somewhat large amounts of iron,,
chiefly obtained from the mother liquors of purer aluminium sulphate made
by treating bauxite, clay, &c. , with sulphuric acid.
YORKSHIRE GREASE. 271
the grease, the slightly acid watery liquors left after this opera-
tion being either run away directly, or, preferably, admixed
with the coloured waste liquors, and the whole treated together
as above described ; a little more lime is requisite in this case
to neutralise the free acid contained in the grease recovery
liquors, which must be done before the alumina can be effectively
precipitated from the sulphate. The precise details of the
method of working necessarily vary in each instance ; but it is
within the author's knowledge that processes substantially of the
character described can be so worked as to answer the purpose in
most satisfactory fashion, especially when carefully carried out
under pressure of an impending injunction.
Two methods of treating soap suds are thus applicable ; in one
the soap is made to react upon a lime compound such as thin milk
of lime or solution of calcium chloride so as to form insoluble lime
soaps by double decomposition; these are collected by subsidence
and nitration (the more or less purified liquor being run away),
and subsequently decomposed by sulphuric or hydrochloric acid
so as to liberate the fatty acids, thus obtaining a more or less,
impure grease ; after hot pressing or filtration the fatty acids
are obtained separate from the solid matters admixed with
them, and may be utilised in the production of rough soap, cart
grease, &c., or submitted to distillation with superheated steam,
according to their nature and degree of impurity. This lime
process is more especially applicable to comparatively dilute
suds, &c., where the object is rather to get rid in some way or
other of a dirty waste liquor which, from the circumstances of the
case, must be somewhat purified before discharging, than to work
a recovery process profitable in itself. When, however, the soap
liquors are more concentrated, the other method is preferable,
consisting of simple acidulation of the suds with sulphuric * or
hydrochloric acid ; the fatty acids thus liberated would naturally
float up as a sort of greasy scum, were it not for the presence of
other heavier suspended matters which, in most cases, and more
especially with wool scouring soap suds, render the total preci-
pitate ("magma" or "coagulate") somewhat heavier than the
watery fluid, causing it to sink. This process is more especially
employed in the recovery of " Wakefield fat" or "Yorkshire
grease," which essentially consists not only of free fatty acids
derived from soap, but also of wool grease contained in the raw
wool, and other oleaginous matters «used in the spinning and
weaving processes.
In the English woollen industry, the method of cleansing wool
usually adopted essentially consists in scouring with soft soap, or
* Chamber acid suffices, or acid from the Glover tower, rectified oil of
vitriol being too costly, except in cases where the less cost of carriage of the
smaller bulk outweighs the increased price through cost of further concen-
tration.
272 OILS, FATS, WAXES, ETC.
other soaps of special character ; during the further processes
through which the wool is put before it is finally converted
into woven cloth, soap and oil are tolerably freely used in the
spinning, fulling, and milling of the fibre, yarn, and cloth.
The soap suds and similar waste liquors produced in these
various operations are collected in large tanks or reservoirs,
holding several thousand gallons, and acidulated with a mineral
acid — e.g., B.O. V. (brown oil of vitriol) ; after agitation and
subsequent standing for some hours, a fatty " magma " or
coagulate deposits at the bottom of the tank ; the supernatant
watery fluid (which should be slightly acid, otherwise the whole
of the soap has not been decomposed) is then run off, and the
tank filled up with fresh suds and acidulated as before, excepting
that somewhat less acid is now requisite, owing to the smaller
quantity of suds treated, the tank having been partly filled with
magma and watery fluid (with a tank 6 feet deep, the magma,
etc., usually fills up 15 or 18 inches). The process is again
repeated, the magma (known locally in Yorkshire as " sake ")
being ultimately thrown on filter beds, where most of the
remaining watery liquor separates, and then subjected to
pressure in bagging ; at first the pressure is very gently applied,
so as to squeeze out water only, but subsequently it is increased
and heat applied (hot press), so as to filter the fused mass
through the bagging, furnishing a dark sticky grease, and a
residual " sudcake " available as manure. This grease is what
is properly called " Yorkshire grease ;" but similar recovered
products ("Fuller's grease") obtained by treating the soap suds
produced in other industries where scouring with soap is largely
employed, are sometimes included in the term (cotton industry,
silk manufacture, dyeing, &c.) Genuine Yorkshire grease from
wool scouring essentially consists of the free fatty acids derived
from the soap used, the wool grease contained in the wool,
and such unsaponified oil and mineral hydrocarbons, &c., as
may have been used in the spinning and weaving operations
for the purpose of oiling or sizing the yarn, &c. ; whilst
analogous greases from other sources are more or less different
as regards the nature of the substances present other than free
fatty acids.
According to Lewkowitsch,* Yorkshire grease rarely, if ever,
contains unsaponified glycerides, any glyceridic oils used in the
spinning process becoming saponified during the after processes
of washing, tfcc. ; so that the essential organic constituents are —
(1) free fatty acids, partly derived from the wool grease, but
chiefly from the soaps used in washing ; (2) cholesterol and
isocholesterol ethers, and similar derivatives of other high
alcohols — e.g., cetylic and cerylic alcohols ; (3) free alcohols
(cholesterol, &c.), either naturally contained in wool grease, or
* Journ. Soc. Chem. Ind., 1892, p. 134.
ANALYSIS OF YORKSHIRE GREASE. 273
produced during scouring by the partial saponification of their
compound ethers ; together with hydrocarbons contained in the
oils used for greasing during spinning, &c.
Analysis of Yorkshire Grease. — The free acids are usually
determined by titration in the usual way (p. 116), their average
molecular weight being assumed to be some constant value — e.g.,
282 = oleic acid ; inasmuch, however, as they usually contain a
notable amount of acids of much higher molecular weight, derived
from the wool grease, this mode of calculation is apt to give too
low a result. In order to obtain a more exact valuation, the
alcoholic soap solution thus formed may be diluted with water,
and shaken with ether or light petroleum spirit, so as to dissolve
out all other constituents (or better, evaporated to dryness and
exhausted with ether or, preferably, light petroleum spirit,
p. 119, as the ethereal and watery fluids are apt to form frothy
emulsions, not readily separating into two liquids) ; the weight of
the free fatty acids insoluble in water is then determined by
acidulation, etc., as in Hehner's process (p. 166 ); by titrating
these with alkali, and subtracting the amount neutralised from
that neutralised during the first titration, the alkali equivalent
to the soluble acids may be deduced (p. 168); so that these latter
may be calculated, assuming an average molecular weight — e.g.,
102 = valeric acid, C5H10O2.
The sum of the cholesterol ethers, &c., and unsaponifiable
matters is obtained by weighing the ether or petroleum spirit
extract ; \vhen only an approximately exact result is required,
this may be got by difference, subtracting the fatty acids found
by titration (together with water, mineral matters, &c.) from 100
(vide infra}. The cholesterol ethers saponify only with great
difficulty ; the best mode of procedure is to heat under pressure
with excess of double-normal alcoholic potash (in a tightly
closed vessel heated to 100°) : in this way a measure of the
amount of compound ethers present is obtained,* so that by
again assuming a mean molecular weight (e.g., that of cholesterol
stearate, C.>6H43 . O . C18H35O = 638), their amount may be calcu-
lated. A preferable method, however, is to separate the soaps
thus formed as before by means of ether, &c., dissolving out the
alcohols formed by saponification (or pre-existing in the grease)
and hydrocarbons, <fcc. ; the fatty acids contained in the soaps
are separated and weighed, and the alcohols, &c., obtained by
evaporating off the solvent. The acetyl test (p. 186) applied to
this residue allows an estimation to be made of the alcoholiform
constituents, again assuming a mean molecular weight — e.g., that
of cholesterol, C.,6H44O = 372, whence the amount of hydrocarbons
present is known by difference.
*If substances analogous to stearolactone (p. 170) are present, or organic
anhydrides (possibly present in distilled grease), alkali is also neutralised by
them during; this operation.
18
274 OILS, FATS, WAXES, ETC.
The figures thus obtained will then come out as follows : —
FIRST TREATMENT.
A B
Free fatty acids insoluble in water (weighed).
,, ,, ,, soluble in water (calculated
from difference of titration).
SECOND TREATMENT OF B.
Compound ethers, alcohols,
and hydrocarbons
(weighed).
Fatty acids contained in
compound ethers
(weighed).
D
Alcohols (pre-existing and formed by saponi-
fication) and hydrocarbons (weighed).
The former calculated as CgeH^O from
the acetyl test ; the latter by subtracting
the quantity thus found from D.
Since water is taken up during the saponification of the com-
pound ethers, the sum of the organic constituents thus reckoned
should exceed 100, as in the parallel case of soap when the total
alkali and fatty acids present are determined (Chap, xxi.)
For certain purposes, more especially the preparation of
"lanolin" or similar cholesterol products of more or less
purity, the proportion of alcohols present regulates the value
of the material more than does the amount of fatty acids.
The presence of hydrocarbons (whether intentionally added as
ingredients in the oiling process during spinning, <fcc., or due to
adulteration of the oils thus used with petroleum products or
rosin oils, or formed during distillation of grease, the "oleine"
thereby obtained, p. 279, being used for wool-oiling) considerably
depreciates the value of the material for these purposes: in
many cases the presence of such substances in the extract D
obtained as above can be indicated, and the amounts roughly
judged, by treating this residue with alcohol or glacial acetic
acid, in which solvents the hydrocarbons are only sparingly
soluble.
For many purposes a less troublesome method of analysis
suffices ; thus Lewkowitsch (loc. cit. supra) recommends the
following process for the examination of Yorkshire grease : —
About 5 grammes are titrated with alcohol and seminormal
alkali ; another portion is similarly titrated by boiling with
excess of alkali (i.e., the "free acid number" and the "total
acid numbers" are determined); the difference between these
titrations gives a measure of the compound ethers, glycerides,
and other saponifiable matters present. By means of ether
(preferably, light petroleum spirit, p. 119) the " unsaponifiable
ANALYSIS OF YORKSHIRE GREASE. £75
matters" (alcohols, hydrocarbons, £c.) are dissolved out and
weighed, whilst the " insoluble fatty acids " and " volatile " acids
are determined by the Hehner and lleichert-Meissl processes
(pp. 166, 174). Thus a sample of Yorkshire grease yielded the
following results : —
Unsapotritiable matters (weighed), . . . . 36*47 per cent.
Free fatty acids ; insoluble (weighed — Hehner
number), 20 '22 ,,
Free volatile acids (calculated as CSH10O2), . . 1'2S „
Combined fatty acids (calculated from difference of
titrations, assuming the mean molecular weight
= 327-5), 48-47
106-44
The excess of 6 '44 per cent, thus found is partly due to the
water taken up during hydrolysis of the compound ethers ; pro-
bably also the assumed mean molecular weight of the combined
fatty acids (327 '5) is somewhat too high. On the other hand the
value 282 (oleic acid) would be too low.
In the determination of the unsaponifiable matters present
"W. Mansbridge * recommends in place of ether the use of light
petroleum spirit (commercial benzoline redistilled, collecting the
part distilling at about 110° F. = 43° C.); the grease is saponified
with excess of alcoholic potash (under pressure if requisite), and
the product decomposed with mineral acid, whereby a mixture of
free fatty acids and unsaponifiable matters is obtained. Of this
a portion sufficient to yield about O5 gramme of unsaponifiable
matter is dissolved in 50 c.c. of methylated spirit saturated
with benzoline distillate, and 50 c.c. of that distillate added; the
whole is heated just to boiling, directly neutralised with semi-
normal potash, and then transferred to a separating funnel,
where the hot benzoline solution of unsaponifiable matter, and
the alcoholic soap solution, separate from one another rapidly.
The alcoholic soap solution is run off, and 50 c.c. of water at
100° F. (37°'8C.) added, and the whole agitated to wash out any
soap dissolved by the benzoline. After separating by standing,
the watery fluid is run off, and replaced by 40 c.c. of warm 70
per cent, alcohol : this when agitated with the benzoline removes
the last traces of dissolved soap. The alcoholic soap solution
first run off is agitated a second time with benzoline, and the
benzoline solution purified as before : for some kinds of grease
more than two such extractions are requisite, but in general two
suffice.
The percentage of unsaponifiable matters (including choles-
terol, &c., produced by decomposition of cholesterol ethers) thus
deduced is not far removed from, but is usually somewhat less
* C.'um'x.tl News, 27th May, 1892.
276
OILS, FATS, WAXES, ETC.
than, that calculated by assuming that the fatty acids present (free
and combined as cholesterol ethers, *fcc.) have the mean molecular
weight 282 (oleic acid), and subtracting their weight (together
with water, suspended matters, &c.) from 100. Thus Mansbridge
gives the following comparisons : —
Pure woolfat, ....
,, ,, another sample,
West of England recovered grease,
West of England recovered grease,
another sample, ....
Distilled woolfat, ....
Oleine from distilled woolfat, .
Oleine from distilled \voolfat,
another sample, ....
Black srease recovered from shoddy
scourings, .....
Unsaponifiable Matters.
By extraction
as above.
By titration,
&c.
{
29-05
29-25
39-36
41-70
41 70
46-79
(
21 -55
( 23-16
i
21-05
j 23-16
|
22-81
23-63
1
52-25
I 48-64
1
51-90
I 48-64
r
44-35
44-25
44-31
{
50-25
50-35
47-13
(
22-61
°5"55
1
22*72
According to A. Hess * the difference between the amounts of
unsaponifiable matters deduced in these two ways gives a rough
valuation of the cholesteroid bodies present, the proportion of
these latter being approximately deducible by multiplying the
difference by 10.
The following analyses of Yorkshire grease (method of analysis
not stated) are given by G. H. Hurst f as fairly typical : —
Sp. gr. at 15°-5C., .
J» 55 98 ,,
Water, .
Fatty acid,
Neutral oil, .
Unsaponifiable oil, .
Ash,
1
2
3
4
:
0-9391
0-8900
0-9417
0-8952
...
0-9570
0-8720
.
0-98
18-61
68-62
11-68
O'll
1-53
24-25
58-25
15-83
0 14
1-21
24-15
30-02
44-44
0-18
0-94
26-43
16-86
55-77
trace
100-00
100-00
100-00
100-00
* Jaurn. Soc. Chnn. Iml., 1892, p. 144.
t Journ. Soc. Chem. 2nd., 1889, p. 90.
DISTILLED GREASE. 277
Thus, the higher the density, the greater the percentage of
imsaponifiable oil. Such greases generally melt at near 44° C. ;
they can be saponified with alkalies, but only imperfectly ; the
flashing point is usually near 220° C. (p. 128).
Distilled Grease. — Yorkshire grease from wool, and analo-
gous recovered greases from other sources, are rarely sufficiently
free from odour and otherwise of general good character, to
enable them to ba directly used for anything but the coarsest
purposes — e.g., cart grease, and similar rough lubricating
materials, such as that required for the hot axles of tin plate
rolling machines. When subjected to distillation in cast iron*
stills of about 1,000 gallons capacity, holding about 4 tons of
grease, a variety of products are obtained, to some extent varying
with the quality and nature of the grease. The stills are first
heated for 10 to 16 hours with free fire to drive off water, and
then for 20 to 24 hours more with superheated steam, during
which time a pale yellow product comes over, known as " first
distilled grease," sometimes preceded by a lighter " spirit oil/'
sometimes not. After the "first distilled grease," "green oil"
comes over, sometimes used for coarse lubricating greases, but
more often put back into the still and worked over along with
the next batch. Finally, the distillate comes over as a thick oil,
when the operation is regarded as finished ; the fires are drawn,
the superheated steam turned off, and the pitch run out of the
still : 100 parts of Yorkshire grease thus treated gave —
Pitch, . . 14-1 parts.
Green oil, . . . . 15 "5 ,,
First distilled grease, . . . 45*5 ,,
Spirit oil, .... 4'1 ,,
Water and loss, . . . 20'S ,,
100-0
The pitch thus obtained forms a useful lubricant for the necks of
hot rollers.
The " first distilled grease " is sometimes allowed to " seed " or
crystallise in the usual way (Chap, xvi.), and then pressed in a
hydraulic press, so as to obtain a liquid " oleine " and a solid
" stearine '; in. about the relative proportions, 2 to 1 ; the oleine
that exudes spontaneously from the crystallised cake before
pressing, is sometimes collected apart and designated "No. 1 oil."
Or the grease is distilled a second time, so as to obtain about
* Cast iron is much less rapidly corroded by the fatty acids than wrought
iron— ride G. H. Hurst, loc. cit. sttpra.
278 OILS, FATS, WAXES, ETC.
96 per cent, of " second distilled grease," and 4 per cent, of
" soft pitch."
The " spirit oil," as it first runs from the stills, is pale yellow
in colour, but darkens on keeping, probably by oxidation, like the
somewhat analogous oils obtained on the redistillation of bone
tar and other products of destructive distillation ; it contains a
small quantity of free fatty acids, equivalent to 4 or 5 per cent,
of oleic acid; on redistillation, it begins to boil at near 150° C.,
about two-thirds distilling below 240°, and seven-eighths below
320°. It finds a limited use in making black varnish. Of what
constituent of the original grease it is a product of decomposition
by heat, is not known certainly ; possibly it is derived from
cholesterol, ttc., but as hydrocarbons are always formed in small
quantity in the redistillation of " red oils " (crude oleic acid) and
similar substances containing little or no constituents analogous
to cholesterol, it is more probable that it comes from the decom-
position of the oleic acid present.
" Distilled grease " is of pale yellow colour, and of granular
texture ; two samples gave the following numbers (Hurst) : —
First Distilled Grease.
Second Distilled Grease.
Water,
Free acid, ....
Uusapornfiable matter, .
Neutral oil, ....
0-98
63-12
12-88
23-02
1-04
66-f>6
1324
19-16
10000
100-00
Lewkowitsch found a considerably larger percentage of hydro-
carbons in a sample of distilled grease examined by him, viz. : —
Free fatty acids (molecular weight = 286), . . 54-91 per cent.
Combined fatty acids (molecular weight = 327'5),. 7 "02 ,,
,Unsaponifiable matters, . . . . .38*80 ,,
100-73
The combined fatty acids would represent about 11-28 per cent,
of compound ethers ("neutral fat"), leaving 34-54 per cent, of
hydrocarbons.
The " stearine " obtained from distilled grease by pressure is
a hard pale yellow greasy solid ; that from the " first distilled
grease" is darker than that from " second distilled grease," but
vhas usually a slightly higher melting point. Apparently the
fatty acids present have a higher molecular weight than stearic
ENGINE WASTE GREASE, FULLERS GREASE.
279
acid, inasmuch as the free acid found on analysis, when cal-
culated as stearic acid and added to the other constituents, gives
a total considerably under 100 ( Hurst). * Thus —
Stearin e.
From First Distilled
Grease.
From Second Distilled
Grease.
Sp. Gr. at 15° -5, ....
98, ....
0-9044
0-9193
0-836
Water,
Free acid calculated as stearic acid,
Unsaponifiable oil,
Neutral oil,
1-48
76-3
0-4
7-7
0-6
88-6
0-49
2-11
85-88
91-80
Melting point, ....
Solidifying point,
57° (134°F.)
53-5 (128°F.)
48° (118° P.)
45°(113°F.)
The oleine simultaneously obtained is pale when fresh, but
gradually darkens, probably owing to the presence of iron
derived from the press or the tanks, in which it is stored. It is
generally known in the district of production as " wool oil,"
because it is chiefly used for oiling woollen yarns, £c.; lubricating
greases and soap are sometimes prepared from it ; but for the
latter purpose it is not at all well suited on account of the large
proportion of unsaponifiable matters. It varies much in com-
position, even when from the same maker, on account of the
varying composition of the Yorkshire grease originally employed,
the neutral oil amounting to between 0 and 28 per cent., and the
unsaponifiable oil to between 10 and 38, whilst the free acid
(calculated as oleic acid) constitutes 53 to 65 per cent. The
Hashing point usually lies between 322° F. and 342° F. (Hurst).
Engine Waste Grease and Fuller's Grease. — The grease
recovered from greasy engine waste (p. 236) is closely akin to
that obtained from soap suds ; but owing to the large use of
hydrocarbons as ingredients in lubricating oils at the present
day, it is usually much less valuable, the yield of solid "stearine"
being but small, and the "oleine" containing large quantities
of unsaponifiable hydrocarbons. When the spindles, &c., are
lubricated with tolerably pure vegetable oils or with sperm
oil, &c., a much better form of grease results ; but this is
comparatively rare.
Grease recovered from silk soap suds and soap baths from
cotton dyeing works, &c., mostly consists of free fatty acids with
"" The presence of stearolactone (p. 170) might possibly explain thfe
apparent deficiency in free acids.
280 OILS, FATS, WAXES, ETC.
but little unsaponifiable matter, and is often clean enough to be
used directly for soapmaking. Its commercial valuation for such
purposes is generally effected by determining the percentage of
water present (p. 122), and of matters insoluble in alcohol (un-
saponifiable matters), subtracting the sum from 100, and reckoning
the difference as available fatty acids. When too dirty for use
in even the coarsest soap, such grease is either directly utilised
for lubricating materials of the roughest kind, or is distilled
by means of superheated steam, and the distillate pressed for
stearine and oleine.
CLASSIFICATION OF OILS, ETC. 281
5. Classification and Uses of Fixed Oils, Fats,
Waxes, &c.; Adulterations.
CHAPTER XIII.
CLASSIFICATION.
In accordance with their ordinary physical texture, sources
(whether animal or vegetable), and essential chemical nature,
the fixed oils, fats, butters, and waxes, <fcc., may be conveniently
divided into twelve classes, falling into two principal divisions,
according as the main components are of glyceridic or non-
glyceridic nature.
DIVISION I. — ESSENTIALLY GLYCERIDIC.
A . Fluid at Ordinary Temperatures : —
1. Non-drying Oils —
Vegetable —
(1) Olive (almond) class.
(2) Rape (colza) class.
(3) Ricinoleic (castor) class.
Animal —
(4) Lard oil class.
2. Intermediate : Drying Qualities possessed to a limited
extent : —
Vegetable —
(5) Cotton (sesame) class.
Animal —
(6) Train, fish, and liver class.
3. Drying Oils : well marked Drying Qualities : —
Vegetable —
(7) Linseed class.
382 OILS, FATS, WAXES, ETC.
B. Solid or Semisolid at Ordinary Temperatures : —
Vegetable —
(8) Palm butter, and Japanese wax class.
Animal —
(9) Tallow, lard, and cow's butter class.
DIVISION II. — ESSENTIALLY NON-GLYCERIDIC.
A. Fluid at Ordinary Temperatures : —
Animal —
(10) Sperm oil class.
B. Solid or Semisolid at Ordinary Temperatures : —
Vegetable —
(11) Carnauba wax class.
Animal —
(12) Beeswax and spermaceti class.
CLASS I.— OLIVE (ALMOND) CLASS.
A large number of oils are known completely fluid at ordinary
temperatures and not congealing until greatly chilled, consisting
chiefly of olein with smaller quantities of more solid glycerides
(myricin, palmitin, stearin, arachin, &c. ), and in some cases small
admixtures of glycerides of other kinds ; as a rule, however,
glycerides of the "drying oil" division are either absent
altogether, or only present in very small quantities, so that oils
of this class are practically non-drying. The presence of the
other constituents raises the relative density somewhat above
that of pure olein (near 0-905 at 15°), usually to between -913
and '92-1 • and at the same time tends to dimmish the iodine
number below 86 -2 per cent., the calculated value for pure olein
(p. 180), excepting in those cases where a notable admixture
•of less saturated glycerides is present, when the superior iodine
absorbing power of these ingredients slightly raises the value
instead of lowering it. The calculated saponification equivalent
of pure olein is 294'7 (p. 158) ; that of an oil of this kind
generally differs but little therefrom, being a little higher or a
little lower, according as the other constituents have mean
equivalent weights above or below this value. The proportion
of glycerides other than those of oleic and the solid fatty acids
is not large enough to interfere with the production of a tolerably
hard solid elaidin with nitrous acid (p. 137), nor to cause that
heat evolution on mixture with sulphuric acid to be large
(p. 147).
The chief oils of commercial or local importance belonging to
VEGETABLE OLEINES. 283
this class that have been investigated to any extent are as
follows : — .
Name of Oil. Source.
Almond oil (sweet), . . Amyydalus communis (Prunus amyg-
dalux), var. dulcis.
,, var. amara.
(bitter),
Arachis oil (grouudimt oil),
Beechmast oil,
Ben oil, . . .
Hazelnut oil, .
Olive oil,
Araclii* hypogcea.
Fagus sylvatica.
Morinrja pterygosperma ; M. apt era
(Guilandia moringa).
Corylus arellana.
Olea Europcea sylvestris : 0. E. satira.
Plum, peach, cherry, and ) P™nu* domestica ; P. persica
apricot kernel oils, . . £ , arme^aca * „ P' «™
P. ongandaca ; P. serotina.
Tea seed oil,
Camellia theifera • C. oleifera :
C. drupifera.
Besides these, however, a large number of oils are in use to
varying extents in different countries for edible purposes, burning,
.anointing, <fcc., many of which agree in their general physical
characters with the above, more especially in being practically
non-drying in character and only solidifying at low temperatures,
And hence presumably consisting essentially of olein ; the
chemical examination of most of these, however, has not yet
been undertaken ; and as yet they are but little exported, and
consequently have not found their way into general trade in any
large quantities (vide pp. 287, 296).
Vegetable Expression Oleines. — Semisolid vegetable tal-
lows and butters, when subjected to cold pressure, yield a solid
mass of higher fusing point together with a comparatively fluid
oil or oleine ; in certain cases, more- especially for the production
of the higher fatty acids for candle making, this treatment is
resorted to in order to partially separate the more fluid glycerides
from the others. Cokernut and palm kernel butters when thus
treated yield fluid oleines, solidifying a few degrees above 0° ;
these consist partly of oleic glyceride, partly of the glycerides of
the acetic series of lower molecular weight contained in the
original butters ; and, in consequence of the presence of these
latter in considerable quantity, possess a somewhat different
composition from ordinary oils of the olive class — e.g., the iodine
.absorption is much lower (often below 30 to 40) owing to the
relatively small amount of oleic glyceride present ; and similarly,
the heat development on mixture with sulphuric acid is below
that observed with olive oil (cokernut oleine = 26° to 27° ; olive
oil = 41° to 43° — A. H. Allen). On account of the absence of
linolic and similar glycerides, these products are almost com-
pletely non-drying.
284
OILS, FATS, WAXES, ETC.
CLASS II.— RAPE (COLZA) CLASS.
The characteristic property of this class of oils is that of
possessing a much higher saponification equivalent than the oils
of Classes I. and III. in virtue of the presence of considerable
quantities of a higher homologue of oleic acid — viz., erucic acid,
(X2H4.2O0, crystallisable and melting at 34°. In the case of
colza oil another acid, rapic acid, C1SH0)4O.}, isomeric with ricin-
oleic acid, has been stated to be also present in considerable
quantity (p. 41). More precise information, however, is decidedly
wanted as regards the constituents not only of the lesser known
members of the group, but also of those most commonly
occurring.
The specific gravity is relatively low, mostly below -918 ; the
.saponification equivalent usually lies between 315 and 325,
whilst the iodine number is between 95 and 105, indicating the
presence of a certain amount of glycerides of linolic character,*
a result also borne out by the possession of some degree of drying
character by the oils themselves, not, however, of a strongly
marked kind.
Oils of this class do not give a particularly solid elaidin re-
action with nitrous acid, buttery masses being usually formed
which often separate on standing into two portions, one solid and
the other liquid.
The principal oils of this class are those undermentioned, but
in all probability many of the lesser known oils are of similar com-
position, judging from their general physical characteristics : —
Name of Oil.
Source
Colza (rape) oil,
Hedge mustard oil (hedge \
radish oil), . . . . J
Mustard oils (black and white ; }
Chinese cabbage oil), . . 1
Different cultivated varieties of
Brasxica campestris.
Raphanus raphaniMrum (Raphanis-
trum arrense).
Sinapis nirjra : S. alba ; and other
species of Sinapis.
Uaphanns Kotivus.
CLASS III.— CASTOR OIL CLASS.
In this class of oils the prevailing glyceride is that of an oxy-
acid, such as ricinoleic acid, which gives to oils of this description
peculiar chemical characteristics. Comparatively few oils besides
castor oil have been sufficiently closely examined to render it
certain that they belong to this class ; but it is highly probable
that several of the lesser known oils used locally for edible
* The calculated value for erucin is 72 '4, that for olein, 86 "2.
ANIMAL NON-DRYING OILS. 285
purposes, or as lamp oils, in different parts of the world, really
consist to a greater or lesser extent of oxy-acid glycerides.
A tolerably high specific gravity, from -950 to -970, is possessed
by oils of this class, and a saponification equivalent of 305 to 315
(calculated value for ricinoleiii = 310-67). The elaidins are soft
and buttery. The following oils appear to contain more or less
considerable proportions of oxy-acid glycerides : —
Name of Oil. Source.
Castor oil, . . . Ricihux communi* (var. minor and major).
C ureas oil (purqueiraoil),. Jatropha curcaa (Curcas purgans).
Grape seed oil, . . . Vitls vinifera.
CLASS IV.— ANIMAL NON-DRYING OILS-
LARD OIL CLASS.
When comparatively solid animal fats are subjected to a
regulated pressure (p. 231), a mechanical separation of the solid
and liquid constituents is effected if the temperature be suitably
adjusted ; the fluid substances thus expressed are, strictly
speaking, the only products to which the term " oleine " is
applicable (besides the analogous fluid constituents of vegetable
oils); but in commercial practice the fluid free fatty acids
separated by similar means from the products of saponification
of such fats, are also designated " oleines," as also are the
analogous fluid acids obtained from steam-distilled fatty acids
from greases of various kinds (p. 110); further, oils treated with
sulphuric acid (Turkey red ohs) are often termed "oleine" in
the cotton dyeing industry. Accordingly, the glyceridic ex-
pression products are more usually spoken of as " oils " (e.g.,
tallow oil) than as oleines ; although, even then, confusion is
not always avoided, since the terms " tallow oil " and " red oil "
are sometimes also applied to the expressed crude oleic acid of
the candle maker.
Products of this class closely resemble vegetable oils of Class I.,
especially when free from any animal or rancid odour betraying
their origin. According to the way in which the expression is
effected (more especially as regards temperature), they contain
varying quantities of the solid constituents (" stearines," chiefly
palmitin and actual stearin — i.e., stearic glyceride) in solution,
but otherwise consist essentially of olein (oleic glyceride). They
usually have a specific gravity of about -915 or -916 at 15°, and
solidify within a few degrees of 0° C. (above or below). With
nitrous acid they form firm solid elaidins ; with sulphuric acid
(Maumene's test) the heat evolution is small, as compared with
most other oils. The chief oils of the class are : —
286
OILS, FATS, WAXES, ETC.
Name of Oil.
Source.
Lard oil, ....
Neat's foot oil, horse foot oil, \
sheep's trotter oil, . . /
Tallow oil, .
Hogs' lard subjected to expression.
The " feet" (hoofs and hocks) of oxen,
horses, and sheep.
Ox and mutton tallow subjected to
expression.
CLASS V.— SESAME OR COTTON SEED CLASS-
VEGETABLE SEMI-DRYING OILS.
The distinctions between this class of oils and those of Classes
I. and VI. are not always very clearly marked, the differences
being rather of degree than of kind, chiefly consisting in the
presence of distinctly larger proportions of glycerides of the
drying class than are present in non-drying oils of Class I.,
although these ingredients are not contained in sufficient
quantity to give true drying qualities, such as are possessed by
oils of Class VI. — i.e., the power of absorbing oxygen from the
air, and becoming a solid varnish-like mass. Accordingly, the
effect of the elaidin test (p. 137) is to form a soft solid mass, far
inferior in hardness and consistency to that furnished by typical
non-drying oils, such as olive or arachis oil, but considerably
more solid in character than the soft nearly fluid products formed
by the true drying oils, such as linseed oil.
In general, the specific gravity at 15° is a little higher than
that of oils of Class I., mostly lying between -923 and -'J35 : and
the iodine absorption is similarly raised considerably above 86*2,
the theoretical value for pure olein. In most cases, solid
glycerides (palmitin, stearin, <tc.) are present to a greater or
lesser extent, together with small quantities of glycerides of oxy-
acids. The following are the best known oils of the class : —
Name of Oil.
Camelina oil (German oil of
sesame or gold of pleasure
oil)
Cotton seed oil,
Cress oil, ....
Madia oil, ....
Maize oil, ....
Niger oil (ramtil oil),
Sesame oil (gingelly oil, til oil,
benne oil), .
Sunflower oil, ....
Source.
Camelina saliva.
Gow/pium herbaccum ; G. hirautum ;
G. barbadense ; G. arboreum ; G.
relirjiosum.
Lepidium sativum.
Madia sativa.
Zea mnis.
Guizotia oltifera.
Sesamum orientale.
Helianthufi annuus ; H. pereniri*.
LESSER KNOWN VEGETABLE OILS. 287
Lesser Known Vegetable Oils. — In addition to the leading
vegetable oils above mentioned belonging to Classes I., II., III.,
and V., a large number of other oils are locally known and used to
a considerable extent in various parts of the world. In most
instances nothing whatever is known as to the chemical constitu-
tion of these substances; judging from their general physical char-
acters they are, as a rule, either nondrying oils of the olive class,
or semidrying oils of the cotton seed type; some, however, in all
probability are more or less akin to rape or to castor oil. Amongst
these lesser known imperfectly drying oils may be mentioned
that derived from the soja bean (Soja hispida or Glycine soja) of
China and Japan, where both the beans themselves and the oil
thence expressed are important articles of food. Recently the
plant has been introduced into Europe ; the seeds yield about a
sixth of their weight of oil by pressure, furnishing an excellent
oilcake for cattle feeding. The oil itself thickens on chilling, and
when exposed to air oxidises somewhat rapidly.
The nuts of the candlenut trees (Aleurites moluccana,A. triloba;
Jatropha moluccanum, Croton moluccanum\ found in the Eastern
Archipelago, Malay, Cochin China and Southern China ; Cali-
fornia, Chili and Venezuela ; Bourbon, Mauritius, Jamaica,.
Polynesia and North Australia) furnish similar oils, chiefly used
for cooking and burning, but sometimes possessing sufficient
drying power to be capable of use for painting purposes in hot
climates. In different countries the oil is known by different
names — e.g., Bankulnut oil, Kekune oil, &c. According to Lach
a sample of candlenut fat fusing at 24° and solidifying at 21°
yielded fatty acids melting at 65° -5 and solidifying at 56° : the
iodine number was 118, indicating the presence of a considerable
proportion of drying oils.
L. Field describes candlenut oil as limpid and sweet, not soli-
difying at 0°, and capable of forming a fine waxy looking soap
by the cold process. It is stated to be well adapted for cloth
dressing and to be largely exported to Europe for soapmakingr
but does not appear to be much used in England for those
purposes. The nuts are extremely hard, so as to be cracked
by ordinary machinery only with difficulty ; when strung on a
twig they can be burnt like a tallow candle, whence the ordinary
name.
The seeds of various species of pine (Pinus sylvestris, P. cibiesy
P. picea furnish by expression or solvents imperfectly drying oils
used to some extent for burning and other purposes ; these vary
in specific gravity from '925 to '931 at 15°, and mostly thicken at
about — 15, solidifying at about — '27°.
Croton oil, from Croton tiglium, is possessed of weak drying
characters, but has a composition differing in many respects from
most of the oils of the nondrying and semidrying classes. The
specific gravity of the fresh oil is '942 at 15°, older oil that has
288 OILS, FATS, WAXES, ETC.
absorbed oxygen from the air being more dense, about .'955 ;
solidification occurs at about - 16°. The oil is strongly purgative
when taken in small doses internally, and vesicatory when applied
to the skin ; it does not form any solid elaidin with nitrous acid.
It mainly consists of glycerides, and on saponification furnishes
stearic, palmitic, myristic, lauric, caproic, valeric, butyric, .acetic,
and formic acids of the acetic family, together with tiglic (methyl
•cro tonic), and crotonic acids of the oleic series. Oleic acid has
been stated to be present by some investigators, and to be absent
by others, a nonvolatile " crotonoleic acid " yielding a barium
salt soluble in alcohol having also been found. The vesicatory
agent is believed to be " crotonol," a semisolid body indicated by
the formula C9HUO2 ; this is not identical with the purgative
principle, the nature of which is uncertain.
An excellent fatty oil is largely used in Morocco, derived from
the Argan tree (Argania sideroxylon, Elwodendron argan, or
Sideroxylon spinosum) : the fruit is fleshy and is eaten greedily
by sheep and goats, cows and camels, but the kernels or stones
are hard and bony, and are consequently rejected by the animals.
These stones are collected and cracked, and the inner white
kernels carefully roasted, ground, and kneaded with a little
warm water, whereby the oil is gradually expelled, more water
being added from time to time, and the mass kneaded until no
more oil exudes. After settling the oil is a clear light brown
iluid, often of somewhat rancid flavour and odour; it is largely
used by the Moors as an edible oil, somewhat cheaper than olive
oil. Somewhat similar oils are obtained from the kernels of the
fruit of titapliylea pinnata (bladdernuts) in Eastern Europe ; the
berries of the dogwood (Cornus sanguined) in Italy, Cashmere,
and Siberia ; the seeds of the spindel tree (Euonymus europoeus)
of Central Europe ; horsechestnuts (^Esculus liippocastanum) ;
and the seeds of Sarcostigma Kleinii (known as Adul or Odal oil
in Southern India), of several Hibiscus species, and of Penta-
clethra macrophylla (Owala oil of the Gaboon, Opochala oil of
Fernando Po).
The Brazil nut or Castanha (BertJiolletia excelsa) of South
America yields a clear yellow bland oil closely resembling that
of almonds, soon becoming rancid ; the edible seeds of the
Telfairia pedata of South-east Africa furnish a similar oil, said
to be equal to the finest olive oil. Pumpkin seed oil (Curcurbita
pepo) is a clear sweet-tasting oil, yellowish or nearly colourless
when obtained by cold pressure, possessed of only faintly marked
drying qualities ; its relative density is '923 at 15° ; at - 15°
it solidifies to a greyish-yellow mass. Similar oils are obtain-
able from the seeds of other curcurbitaceous plants— e.g., the
watermelon (Cucumis citrullus), sweet melon (C. melo), gherkin
(C. sativus), colocynth (C. colocynthis}, Arc. The oil of the
Boma nut (Pycnocoma macrophylla) is sweet and bland, and is
LESSER KNOWN VEGETABLE OILS. 289
much used for cooking by the natives of Central Africa ; that of
the Cashew or Acajou nut (Anacardium occidentals) is similarly
employed in the East and West Indies and the West Coast of
Africa; in the Brazils it has been in use for centuries as an
edible oil ; it is a light yellow sweet-tasting oil much like that of
almonds, of relative density -916. Mango seeds (Mangifera
indica) and pistachio nuts (Pistachio, vera) yield similar oils, as
also do the fruit kernels of BucJianania latifolia, a forest tree
common in Coromandel, Malabar, and Mysore ; the oil from the
last is limpid and of a pale straw colour and is sometimes known
as Chironji oil. Various species of (Enocarpus bear oleaginous
nuts furnishing sweet cooking and eating oils, known in Para as
"coumu oil," resembling olive oil but becoming solid much more
readily 011 chilling ; hickory nuts (Gary a olivceformis), M'poga
nuts (common in the Gaboon), breadnuts (OmpJialea diandra
and 0. triandra — St. Domingo and Jamaica), and many other
lesser known nuts and seeds are also sources of similar pro-
ducts.
According to J. R. Jackson,* a large number of new oil seeds
have come into the English market of late years from the
West Coast of Africa, but the supplies have mostly been inter-
mittent ; some few are particularly well adapted for use were a
constant supply forthcoming, more especially the seeds of the
Telfairia occidentalis (a cucurbitaceous plant) ; the Myristica
angolensis (a scentless nutmeg) ; the Hyptis spicigera (a herbaceous
labiate plant); the Poly gala rarifolia ("Maluku" seeds); the
Lophira alata (" Meni " or " Laintlaintain " seeds, from one of
the Dipterocarpece ; Senegambia and Sierra Leone) ; and the
Penteclethra macropJiylla (a leguminous tree, the " Owala " of the
Gaboon, and the " Opachala " of the Eboe country. " M'poga,"
" Mabo," and " Niko " nuts also furnish oils of a character that
might render them very useful.
Similar remarks apply to the oil bearing produce of many
other countries ; in many instances the oils thence obtainable are
of characters so good for a variety of purposes as to leave little
doubt that a considerable amount of trade in such materials will
hereafter become developed whenever the conditions are realised
necessary for the economical growth of the trees and plants, and
the harvesting of their seeds, nuts, or other fruits, &c., or for their
treatment on the spot for the extraction of oil ; together with the
necessary opening up of the districts for transport purposes, so
as to enable regular supplies to be obtained. In all probability
the uncertainty as to what quantity of material could be obtained,
and its price, has largely militated against the importation into
Europe of numerous raw materials of the kind, manufacturers
not caring to expend time, skill, and capital in working up sale-
able products until assured on these points.
* Journal Society of Arts, 1891, 40, p. 122.
19
290 OILS, FATS, WAXES, ETC.
€LASS VI.— DRYING OILS— LINSEED OIL CLASS.
The drying oils proper principally differ from the semi-drying
oils in containing much larger proportions of the glycerides of
the more " unsaturated " acids (linolic, linolenic, and isolinolenic
acids), these substances greatly predominating, and only compara-
tively small amounts of olein and of the glycerides of the solid
fatty acids being present, so that these latter rarely separate in
any quantity as solid " stearines" on chilling and standing.
Owing to the more or less considerable amount present of
these unsaturated constituents, both drying and semi-drying oils
possess higher iodine absorbing powers than the oils of the first
four classes, and develop more heat on mixture with sulphuric
acid (Maumene^s test, p. 147). When drying oils are spread
out in a thin layer they rapidly absorb oxygen from the air,
increasing in weight and " drying up " to a solid varnish, which
in time becomes perfectly hard and not in the least sticky or
"tacky;" semi-drying oils, similarly treated, increase in weight
to a much less extent, and more slowly, and never dry up
thoroughly to a hard varnish free from stickiness. With nitrous
acid, drying oils give no solid elaidins ; semi-drying oils usually
give buttery masses from which fluid matter separates.
The specific gravity of drying oils is usually distinctly higher
than that of oils of Class I., generally lying between '923 and
•935, and increasing as oxidation goes 011 until finally the dried
films or " skins " are heavier than water. According to Bauer
and Hazura, the drying qualities are the more pronounced the
larger the proportion of linolenic and isolinolenic acids present,
linolic acid contributing less markedly to the drying properties ;
so that an oil consisting mainly of the glycerides of oleic and
linolic acids, even when the latter predominates, does not
exhibit drying powers equal to that of another containing a
considerable proportion of linolenic and isolinolenic glycerides.
They regard non-drying, semi-drying, and drying vegetable oils
as distinguishable by the following characters so far as liquid
constituents are concerned : —
Non-Drying Oils contain none, or at most only small per-
centages, of the glycerides of either linolic, linolenic, or isolin-
olenic acids.
Semi-Drying Oils contain more or less considerable amounts
of linolic glyceride, but little or no glycerides of linolenic or iso-
linolenic acid; the drying action being also retarded by the
presence of more or less olein and other non-drying glycerides.
True Drying Oils contain considerable amounts of linolenic
and isolinolenic glycerides, together with linolin, and but small
amounts of olein and non-drying glycerides.
Obviously the exact lines of demarcation between non-drying
DRYING OILS. 291
and semi-drying oils, on the one hand, and between semi-drying
and truly drying oils, on the other, are but faintly traced j so
that it often happens that a given oil is classed by one writer
amongst the oils of one class, and by another amongst those of
the adjacent class.
As regards non-drying and semi-drying animal oils, it is
noticeable that the fatty acids thence obtainable yield no sativic
acid on oxidation by alkaline permanganate (Benedikt and
Hazura) ; from which it results that linolic acid is not a consti-
tuent of oils of this class ; whereas larger or smaller quantities
of sativic acid appear to be obtainable from many, if not all,
vegetable oils by this treatment.
The best known drying oils are the following : —
Name of Oil.
Source.
Hemp seed oil,
Lallemaiitia oil,
Linseed oil,
Poppy seed oil,
Tobacco seed oil,
Walnut oil (nut oil),
Weldseed oil, .
Cannabis saliva.
Lallemantia iberica.
Linum usitatissimum (L. perenne).
Papaver somniferum ; P. rheas ; Glau-
cium luteum; Argemone mexicana.
Nicotiana tabacum.
Juylans regia.
Reseda luteola.
Many other oils of pretty strongly marked drying qualities are
known and employed locally, without being articles in which any
considerable amount of export trade is done ; few of these have
been submitted to any detailed examination. Hickory nut oil
(Gary a olivcrformis) is sometimes sold under the name of
"American walnut oil," but appears to be very inferior in drying
qualities. The seeds of Calopliyllum inophyllum, a forest tree
widely distributed in the eastern tropics, furnish an oil known
by various names (dilo, domba, pinnay, poon seed, or tamanu
oil) ; when mixed with pigments, this forms a paint that dries in
1 2 hours, without any previous boiling ; owing to the large yield
of oil, and the plentifulness of the tree in India, Ceylon, the
Malay Archipelago and Java, and the South Pacific Islands, &c.,
this oil appears likely to be an important article in future. The
kernels of the Aleurites cordata (Elceococca vernicia) furnish an oil
("Japanese wood oil," " tung oil") largely used as a varnish in
China and Japan on account of its extremely rapid drying
qualities. According to Cloez, this oil contains about 25 per
cent, of olein, and 75 of a homologue of linolin, furnishing on
saponificatioii elceomargaric acid, CirH30Oo//r Further investiga-
tion is desirable, as the qualities of the oil are such as to render
it valuable.
* Ccmptes rmdw, 83, p. 943.
292 OILS, FATS, WAXES, ETC.
CLASS vii.— TRAIN, LIVER, AND FISH OILS.
The term " train oil," strictly speaking, applies to any oil
extracted from the blubber of cetaceans and allied marine
mammalia (such as the seal, porpoise, dolphin, walrus, &c.), and,
therefore, in the widest sense includes the sperm oil class, No. X. ;
but in the present connection it is intended to apply only to
those blubber oils that are essentially of glyceridic character, and
not to those that mainly consist of compound ethers of mono-
hydric alcohols. It is not quite the equivalent of the German
term "thran," which also includes fish oils (sardine oil, menhaden
oil, &c.) as well as liver oils (cod liver oil, sunfish liver oil, &c.)
Oils of this class have been much less thoroughly examined as
to their chemical constitution than their importance as trade
products warrants. In some cases they consist mainly of the
glyceride of physetoleic acid, a lower homologue of oleic acid ; but
other glycerides are generally present as well, preventing the
formation of solid elaidins ; soft products from which liquid
matter separates on standing are generally formed, much as with
the oils of Classes II. and VI. ; from which circumstance, toge-
ther with the high iodine number generally indicated, and the
possession of some degree of drying qualities, it appears probable
that drying oil glycerides are also present. Liver oils (cod and
shark's livers, &c.) generally contain perceptible amounts of
cholesterol and allied biliary products ; like fish oils proper (e.g.,
menhaden oil), they evolve large amounts of heat on admixture
with sulphuric acid, resembling the vegetable drying oils in this
respect; whilst train oils (whale oil, seal oil, &c.) give a somewhat
lower degree of heat evolution, probably on account of the presence
of notable amounts of the glycerides of solid fatty acids (stearin,
&c.) When oils of this class are separated from the nitrogenous
tissues immediately, so that no decomposition takes place, they
are comparatively inodorous and tasteless, and contain no
appreciable quantity of free fatty acids ; but if the livers, blubber,
fish, &c., are kept for any length of time before the oil is
extracted, a more or less strongly marked animal fishy smell is
developed, becoming excessively rank in extreme cases ; as in the
case of rancid vegetable oils, more or less hydrolysis of glycerides
with production of free fatty acids, appears to accompany the
development of the strong-smelling bye products thus formed.
The distinction between oils of this class (mainly glyceridic in
character) and those of Class X. (mainly non-glyceridic) is in
actual practice not extremely sharply marked ; for sperm oils
usually contain small quantities of glycerides, although the chief
constituents are non-glyceridic compound ethers ; whilst on the
other hand, some of the blubber oils contain notable amounts of
solid non-glyceridic compound ethers (spermaceti), deposited on
TRAIN OILS.
293
cooling and standing. In fact, it is as difficult or impossible to
draw a hard and fast line of demarcation between the glyceridic
and non-glyceridic animal oils, as it is between the drying and
non-drying vegetable oils ; and for the same reason, viz., that
whilst the two extremes are tolerably sharply contrasted in
general composition, yet various intermediates exist, partaking
of the character of both classes. To some extent, this may
possibly arise from the circumstance, that when a ship is engaged
in oil-fishery, it is not always practicable to keep apart the
blubbers obtained from different species, so that the oil ultimately
extracted is often a mixture of the products obtained from
different kinds of animal, each of which, if examined separately,
would exhibit special characteristics analogous to those dis-
tinguishing different seed oils. In general, it appears that
whalebone-yielding whales * (Balcenoidea] furnish oils containing
little or no monohydric compound ethers like spermaceti ; whilst
toothed whales (Delphinoidea) yield oil where these substances
are usually present, in some cases as chief constituents ; these
latter form the oils of Class X.
The chief oils of this class ate the following : — ' A
Name of Oil.
Sources.
Train Oils-
Dolphin and Porpoise oils,
Seal oils,
Walrus oil,
(morse oil, dugong oil,
manatee oil).
Whale oils and Blackfish
oils.
Delphinus phoccena (Phoccena communis),
or common porpoise. P. orca, or grampus.
Delphinus ddphis, or common dolphin.
Delphinus globiceps. D.tursio. Monodon
monoce.ros, or narwhal.
Phoca vttulina; P. groznlandica; P. barbata;
P.annelata; P. lagura; P.foetida; P. cas-
pica ; P. proboscidea. Otaria jubata. 0.
australis.
Trichechus rosmarus, morse or walrus.
lialicore australis and //. indicus, or
dugong. Manatus australis and M.
>tmt.ricanus, or manatee.
Baloznus mysticetus or B. grcenlandicus,
the "right whale." B. glacialis, or polar
whale. B. bb'ops, or humpbacked whale.
B. antarctica, or cape whale. B. australis,
or southern black whale. Balcenoptera
gibbar, or finner whale. Globiocephalus
intermedias, or pilot whale. G. macro-
rhyncus, or killer. Beluga catodon, or
white whale.
* Huxley classes the existing cetacea (exclusive of extinct genera) as
Balcenoidea and Delphinoidea, the latter group including Platinistidce,
Delphinidce (dolphins, porpoises, grampus, and narwhal) and P/t.yseteridce ;
these last being further subdivided into Physeterina> (cachelots or sperm
whales) and Ilhyncoceti (bottlenose whales).
294
OILS, FATS, WAXES, ETC.
Name of Oil.
Sources.
Liver Oils-
Cod oils, .
Malabar oils, .
Ray and Shark oils,
Fish Oils-
Herring oils, .
(sardine, sprat, pilchard,
anchovy, louar, &c. )
Menhaden oil,
Oolachan oil, .
Tunny oil,
Gadus morrhua(Asellus major). G. cellarius.
O. molva (Molva vulgaris). G. (Kglefinus.
G. carbonarius (Meriangus carbonarius).
G. merlangus (Merlangus vulgaris).
G. pollachius (Merlangus pollachius).
Merluccius communis.
Rhyncobatus pectinata. R. Icevis. Galio-
cerda tigrina. Carcharias melanopterus.
Raja clavata. R. batis. Trigon pastinaca.
Squalus carckarias, or common shark.
S. maxima, or basking shark. S. glacialis,
or Greenland shark. S. zygcena (Zygcena
malleus), or hammerfish. S. acanthius, or
picked dogfish. S. spinax niger, or kulp.
Clupcea pontica (Astrakan herring).
O. sardinus, or sardine ; C. neohouri, C.
lemuru, and C. palasah, or Indian and
Malayan louar. C. sprattus, or sprat.
C. pilchardus, or pilchard. Engraulis
encrasicholus, or anchovy.
Alosa menhaden (Brevoordia menhaden).
Thaleichthys paciferus osmerus.
Thynnus vulgaris.
Schadler gives the following table of colour reactions of seal,
whale, liver, and fish oils with strong nitric acid (sp. gr. 1*45);
sulphuric acid (sp. gr. 1/6— 1 '7) ; and the two mixed in equal pro-
portions (compare p. 153).
Nitric Acid.
Sulphuric Acid.
Mixed Acids.
SEAL OIL—
Red brown,
WHALE OIL—
Brownish, becoming
full brown, and
finally black brown.
LIVER OILS —
Blood red, becoming
brownish red to
brown.
FISH OILS—
Brown, .
Reddish yellow, becoming
reddish brown, and ul-
timately brownish red,
somewhat like blood.
Brown, becoming black
brown.
Violet to black violet.
At first greenish, then
brown, and finally quite
black.
Reddish, becoming
brown.
Yellow, becoming
reddish, and finally
dirty brown.
Yellow red, becoming
bright red, finally
reddish brown with
violet streak.
Yellow, then greenish,
afterwards brown.
VEGETABLE BUTTERS, ETC.
295
CLASS VIII.— VEGETABLE BUTTERS, FATS AND
WAXES, &c.
When the proportion of glycerides of relatively high melting
point to olein is large, the physical texture of a substance that
would be an oil in the tropics becomes more like that of butter
at 15°-20°; concurrently with the change in comparative fluidity
the iodine absorption is largely reduced as compared with oils
of Classes I. and VI., on account of the diminished proportion
of olein present. In the case of certain vegetable glyceridic
waxes (e.g., Japanese wax), the olein is reduced to insignificant
proportions or to nil, with the result of increasing the relative
solidity and considerably raising the melting point. Some of the
substances of this class contain a notable proportion of glycerides
of acids of the acetic family of sufficiently low molecular weight
to be readily volatile with steam at ordinary pressure (e.g., coker-
nut and laurel butters and palm kernel fat) ; others are practically
destitute of such ingredients. When subjected to regulated
pressure (p. 283) liquid oleines are squeezed out, and solid
stearines left, the former closely resembling oils of Classes I.
and VI. when sufficiently freed from the latter.
The best known substances of this class are the following : —
Name of Butter, &c.
Bassia fat; HUpe* butter,
Mahwa butter, Phulwara
fat (Fulwa fat), Shea but-
ter (Galam butter), &c.
Cacao butter, .
Chinese tallow,
Cokernut butter (copra
butter or copra fat).
Cotton seed stearine,
Dika fat, ....
Japanese wax, .
Malabar tallow (Piney-
tallow).
Myrtle wax,
Myristica butters ( Xutrneg
butter, Virola tallow,
Otaba wax, Deuba or
ocuba wax, &c. )
Palm butter (palm oil).
Palmmit butter (palm
kernel oil).
Sources.
Bassia lalifolia (Roxb. ) B. longifolia(L\aja.. )
B. butyracea. B. Parkii (Butyrosperma
Parkii — Kotschy).
Theobroma cacao (Linn. ) T. bicolor (Humb. )
T. aufjustifolium (Sesse). T. leiocarpium
and T. pentagonum (Bern. ) T. microcar-
pium (Mart.)
Stillingia sebifera (Croton sebiferum,Lmn.)
Cocos nucifera; C. butyracea,
Cotton seed oil by chilling and pressing.
Irvingia barteri (Hock.) Mangifera gabo-
nensis (Aubry Le Comte).
Rhus succedanea (Linn.); E. acuminata
(De C.); 2t. vernidfera (De C.); R.juglan-
difolia (Don). It. sylvestris (Siebold).
Vateria indica (Linn.) ; V- malabarica
(Blum.); JSlaeocarpus copaliferus (Retz.)
Myrica cerifera, and several other species
of myrtle.
Myristica officinalis (Linn.); M. moscliata
(Thumb.); M. sebifera (Virola sebifera)',
M. otoba (Humb. and B.); M. ocuba (M.
ucuba, M. bicuhyba); M. malabarica.
Elais fjuineensis (Jacq.) ; E. melanococca
(Gaert.); Alfonsia oleifera (Humb.)
296 OILS, FATS, WAXES, ETC.
Similar solid or semisolid vegetable fats are also furnished by the
following trees and plants : —
Nephelium lappaceum (Linn.) ; indigenous to Sunda Island,
Malacca, and some parts of China. The seeds furnish " Ram-
butan tallow," melting at about 65°, the solid stearine of which
is chiefly the glyceride of arachic acid; a little olein is also
present (Oudemanns).
Carapa guyanensis (C. guineensis) and C. indica (or C. moluc-
censis) ; found in Brazil, Guiana, Cruinea, Sierra Leone, India,
Ceylon, &c. The seeds of these two species furnish " Carapa fat "
(otherwise designated " Andiroba fat," "Coundi oil," " Crabwood
oil," " Touloucoona oil," &c.), possessing a composition akin to
that of palm oil — i.e., consisting chiefly of the glycerides of
palmitic and oleic acid. It usually possesses a sickly persistent
odour almost impossible to get rid of. The coloured natives use
it largely as an unguent and insectifuge for the head, its pro-
perties in this respect being apparently due to an admixed bitter
principle termed carapin.
Mafureira oleifera (Bert.) or Trichelia emetica (Vahl.) This
tree grows in Mozambique, and about Zambesi and the White
Nile ; by crushing the seeds and boiling with water a fat known
as " Mafura tallow " is obtained, much resembling cacao butter,
melting at 42°, and chiefly consisting of palmitin and olein.
Calophyllum inophyllum (Linn.), indigenous to India and the
Malay Archipelago, and C. calaba, found in the Antilles, yield
respectively "Poona fat" (" poon seed oil ") or "Tacamahac fat")
and " Calabar oil." The former is also known by various other
names (vide p. 291).
Laurus nobilis, found largely in Southern Europe and Asia,
yields "laurel butter" ("bayberry fat"), largely consisting of
the glyceride of lauric acid, along with a little myristin and
other homologues, and some olein. A similar product is obtained
from L. persea (Linn.) or Persea gratissima (Gaert.), the Alligator
pear tree of Brazil and the West Indies ; known as " Alligator
pear oil," " Persea fat," and "Avocado oil."
In addition to these, a large number of more or less hard
vegetable fats and tallows are obtainable from other sources,
concerning the chemical constitution of which little or nothing
is known • thus " Malayan tallow " and " Borneo tallow " are
solid fats obtained from the nuts of various species of Hopea in
Java, Sumatra, and Borneo. An analogous product, "Sierra
Leone butter," is obtained in Sierra Leone from Pentadesma
butyracea. " Goa butter" ("Kokum butter" or " Mangosteen
oil ") is a similar fat obtained in the East Indies from the seeds
of Garcinia indica (Mangosteena indica). The allied species
G. pictoria or gamboge tree furnishes "gamboge butter." The
seeds of Pongamia glabra, another East Indian shrub, furnish
" Korinje (Karanja) butter," " Poondi oil " or " Ponga oil," some-
LESSER KNOWN VEGETABLE FATS. 297
what more readily fusible than most of the vegetable fats and
tallows. " Macaja butter " is derived from the edible fruit of
Cocos aculeata (Acromia sclerocarpa, Mart.; Bactris minor, Gaert.),
indigenous to Brazil, Guiana, and the WTest Indies. In Java a
fat much resembling coker butter, " tangkallak fat," is derived
from the Cylicodaphne sebifera. Semisolid fats are obtained
from the Canarium commune of the Moluccas and Malabar
(" Canary oil," "Java almond oil ") and the butternut tree of the
Brazils (Rhizobolus butyrosa; the allied species, R. amygdalifera
(Caryocar brasiliensis) and Caryocar tomentosum, respectively
furnish " Caryocar oil " and " Sawarri (or Souari) nut butter."
The soap tree of Bengal, Southern India, and the West Indies
(Sapindus emarginatus, Roxb.; S. trifoliatus, Linn.; S.laurifolia,
Vahl.), furnishes a fruit rich in saponin, and also yielding a semi-
solid fat. " Maccassar oil " is a semisolid fat obtained from the
seeds of Sckleicliera trijuga ;* and "Piquia oil" ("Pekea fat")
is a similar product from Pekea butyrosa and P. ternatea, found
in Guiana and the Antilles. Melia azedarach (Linn.), the "pater-
noster tree " of Syria, Northern India, and the Deccan, <kc. (so-
called from the employment of its stones in Italy and elsewhere
for making rosaries), also known as Melia indica (Brand.) and
Azadirachta indica (Juss.), furnishes a very similar semisolid fat,
known as " Zedrach oil," " Margosa oil," " Veppam fat," or
" Nimb (or Neem) oil." " Niam fat " is derived from the
Lophira alata, found in Eastern and Western Africa. " Chaul-
moogra oil" is a soft fat fusing at about 17°C., obtained from
the seeds of Gynocardia odorata (Cliaulmoogra odorata), much
used in India, China, and elsewhere for medicinal application to
the skin. "Soudan butter" is a soft fat obtained by boiling
with water the seeds of Vitellaria paradoxa, or Soudanese butter
plant ; a similar product is obtained in Cochin China and Japan
from the seeds of Sebifera glutinosa (Tetrantliera laurifolia, Jacq.)
The seeds of (Enocarpus bacaba and CE. patawa, of Central
America, yield by similar treatment a soft fat known locally as
"Comou butter." "Para butter" or "Assai oil" is similarly
obtained from the Assai palm (Euterpe oleracea], common in
Brazil and the neighbourhood of Para. "Chequito" is a fatty
substance obtained by the Kaffirs of Southeast Africa from the
"butter tree," Combretum butyraceum. The seeds of Cocculus
indicus contain a solid fat, extracted and used by the natives in
India, but apparently not yet known commercially ; similar pro-
ducts are obtained from the fruit kernels of Lucuma bonj)landi
in Mexico, and the Ochoco (Dryobalanops) of Guinea.
* Also from the oleaginous fruit of Stadmannia (Cupania) Sideroxylon,
growing in Sunda and Timor Islands, and from the seeds of the safflower
(Oarthamus tinctorins) ; other varieties of socalled "Macassor" oil are
simply more or less fluid oils in which odorous flowers, &c., have been
digested so as to scent them.
CFTHE
298 OILS, FATS, WAXES, ETC.
In addition to the above, a large number of other sources of
vegetable fats exist in different parts of the world, the knowledge
of which is as yet chiefly confined to the natives ; there can,
however, be little doubt that in due time, as civilisation advances
and opportunities for export and manufacture become more
frequent, many of these little-known products will be found to
be of considerable value as sources of oleaginous material.
CLASS IX.— ANIMAL FATS— TALLOW, LAUD, AND
BUTTER CLASS.
Almost every known animal is capable of yielding more or less
considerable amounts of fatty matter by appropriate treatment ;
but in practice, comparatively few are actually employed as
sources of fat, apart from their consumption as food. The solid
fat of oxen and sheep (known as tallow or suet when derived from
the adipose tissues of the body), the grease extracted from their
hoofs (neat's foot oil, sheep's trotter oil), and that obtained by
boiling the bones (bone grease) are closely akin in general
composition, except that the latter are softer in character, chiefly
because containing a larger proportion of olein, and a smaller
amount of solid glycerides. The fatty matters (butters) contained
in the milk of cows and ewes, on the other hand, have a composi-
tion materially different from that of the fats present in the
adipose tissues of the body ; and the same remark applies to the
milk fats of all other mammalia, so far as they have been
examined. In general, the milk fats of various animals do not
differ very greatly in character ; thus, the butters derived from
the cow, ass, ewe, goat, elephant, hippopotamus, sow, mare, and
woman, appear to be as closely akin as are the more or less solid
tallows, greases, and suets obtainable from the body tissues of
these various animals ; but whilst the latter fats are all essentially
mixtures of the liquid glyceride of oleic acid, and the solid
glycerides of stearic and palmitic acids (the liquid constituents
being present in larger quantity in the softer fats, like lard), the
former fats contain a considerable amount of the glycerides of
acids, also of the stearic series, but of much lower molecular
weight than palmitic acid. Similarly, the milk fat of the whale
is not widely different from that of the cow, although the oil of
whales' blubber differs much from suet in composition.
The fats obtained from the carcases of birds (goose grease,
turkey fat, pheasant grease, &c.) appear to be substantially
similar to the softer body fats of mammalia in general composi-
tion, essentially consisting of olein, with enough stearin and
palmitin to render them semisolid at the ordinary temperature ;
the oleaginous matter contained in eggs (e.g., hen's eggs) is softer
ANIMAL FATS AND OILS.
299
still, and consists of olein and palmitin, together with other
substances foreign to the oil proper (vide p. 121).
Various reptiles (turtles, crocodiles, &c.) are utilised in different
parts of the world as sources of oleaginous matters, apparently,
for the most part, closely akin to the fats of the mammalian
vertebrates ; on the other hand, the oily matters derived from
fish are differently constituted (supra, p. 292).
The following list includes the more important solid or semi-
solid animal fats, apart from those derived from fishes and
cetacea : —
Name of Fat.
Sources.
Bone fat, ....
Butter (cow's milk fat),
Butter substitutes (butterine,
margarine, oleomargarine),
Crocodile fat (alligator fat), .
Egg oil,
Goose grease,
Horse grease (mare's grease)
Lard, ....
Tallow,
Tannery grease, kitchen grease,
wool grease,
Bones of oxen and horses, &c., extracted
by boiling or by solvents.
Domestic cow.
The softer portions of the fat of oxen
and sheep, &c., separated by special
processes.
Indian crocodile and common alligator
(Alligator Iticius).
Yolks of hen's eggs (Gallus domesticus).
Common goose.
Horse carcases (Equus caballus}.
Common hog.
Ox, sheep, goat, &c.
Animal greases from various kinds of
trade refuse.
In addition to these, the fat of the alpaca is used to a con-
siderable extent in some parts of South America; that of the
dog in continental Europe, that of the hippopotamus in Africa, and
that of the turtle in the islands "of the South Pacific, Brazil, and
along the South American coast. The last is sufficiently fluid in
a tropical or subtropical climate to be used as a burning oil.
Bear's grease was at one time highly esteemed as a pomade, but
is now mostly superseded by other forms of clarified fat. Many
other animal fats are also used locally in different countries to a
greater or lesser extent, but as yet are not articles of regular
trade. When the solid or semisolid fats of this class are
subjected to expression, the liquid animal oleines of Class IV.
result — e.g., lard oil, tallow oil, &c.
CLASS X.— ANIMAL OILS— SPERM OIL CLASS.
The blubber oils included in Class VII. (whale, seal, porpoise,
<fec.) differ from those belonging to this class essentially in that they
consist chiefly of fatty glycerides ; whereas the oils now under
consideration, whilst not invariably free from glyceridic con-
300 OILS, FATS, WAXES, ETC.
stituents, have, as regards their leading constituents, an entirely
different composition, these substances being compound ethers
formed from monohydric alcohols and fatty acids, analogous to
ethyl acetate and similar substances. In general, two kinds of
such compound ethers appear to be present simultaneously — one
liquid at ordinary temperatures, corresponding with the olein of
ordinary vegetable oils, and consisting of ethers of acids of the
oleic family ; the other solid, corresponding with stearin or
palmitin. and consisting of ethers of acids of the acetic family.
Just as a vegetable oil on chilling deposits solid matter of the
stearin character, readily separable by filtration or straining, so
does a blubber oil of the sperm class similarly deposit solid
crystallisable matter, generally the substance known as spermaceti
(mainly consisting of cetyl palmitate); the liquid portions
separated from this deposit appear to be mixtures not only of
compound ethers of different homologous acids, but also of
different homologous alcohols, some of which belong to the ethylic
series, whilst others are apparently homologues of acrylic alcohol,
capable of combining with iodine, like the unsaturated acids. In
consequence, when saponified, these liquid oils yield large
percentages of products insoluble in water, but soluble in ether,
«fec., consisting of mixtures of the alcohols formed during saponi-
fication ; a circumstance sharply distinguishing them from the
glyceridic oils of Class VII., which yield only comparatively
small quantities of unsaponifiable matters insoluble in water,
chiefly consisting of cholesterol and similar substances.
On account of the presence of compound ethers of the oleic
family, oils of the sperm class become more or less solidified by
nitrous acid in virtue of the elaidin reaction ; with Maumene's
test (p. 147) they develop but little more heat than olive oil,
being thus sharply distinguished from most fish oils of Class VII.,
which give a much greater heat evolution (pp. 149, 150). Their
peculiar compound ether composition largely raises the saponifi-
cation equivalent.
The physical characters of this class of oils also are peculiar in
virtue of their unusual constitution ; thus their efflux viscosity
(p. 101) is much less influenced by variation of temperature than
is the case with most other oils, whence their value as lubricants
for special purposes. Their specific gravity is low, usually con-
siderably below -900, near -880.
The principal oils of this class are as follows : —
Name of Oil.
Sources.
Sperm oil, .
Doegling oil (Arctic sperm
oil or true bottlenose oil),
Physeter macrocephalus, L. (Cachelot
whale).
Hypeioodon rostratus (Balcena rostrata),
or true bottlenose whale, H. Bid ens.
WAXES. 301
Various other toothed cetaceans also furnish oils containing
spermaceti in sufficient quantity to separate out in the solid
state on chilling and standing, more especially the oil from the
bottlenose dolphin, Delphinus globiceps, which appears to be
essentially intermediate in character between the almost wholly
glyceridic and largely valerin-containing oil from the common
porpoise, and the mainly compound ethereal sperm oil of the
cachelot in which only small amounts of valerin are present.
CLASS XI.— VEGETABLE NONGLYCERIDIC WAXES.
Several species of plants are known, the berries, leaves, stalks,
<fec., of which are naturally covered with a waxy exudation closely
akin in its origin to certain of the more solid vegetable fats, but
differing therefrom in being essentially nonglyceridic in character.
Of these substances the principal are as follows : —
Name of Wax.
Source.
Carnauba wax,
Cowtree wax,
Corypha cerifera (Linn.); Copernicia
cerifera (Mart.)
Galactodendron americaum (Linn.);
(G. utile, Kunth ; Brosimum galacto-
dendron, Don.)
In addition very similar products are obtained from several
other sources — e.g., Petha wax, from the bloom on the Indian
white gourd (Benincasa cerifera) ; Fig wax (Getah wax), pre-
pared in Java and Sumatra from Ficus umbellata and F. cerifera
(Blume) ; Palm ivax (Ceroxylin), largely used in Brazil, from the
common wax palm, Ceroxylon andicola (Humb.), and the Klop-
stock palm, Klopstockia cerifera (Karsten) ; and Cordillera wax
from the Cordillera waxtree (Elceagia utilis.
These products, however, do not seem to have been submitted
as yet to full chemical investigation, so that it is not certain
whether they are true vegetable waxes of nonglyceridic character,
or simply vegetable fats of waxy texture analogous to socalled
Japanese wax. Comparatively little of these various kinds
of vegetable waxes is as yet exported to Europe, most being
used for candlemaking, &c., in the countries where they are
indigenous.
CLASS XII.— BEESWAX AND SPERMACETI CLASS.
The nonglyceridic waxlike compound ethers of animal origin
used to any extent industrially are but few in number, the prin-
cipal being as follows : —
302
OILS, FATS, WAXES, ETC.
Name of Wax.
Beeswax (ordinary beeswax.
Andaquia wax, Antilles wax,
African beeswax, Abyssinian
beeswax, &c.),
Chinese wax (Peh-la or Pela),
Indian wax (Arjun wax),
Niin fat, ....
Spermaceti, ....
Woolgrease,
Source.
Apis meUifera, or common bee. Numer-
ous allied species exist, many of which
are also wax producers — e.g., Apis
fasciata (Melipona fasciata), or South
American bee ; Apis unicolor, or Mada-
gascan bee ; Apis dorsata, of the Eastern
Archipelago. The common wasp and
other allied genera are also wax pro-
ducers to a limited extent.
j Coccus sinensis (Coccus pe-la, C.chinensis}
Ceroplastes ceriferus.
Coccus adipofera.
Physeter macrocephalus.
Natural grease (inspissated perspiration)
of the common sheep.
CHAPTER XIY.
PRINCIPAL USES OF OILS AND FATS, &c.
THE classification described in the previous chapter is mainly
based on the physical and chemical characters of the natural fixed
oils and allied substances ; from the point of view of their leadiDg
practical uses they may be conveniently considered under one or
other of the following six heads : —
1. Substances used for edible purposes, including cooking and
preservation of food (e.g., sardines).
2. Fluid oils employed for burning in lamps or otherwise.
3. Substances furnishing solid materials for candlernaking.
4. Substances used in the manufacture of soap.
5. Drying oils employed for paint manufacture and in the pre-.
paration of varnishes, linoleum, and such like products.
6. Substances used for miscellaneous purposes ; more especially
as lubricants or ingredients in lubricating mixtures ; for currying
leather, dressing cloth and textile fabrics, and similar purposes ;
as oil baths for tempering metals ; as solvents for odorous matters
in the process of enfleurage in perfumery manufacture ; for the
preparation of unguents, pomades, cosmetics, &c. ; in the manu-
facture of sealing wax and analogous compositions ; and for,
numerous minor uses in the arts generally.
Of these six groups, Nos. 3 and 4 are separately considered in
§ 6 and § 7 (candle and soapmaking, including glycerol extrac-
tion) ; with respect to the other uses, some few points are of
special interest from the technological point of view, in connection
with which the question of purity and freedom from adulteration
with inferior materials is frequently of prime importance.
EDIBLE OILS AND FATS. 303
EDIBLE AND CULINARY USES OF OILS,
FATS, «fec.
Fatty matters of various kinds are ingredients in most kinds
of food stuffs in common use to a greater or lesser extent ; thus
apart from suet and the adipose tissues interleaved with the
" lean " of most kinds of animal meat, most vegetable seeds, nuts,
and other edible produce contain more or less considerable
quantities of oleaginous matter ; sometimes to an extent suffi-
ciently large to admit of oil being extracted by pressure fy.g.t
olives, walnuts, hazelnuts, &c.), sometimes only in smaller quan-
tity, so that a solvent (ether, Ac.) is requisite before the presence
of oil can be demonstrated. When thus treated, however, even
such substances as wheaten flour and cereal produce generally,
rice, and dried vegetables can be shown to contain small quan-
tities of oleaginous ingredients.
Apart from the consumption of oily matter for food in forms
such as these, large quantities of separately extracted fatty sub-
stances are habitually used as edibles by both civilised and
uncivilised races — e.g., " salad " oils employed for " dressing " raw
vegetables and otherwise as food materials ; more or less purified
and rendered animal fats, especially dripping and lard ; and the
fatty matter of cow's milk (butter). In cold climates seal and
whale oil are eagerly partaken of by the natives as heat-generating
foods, whilst a lump of tallow is a delicacy ; elsewhere fish pre-
served in oil (e.g., sardines), or cooked in hot oil, pastry containing
butter, suet puddings, and numberless other viands into the com-
position of which more or less oleaginous matter enters, are-
everyday articles of diet.
With the exception of actively medicinal oils (such as croton and
castor oils), the great bulk of natural glycerides are suitable as
food material for cattle, especially when used without separation
from the other vegetable matters naturally accompanying them.
Linseed cake (crushed linseed subjected to pressure so as to
express most of the oil), and similar substances from other kinds of
seeds, &c., are well known cattle foods, the value of which largely
depends on the amount of residual oily matter left in the mass.
Waxes, on the other hand, are but little adapted for nutritive
purposes ; thus beeswax (even when eaten along with honey)
mostly passes unchanged through the alimentary canal, and is not
assimilated at all, either by human beings or other mammalia.
In the preparation for table and culinary use of oils and fatsr
&c., but little treatment of a technical nature is usually requisite,
the chief points requiring attention being good quality of the
raw material, and cleanliness in the treatment to which it is
subjected ; thus the excellence of the butter prepared in a given
dairy chiefly depends on the quality of the milk from which it is.
separated, and the care and cleanliness employed throughout the
304 OILS, FATS, WAXES, ETC.
process. Very similar remarks apply to the preparation of the
finer qualities of refined lard intended for food, and the ordin-
ary kitchen operations of clarifying dripping, &c., and to the
extraction of vegetable oils generally. As already described,
"virgin" oils, and "first runnings" are generally prepared from
choice oil sources (olives, arachis nuts, &c.) by gentle pressure
without heat, somewhat coarser grades being subsequently ex-
pressed by stronger pressure and heat combined; refining by
agitation with water, subsidence, and straining, being usually
preferred to processes involving chemical treatment. In some
parts of Russia and Eastern Europe much coarser oils are con-
sumed by the peasantry than are usually similarly employed
amongst either Western Nations or Asiatics ; hempseed, poppy
seed, and linseed oils, often somewhat crudely extracted, being
largely used as cooking oils. | Of late years, however, sunflower
seed oil has to a great extent superseded these coarser oils ; whilst
in Western Europe, America, and many other parts of the world,
cotton seed oil, expressed by the hydraulic process described
in Chap, ix., and subsequently refined by boiling with alkalies,
ifec., is now very largely employed for many purposes for which
formerly only olive oil was used, or the better grades of arachis
oil, sesame oil, and similar high-class substances ; the result of
properly refining a fair quality of raw cotton seed oil being to
produce a light coloured pleasantly tasting wholesome product
eminently well adapted for frying fish and such like cooking
operations. In connection with this the following table by
Grimshaw is of interest, showing the way in which a ton of seeds
is practically utilised : —
Cotton seeds = 2000 pounds.
i
About 1089 Ibs. of " Meats " About 20 Ibs. About 891 Ibs. of "Hulls"
or decorticated seeds ready of Lint. ultimately separated into
for crushing
Fibre used for high class
papermaking.
About 800 Ibs. About 289 Ibs. of „ , ., , , ,. ,
Oilcake used Crude oil. Fu^ the ashes °f ^
for cattle feeding. After refining this J™ an excellent fer'
yields tlllser'
I
Summer yellow (refined). Foots,
After chilling and filterpressing, &c., used for soapmaking, &c.
this yields
Winter yellow. Cotton seed stearine.
VEGETABLE LARD. 305
Cotton Seed Stearine (Vegetable Margarine). — When
cotton seed oil is chilled, a portion solidifies as solid glycerides ;
when these are separated by " bagging " or the use of a filterpress
(p. 229), and subsequently subjected to hydraulic pressure, a com-
pletely solid fat results. The more solid substances thus obtained
are largely used as ingredients in artificial butter ; the physical
characters, and especially the melting point, vary somewhat with
the extent to which the expression has been carried ; usually
cotton seed stearine is pressed so as to melt at a little above 30°.
Amongst the Hindoos and others whose religious beliefs
preclude the use of animal fats for edible and cooking purposes,
a large sale now exists for purely vegetable fats of buttery con-
sistence (vegetable lard) ; the process of semisolid stearine
extraction from vegetable oils (such as cotton seed, cokernut,
and many other native oils) is consequently somewhat largely
adopted for the purpose of meeting this demand ; quite
irrespective of the illegitimate use of these products for purely
adulterative purposes in reference to more highly priced animal
fats, especially butter and lard.
Another substance, improperly called cotton seed stearine, is
obtained by distilling with superheated steam the mixture of
organic acids formed when a mineral acid is made to decompose
the " foots " obtained during the process of refining cotton seed
oil by alkalies (p. 261), and pressing out the "oleine" from the
distillate after cooling and solidification. Products of this kind
appear to contain a large amount of un saturated solid fatty
acids, possibly isoleic acid (p. 29). A. H. Allen found that a
" stearine " of this kind had the specific gravity 0-868 at 99°,
and melted at 40°, whilst the iodine number was 89 '9 ; the theo-
retical value for pure isoleic (oleic) acid being 90'1.
Recent Cultivation of Sunflower Seeds in Russia. — Of
late years the oil obtained in Russia from sunflower seeds has
very largely displaced the other cooking and table oils (chiefly
poppy and hemp) in popular estimation, and the cultivation of
the plant has increased enormously; with due care in the drying
and cleaning of the seeds, the oil first expressed is equal to the
best French table oils in colour, flavour, and taste. The shells
form a considerable article of trade for heating purposes, whilst
the stalks, dried in piles, are preferred even to pine wood for
producing a quick and hot- flame fire ; each acre yields about
2,000 Ibs. of such firewood and some 1,350 Ibs. of oil. The ashes
contain much potash ; 1,000 Ibs. of dried stalks yield 5 7 '2 of
ash, from which about 35 per cent, of the best potashes are
obtainable. The oilcakes are looked upon as the best in Russia ;
superior to either hemp or rape seed cake ; upwards of 2,000,000
Ibs. are exported by the Government of Saratov alone. The
seed cups are used as food for sheep. In the larger mills the
process of extraction is much the same as that used in England
20
306 OILS, FATS, WAXES, ETC.
for linseed and rape seed (Chap. XL), the shelled seeds being
dusted and crushed to a paste in a steam heated vessel ; the
warm paste is wrapped in camel's hair webbing, and pressed.
•Out of 104 oil mills in Russia, 85 are employed solely in
obtaining sunflower oil, steam being used in 24, and manual
labour only in the others (Journ. Soc. of Arts, March 18, 1892).
Manufacture of Lard. — The fatty tissues of the hog when
properly rendered furnish a white semisolid grease considerably
softer than the corresponding fat (tallow) from oxen and sheep,
chiefly differing therefrom in containing more olein and less
solid glycerides. In most of the larger American hog slaughter-
ing factories the fats from different parts of the body are kept
separate from one another, each being treated in a steam render-
ing pan reserved for that kind only ; s@ that different grades are
obtained of considerable constancy of character. The fat from
the vicinity of the kidneys, and the "leaf" fat from underneath
the skin furnish a superior and harder lard; whilst the fats from
tainted carcases and diseased hogs, being generally melted down
all together, produce the lowest grade. The finest qualities are
usually put up in bladders, and the other sorts in kegs, whence
the terms "bladder lard" and "keg lard" are respectively applied.
Bladder lard, when pure, fuses at 42° to 45° ; keg lard at 28° to
38°, according to its quality (Allen). The particular texture
exhibited by any given example depends largely on the way in
which the cooling and solidification of the fused fat was effected,
the texture being rendered firmer "by stirring during solidifica-
tion, or subsequent chilling in a refrigerating chamber. Some-
times water, salt, and a variety of other weigh tgiviDg adul-
terants (such as Iceland moss and starch) are stirred in for the
purpose of increasing the solidity of the mass. Sodium carbonate
solution thus admixed whitens the fat, and enables it to hold a
larger proportion of water. The chief sophistication of American
lard consists in subjecting the pure lard to pressure so as to
express "lard oil" (p. 231), and then working up the residue
with cotton seed or other cheap oil so as ultimately to obtain a
mass of the proper consistency and texture ; beef suet, mutton
tallow, and other fatty matters being often also introduced.
A test at one time much relied on for the detection of cotton
seed oil in such mixtures was Becchi's silver nitrate test
(variously modified by different chemists*), depending on the
reduction by some constituent of cotton seed oil of silver from
silver nitrate, with the formation of a brown mass in a way
not observed with other fats, &c. ; but latterly it has been
found that by thoroughly refining or otherwise treating the
cotton seed oil this constituent is mostly either removed or
altered, so that the presence of that oil is no longer indicated
. with certainty by silver nitrate. Sesame oil, cokernut butter,
*Vide Analyst, 1887, 170 ; 1SSS, 95, 161, et seq.
ti
LARD.
307
and similar materials are also used as admixtures, generally
along with more or less harder fat, especially " beef stearine."
According to A. H. Allen the presence of any considerable
quantity of cotton seed stearine or coker butter may be detected
by the effect produced on the relative density, melting point,
saponification equivalent, and iodine number, as indicated by the
following table :—
Lard.
Cokernut Butter.
Cotton Seed
Stearine.
Specific gravity at ' ~» *
lo *o
•860--861
•SG8--874
...
Specific gravity at 37° '8 \
(=100°F.),t . . J
•903--907
•910- -916
•911- -912
Melting point,
Saponification equivalent,
33°-45°
286°-292°
20°-28°
209°-228°
32°
285°- 294°
Iodine number,
59-62
9
The percentage of water present is determined as described on
p. 122; substances insoluble in ether (starch, limesoap, <fec.) as
indicated on p. 123. Mineral nonvolatile matters (lime, salt,
alum, <kc.) may be found by incineration: soluble substances
(salt, alum, &c.) by agitating thoroughly with hot water and
separating the aqueous solution for further examination.
Pure unadulterated lard has, according to various authorities,
the total acid number 192-197, corresponding with the saponi-
fication equivalent 285-292, averaging about 289, whence the
mean equivalent of the fatty acids is about 277 (p. 1G5); the
average value directly found is near 278. The iodine number
has been found to lie between 50 and 64, indicating about two-
thirds olein and one-third palmitin and stearin as the essential
composition. Traces of unsaponifiable matters (0*2— 0'3 percent.)
are also generally present. When perfectly fresh, lard contains
only minute quantities of free fatty acids, less than 1 per cent, j
larger amounts are usually found in stale or partly rancid lard.
When chilled to 0 and pressed, lard furnished a solid stearine
(sometimes known as solar stearine) and lard oil (p. 231) : the
examination of the fluid oil thus obtained is often better adapted
than that of the original lard for the purpose of detecting adul-
teration ; thus admixture of cotton seed oil largely increases its
iodine number, and interferes with the formation of a solid elaidin
(p. 137), and similarly in other cases. Still better results are ob-
tained on separating the solid and liquid fatty acids by Muter
and Koningh's process and examining the latter apart (Chap, xv.)
Artificial Lard. — This name is sometimes applied to various
mixtures of " beef stearine " (vide infra) and cotton seed oil, or
similar hard fats and vegetable oils, in such proportions as to
Water at 15° '5 = 1.
t Water also at 37°' 8 = 1.
308 OILS, FATS, WAXES, ETC.
give a product possessing the consistency of genuine lard.
These substances are less frequently sold under names clearly
indicating their nature than used for admixture in larger or
smaller proportions with genuine lard for purposes of sophisti-
cation. According to some writers adulterations of this kind
are becoming much less common than they were a few years
ago ; but it is doubtful if any great improvement has really
taken place in the trade, as a whole.
Manufacture of Artificial Butter. — Several processes are
in use whereby the more fusible portions of fresh animal fatty
matters are separated from the more solid constituents, so as to
yield a mass of buttery consistence which, when treated with
annatto or other harmless vegetable colouring matter, and
churned up with milk or otherwise treated so as to acquire a
weak buttery flavour, furnishes a cheap palatable foodstuff. The
better kinds of product thus obtained are undeniably valuable
additions to the general food supply ; but the practice of mixing
them with genuine cow's butter and selling the mixture (or the
substitute alone) at considerably above its proper value under
the name of "butter," is obviously not a desirable one.* More-
over, the inferior kinds of oleomargarine are not invariably of
harmless character, as the earlier forms of tapeworm (cysticerci)
and other entozoa are sometimes present.
The earliest processes are said to date commercially from the
Franco-German war, when the scarcity of butter in Paris during
the siege led to the utilisation of various other forms of fat (more
especially that of horses) and their treatment so as to obtain a
softer and more palatable substance. The original Mege Mouries
process consists in treating chopped-up adipose tissue with a
weak alkaline solution (potassium carbonate) and minced sheep's
or hog's stomach at about 45° C., when partial digestion of the
albuminous fatty envelopes and cellular tissue is brought about
so that the fat separates, being "rendered" completely at the
comparatively low temperature used. On cooling and standing
the solid glycerides more or less completely separate in a crystalline
form, so that by applying pressure in cloths in an ordinary
hydraulic press (p. 231) the still liquid portion is squeezed out,
whilst a tolerably hard mixture of glycerides is left, valuable for
candlemaking. Instead of alkaline potash solution dilute hydro-
chloric acid is preferred by some, more especially with an addition
of calcium phosphate, so as to form phosphoric acid or an acid
phosphate of calcium : the digestive action is thus promoted and
hastened.
Much of the "bosch," "Dutch butter," "butterine," "mar-
garine,"! and "oleomargarine" of the present day is prepared
* In certain of the United States the Legislature requires that oleomar-
garine must be coloured pink in order to prevent its being sold as butter,
f The term "margarine" is an unfortunate survival of a misnomer
ARTIFICIAL BUTTER. 309
by processes analogous to that of Mege Mouries, excepting that
the digestive operation is omitted. The sorted adipose tissue
(carefully handpicked, and sometimes washed to separate traces
of blood and suchlike animal matters, and then finely minced) is
subjected to gentle heat ; in some cases alone, so that the more
fusible constituents liquate away from the rest, the mass being
supported in trays on sloping racks in a room kept at a temper-
ature not much exceeding 50° C. ; in other cases in tubs in contact
with water at about 45°— 48°, when the more fluid matters gradu-
ally float up and are withdrawn from time to time. Beef suet
is the preferable material, but sheep's fat is also employed ; much
of the margarine made in America is derived from hog's fat,
being in fact a variety of lard from which much of the solid
matter has been removed. The partially exhausted tissues left
are rendered in the usual way (p. 245), either alone or mixed
with other fatty matters, so as to produce a superior quality of
tallow : the oleaginous fluid matters that result from the first
processes are cooled and kept at about 25° for some time to allow
the solid glycerides to crystallise, and the mass is then pressed.
The solid pressed residue is generally known as " beef stearine,"
and is largely used in the manufacture of factitious lard by
incorporation with cotton seed or other fluid vegetable oil so
as to form a mass of the required physical consistency.
The resulting expressed oil acquires a buttery consistence at
the ordinary temperature, but is usually somewhat softer than
cow's butter ; by thoroughly churning it up with fresh (or, as
preferred by some, sour) milk, and a little minced cow's udder,
it acquires a slightly firmer consistence and a buttery flavour.
If the temperature during pressing has been too high, or if the
solid glycerides have not sufficiently thoroughly separated whilst
standing, the expressed substance may be too solid, in which
case it is admixed with fluid vegetable oil (cotton seed, arachis,
sesame, tire.) The temperature at which the churning is effected
applied to certain fat constituents in earlier days before the chemistry of
these substances was well elucidated. By saponifying tallow, lard, and
other animal fats, and separating the fatty acids thence ultimately obtained
as far as practicable, various substances" were got of somewhat different
characters in different cases, but mostly consisting of a liquid fatty acid
(oleic acid) ; a solid constituent melting at about 75°, known originally as
maryarous acid (Chevreul), subsequently as stearic acid; and another solid
product termed maryaric acid, crystallising in pearly scales (whence the
name, from /mupyapov, or ^npyupiT^ — pearl), and melting at a lower
temperature, near 60°. This last was long regarded as a single substance
indicated by the formula C^H^C^; the glyceride containing it in the
original fat was accordingly known as margarine. Subsequently, how-
ever, it was shown by Heintz that this pearly-scale crystalline substance
was a mixture of homologous substances, consisting chiefly of stearic and
palmitic acids; and that whilst true margaric acid, C]7Hg402, could be
produced artificially (p. 21), it was not a product of the saponification of
natural fats, and its supposed glyceride, margarine, was not contained
therein.
310 OILS, FATS, WAXES, ETC.
has a good deal of influence on the physical character of the
product; preferably the factitious "butter" is withdrawn and
quickly chilled, either by running into ice cold water or on to
slabs of solid ice, and then made up into " pats " for the market.
Annatto, turmeric, saffron, and various other colouring matters
(preferably vegetable, but sometimes of coaltar origin) are used
to communicate a yellow tint ; sometimes a minute quantity of
butyric ether or other special flavouring and odour-giving sub-
stance is added. Inferior kinds of socalled margarine are some-
times made by the simple process of working up comparatively
hard fats (such as moderately scentless tallow) with fluid vegetable
oils, coker butter, lard oil, and similar softer materials ; when such
mixtures are further incorporated with more or less stale genuine
butter and churned up with milk, &c., products are obtained very
closely simulating genuine butter of second or third rate quality ;
they may be made to correspond with actual butter so closely as
to pass most of the tests applicable thereto, excepting that a more
or less marked increment is observable in the " Hehner number ;5
(p. 166), and a decrement in the Reichert number (p. 173) ; with
in many cases a slight depreciation of the specific gravity.
Margarine and oleomargarine prepared from solid animal fats,
without admixture with cokernut oil, possess a higher total acid
number than genuine butter — viz., 192 to 199 — corresponding
with the saporiification equivalent 282 to 293 (tripalmitin
= 268-7, trioleine = 294-7, tristearin - 296-7) ; the iodine
number is also higher, being usually between 45 and 55; but since
methods have been discovered * for removing the characteristic
odour of cokernut oil, the deodorised substance can be admixed
with animal margarine in such fashion as to bring down both the
saponification equivalent and iodine number to close to the
figures observed with genuine butter. Moreover, since cokernut
and palmnut oils furnish much smaller percentages of insoluble
fatty acids, and larger ones of volatile acids than ordinary soft
animal fats, their admixture in the mass tends to lower the
Hehner number, and raise the Eeichert number, thus rendering
detection by these tests more difficult.
The following table, based on one given by Schadler,f repre-
sents the wray in which the fatty matter from an ox is utilised : —
* Schlink's method for removing the volatile and odorous fatty acids, &c. ,
from cokernut oil, consists in treatment with alcohol and animal charcoal,
whereby a perfectly white mass is obtained, of the consistency of butter,
and of sweet neutral agreeable flavour. A very considerable sale for the
product exists, nominally as a " vegetable lard " for cooking purposes
(supra) ; practically, however, the material is largely if not mainly em-
ployed in sophisticating cow's butter. For a description of tests emploj^ed
in the examination of butter supposed to be thus adulterated, vide F. Jean,
Moniteur Stientifique, 1890, 36, p. 1116; in abstract, Journ. Soc. Chem. Ind.,
1891, p. 275.
t From results obtained in Sarg's factory, Vienna.
UTILISATION OF OX FAT.
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312 OILS, FATS, WAXES, ETC.
FINAL PRODUCTS.
" Artificial butter," about 18 kilos, representing of
oleomargarine, .... about 16'5 kilos.
Pure commercial " glycerine,"
" Stearine " (stearic and palmitic acids),
" Oleine " (impure oleic acid),
" Scraps " used for manure,
2-5
24-0
23-5
16-5
83-0
It would hence seem that a very considerable loss of glycerol
accompanies the various processes gone through in the course of
the isolation of the pure redistilled commercial article; for
24 kilos, of stearic acid, together with 23-5 of oleic acid, theo-
retically correspond with about 5 -3 kilos, of glycerol instead of
2-5, indicating a total loss of more than 50 per cent, of the
glycerol formed during saponification.
LAMP OILS.
From the earliest ages the use of lamps has been general,
essentially consisting of a vessel for holding the oily matter,
provided with some kind of porous wick up which the oil rises,
by capillary action, to supply the place of that burnt in the
flame. Probably this arrangement was actually a development
of the still earlier torch or flambeau, consisting in its simplest
form of a splinter of pine containing natural resin, and in a more
elaborate shape of strands of vegetable fibre dipped in resin,
asphalt, and similar materials (obviously the prototype of the
more modern wicked candle). The wicks used in some of the
early forms of lamp appear to have been of rush-pith, apparently
closely akin to the rush-candle or rush-light ; saving that in the
latter the vegetable wick was dipped in a comparatively solid
fat melted by heat, and then taken out and allowed to
harden, whilst in the former the wick was held in position by
some simple device, and a thinner fat or oil used, fluid enough
to moisten the wick without extraneous heat. In the modern
" nightlight " both forms are substantially combined, the arrange-
ment being virtually a candle on first lighting, and practically an
oil lamp after burning sufficiently long to melt the remainder of
the fatty matter by the heat developed.
Amongst the Eastern nations, crude natural naphtha or
petroleum has been largely used as a burning oil from time
immemorial ; but the methods now in use for purifying it and
separating it into different fractions (some of which are far better
adapted for burning in lamps than the raw material, whilst others
are quite unfit for that purpose) are of quite modern origin.
Amongst the Greeks and Romans, olive oil appears to have been
LAMP OILS. 313
largely used for the purpose ; whilst rough candles of tallow,
and superior ones of wax, were also in use. In all the early
forms of household lamp no chimney was employed, so that the
flame was invariably more or less smoky, a circumstance which
considerably limited the number of vegetable oils available ; in
1784, Argand introduced the form of lamp still bearing his name
(although greatly altered and improved by subsequent inventors),
essentially consisting of a circular wick with an air supply in the
centre, a chimney of iron (later of glass) being also applied, so as to
increase the draught and so facilitate combustion, thus diminish-
ing smoke and increasing the light emitted.* This invention
greatly stimulated the use of oil lamps, and colza oil and sperm
oil soon became extensively used for consumption therein, together
with many other varieties, notably the oils from rape seed, ground
nuts, and cotton seed. At the present day, however, the use of
these oils in this way, though by no means inconsiderable, is
small as compared with that of the hydrocarbon oils from
petroleum and paraffin shale, &c. (at any rate in those countries
where the latter are readily obtainable), on account of the greater
cost ; but in many semicivilised lands the cost of vegetable oils
indigenous to the district is often below that of imported
petroleum burning oils, so that the mineral oils have in such
cases not yet largely supplanted the vegetable ones.
When rape (colza) oil is burnt, a tendency to charring of the
wick appears to exist if the oil contain much free fatty acids
(formed by decomposition of the original glycerides during ex-
traction and refining, <fcc.) ; this is also marked in the case of
olive oil. According to Arch butt, 5 per cent, of free fatty acids
is the maximum permissible, otherwise a defective light results,
arid the wick soon chars.
DRYING OILS USED FOR PAINT MANUFACTURE
AND IN THE PREPARATION OF VARNISHES,
LINOLEUM, AND SUCH LIKE PRODUCTS.
Drying oils, such as linseed oil, in their natural state as
obtained by expression and refining (raw oils), absorb oxygen
from the air and inspissate at much lower rates than are observed
after subjecting them to a form of treatment usually spoken of as
" boiling/' although the term is not strictly correct, inasmuch as
the oils do not become converted into vapour capable of recon-
* Flues or chimneys applied to lamps were not wholly unknown to the
ancients ; thus the lamp (of pure gold), designed by Callimachus about
400 B.C. for the Erechtheum of the Athens Acropolis, was provided with a
chimney in the form of an inverted palm tree of bronze. Argand's use of a
chimney was also previously suggested by Quinquet (Leopold Field, Cantor
Lectures, Soc. of Arts Journ., 1883, pp. 826 and 848).
314 OILS, FATS, WAXES, ETC.
densation to the original substance as water or alcohol does when
boiled, but only become partially decomposed so as to evolve
vapours in consequence of incipient destructive distillation
(p. 125) or other decomposition, more especially of the glyceridic
portion of the molecule, whereby acrolein is formed.
In the older processes for preparing "boiled" oils, this effect
was brought about by heat alone ; subsequently various sub-
stances known as "driers" were added to the oil in small
quantity for the purpose of promoting the particular changes in
view. In the more modern methods somewhat lower tempera-
tures are mostly employed, whilst the action is accelerated by
injecting air into the hot mass, whereby a greater degree of
incipient oxidation is effected, the result of which is to render
the oil much more prone to oxidise spontaneously by subsequent
exposure to air, and hence to " dry " more rapidly.
The nature of the driers used, and the exact methods of mani-
pulation are often supposed to be valuable trade secrets ; but the
practical result of working secret " rule of thumb " methods of
the kind has not always proved commercially successful. Some
of the substances used under the name of " driers " (e.g., dried
alum, and zinc sulphate) contribute but little, if anything at all,
to the drying effect, their action being simply to coagulate re-
maining mucilage, and aid its subsequent removal by subsidence.
Numerous metallic salts and oxides, <kc., are, or have been,
employed for the purpose ; according to the experiments of
Livache, the most marked effect in the way of increasing the
rate of drying is produced by manganese and lead salts, copper,
cobalt, and zinc compounds being much less active, and salts of
iron, chromium, and nickel still less so. In actual practice, com-
pounds of lead are those most frequently used, especially litharge,
red lead, and lead acetate ; the result of which is that the boiled
oil finally obtained contains lead in solution as some kind of lead
soap (to the formation of which, in the first instance, the action
of improving drying qualities is probably due, the lead soap acting
as carrier of oxygen) ; hence, more or less discoloration of paint
made with such oil is apt to occur, especially in towns, inde-
pendently of that brought about by the white lead added to most
kinds of paint. This result is avoided by substituting manganese
salts, &c., for lead compounds ; accordingly, manganese hydroxide,
dioxide, borate, oleate, oxalate, and other organic salts are now
.somewhat largely employed.*
When the drier is added in fine powder, a considerable fraction
of it can be recovered, as it settles to the bottom when the oil is
allowed to cool and stand ; but a portion is taken into solution
as metallic soap and permanently retained in the oil. Apparently
* According to K Clarke (Journ. Soc. Art*, Feb. 10, 1893, p. 289), boiled
oil prepared with manganese is unsuitable for varnish making, as it produces
a bloom on any varnish made with it.
DRYING OILS. 315
this soap absorbs oxygen from the air, and then in some way
parts with it again to the glycerides present ; but the precise way
in which the carrying action is effected is not thoroughly under-
stood. In some cases, if too large a proportion of metallic soap
is formed, the boiled oil produced is deteriorated, probably because
the oxidising action then gets carried too far. By the use of the
drier in the form of a solution of known strength, any required
proportion can be readily introduced; manganese oleate or
linolate, or other fatty acid manganese soap, dissolved in oil of
turpentine or similar solvent, is accordingly coming into use for
the purpose,* more especially for oils intended to mix with zinc
white or other pigments of light tint where darkening is desired
to be avoided, such as is liable to be produced in lead-containing
oil by the action of sulphur compounds in the air. Moreover,
oils " boiled " with manganese driers are generally of a lighter
colour than when lead is used. Occasionally, to meet trade pre-
judices as regards colour, a mixture of lead and manganese com-
pounds is used, so that the darker red tint produced by the lead
may be developed to an extent proportionate to the quantity of
lead employed.
The proportion of driers employed is usually but small, not
exceeding 0-25 to O75 per cent, of the weight of the oil (a few
Ibs. per ton) ; when used in the solid form it is important that
they should be in the finest possible state of division, for which
purpose they are usually subjected to a process of levigation after
continued grinding ; finally, they are ground with oil, much
as paint is ground, so as to form a mixture that can be readily
disseminated through the mass of oil treated by means of
agitators.
In the older method of " boiling," the oil is simply heated
along with the driers for some hours to a temperature varying
from 200° to 250° C., free fire being, used as the heating agent.
Fig. 76 represents the kind of arrangement employed ; a lid, e,
is arranged, capable of being lowered on to the pan, a, and
closing it up airtight by means of the flanged rim, b b, so that in
the event of the evolved vapours taking fire they can be almost
instantaneously extinguished. To avoid frothing over, the part
is originally filled not more than half full with oil.
Fig. 77 represents a pair of steam heated kettles, the jackets
being strong enough to resist several atmospheres pressure :
usually 4 to 5 atmospheres are employed, the oil being heated to
1 30° 0. or a little upwards. When air is blown through the hot
* Hartley & Blenkinsop's process (Patent No. 11,629, 1890) combines the
drying action of manganese soap added in this form with the bleaching
action produced by blowing a current of air through the mass at a tempera-
ture a little short of 100° C. ; by using only a small proportion of manganese
linolate solution, the oxidising action can be almost wholly confined to the
colouring matter, so as to bleach the oil without producing any notable
degree of other oxidation (Journ. Soc. Arts, loc. ctt. supra).
316
OILS, FATS, WAXES, ETC.
oil a dome-shaped cover is fitted on to keep in splashes, provided
with an exit pipe for the vapours evolved.
An improved vessel for boiling oil and suitable for many other
kindred purposes has been recently described by T. Frederking.*
Fig. 76.
A coil of stout piping is arranged in a casting mould so that the
molten metal forming the pan is cast round the coil ; much as is
done in the case of the water-tuyeres of a blast furnace. Steam
at any required pressure being passed through the coil, the pan
* Chemical News, Jan. 27, 1893 : German Patent No. 63,315.
BOILED OILS. 317
is heated up proportionately without any danger, the pressure
bearing solely on the piping and not on the metal pan itself,
whilst the well-conducting metal walls allow the heat to pass
readily. Temperatures up to 350° and 400° C. can be thus
obtained.
According to C. W. Vincent * the use of air alone without
driers does nothing towards making oil " drying." Linseed oil
heated for three days consecutively at a high temperature in
presence of the air but without driers required the same time to
dry as the raw oil from which it was prepared, but the " body "
was much increased. Heating alone for the same time with only
surface exposure to air produced no such increase of body ; the oil
became more greasy, less penetrative, and less drying.
The exact nature of the changes taking place during the boiling
of drying oils is not clearly understood ; beyond the fact than an
incipient alteration is produced (either by decomposition by
Fig. 77.
heat, or by oxidation, or both together, largely assisted by the
carrier action of the driers), which tends in the direction of the
further changes effected by the absorption of oxygen whilst
drying, little is known with certainty. No considerable destruc-
tion of glycerides appears to occur until the action is pushed
very far, ordinary "boiled" linseed oil furnishing nearly the
same amount of glycerol on saponification as raw unboiled oil ; on
the other hand, a more or less distinguishable small diminution
in iodine absorbing power is generally brought about indicating
oxidation. For the further changes effected during actual
"drying," see pp. 129, 134.
In the manufacture of printing ink, the action is pushed
considerably further. In the older direct-firing process (still
preferred by many) the oil is heated until the escaping vapours
* Muspratt's Dictionary of Chemistry, edited by C. W. Vincent, p. 475,
vol. ii.
318 OILS, FATS, WAXES, ETC.
will fire freely; the mass thickens considerably as the action
progresses ; when a sample taken out and dropped on a cold
porcelain surface can be drawn into strings half an inch long,
a cover is put on to extinguish the flame ; amber or rosin is
then dissolved in the hot oil, and slices of soap (essential in
order to enable the ink to adhere to damp paper) ; and finally
the pigment (lamp black, ivory black, <fcc., mixed with prussian
blue or other coloured pigments to tone the black as required).
Obviously in this case the heat causes a partial decomposition of
the oil, and the thickening is probably due largely to an action
of polymerisation taking place in the nascent acids or anhydrides,
thus formed, somewhat analogous to that which occurs during
the "vulcanising" of oils by the action of sulphur chloride, &c.
(p. 154).
The varnishlike film of oxidised oil produced when boiled
linseed oil is made to form a thin coating on a suitable large
surface 'freely exposed to the air can be increased to an almost
indefinite extent by painting a second film over the first when
approaching dryness, and so on in succession. The product thus
formed is largely employed in the manufacture of linoleum and
floorcloth, thin sheets of canvas or cotton scrim being suspended
vertically in a room freely supplied with air, and " flooded " with
oil from an overhead reservoir or tank running on wheels like a
travelling crane ; the sheets thus moistened with a film of oil
are kept suspended with free access of air, and when the coating
is nearly dry, alternate floodings and exposure to air are
repeated for some weeks until the "skin" formed is sufficiently
thick, the chamber being supplied with warmed air if necessary,
so as to keep its temperature up to at least 70° F. = 21° C., and
freely ventilated, much acrid vapour (acrolein, £c.) being evolved
during the oxidation by the destruction of the glyceridic portion
of the oil. The oxidised oil thus formed is heavier than water
(raw linseed oil has the specific gravity -935 or thereabouts), and
forms a yellow translucent mass, insoluble in alcohol, ether,
chloroform, and carbon disulphide ; boiling naphtha (under
pressure) softens it so that it can be worked into a paste. For
the manufacture of linoleum the skins are ground between rollers,
and heated with rosin and kaurie gum in a mixing pan, and the
resulting paste or "cement" then intermixed with rasped cork
and ultimately spread upon a canvas backing.
Notwithstanding the loss of weight due to the evolution of
acrolein and other volatile products during this process, a gain
in weight averaging about 11 per cent, is experienced, so that
the fixation of oxygen is considerable. In order to shorten
the time requisite for the oxidation of drying oils for linoleum
manufacture, F. Walton* forces air at a pressure of 5 to 10
atmospheres through the oil warmed to about 100° F. = 37° C.,
* Patent Specification No. 12,000, July 31, 1890.
BLOWN OILS. 319
the air current being divided by means of perforated plates ;
an agitator is provided, by means of which the product when
approaching solidification is more or less granulated, whilst fused
gums, &c., can be incorporated.
Blown Oils. — Of late years the manufacture of oils oxidised
by the direct action of air upon them, has acquired a considerable
magnitude, the effect produced usually being a considerable
increment in density and viscosity, rendering nondrying or
semidrying oils (rape, cotton seed, fish oils, &c.) more suitable
for use as lubricants, either directly or as ingredients in lubri-
cating mixtures : and in the case of drying oils (more especially
linseed oil), bringing about more rapidly and certainly those
incipient oxidation changes requisite to produce more rapid
spontaneous absorption of oxygen from the air by the oil, when
spread out in thin layers — i.e., the changes effected in socalled
" boiled " oil, rendering it better applicable for the production of
paint and varnish, <fcc., owing to its more rapidly "drying" up
to a comparatively hard varnish-like coating when thus applied.
The plant employed for the process is of simple construction,
consisting of a pan or tank fitted with a steam jacket (or an
internal dry steam coil) for heating up the oil, and with a false
bottom perforated with numerous small holes, cullender-fashion ;
air being pumped in under the false bottom rises up through the
hot oil in numerous minute streams of bubbles. Instead of a
false bottom, a horizontal serpentine with numerous pin holes is
sometimes employed. When the action is intended to be carried
to the limit, as in oxidising drying oils for linoleum making, an
agitating arrangement is also added for the purpose of breaking
up clots, and keeping the mass well stirred up (supra).
The nature of the chemical changes taking place during the
action of air on hot lard oil, cotton seed oil, rape oil, &c., has
not been thoroughly elucidated ; a considerable amount of heat
is developed during the process, so that, when once started, no
further extraneous heating is requisite, but in some cases rather
the converse, otherwise the temperature may rise so high as to-
injure the product by incipient decomposition. In all probability
the olein present (or other homologous glyceride) becomes largely
converted into the glyceride of an oxyoleic or oxystearic acid,
either analogous to the ricinoleic acid of castor oil (i.e., an
unsaturated hydroxylated acid), or more* probably constituted
like anhydrodioxystearic acid (pp. 42, 46), where the oxygen is
directly added on in the same way that iodine or bromine is
added, so as to convert an unsaturated acid into a saturated
derivative ; for in proportion as the oxidation proceeds, the
iodine absorption lessens. Other subsidiary actions, however,
also take place ; thus, the proportion of insoluble acids (Hehner
number) lessens as the oxidation goes on, whilst increasing
amounts of soluble acids are formed; the mean saponification
320
OILS, FATS, WAXES, ETC.
equivalent of the blown oil is usually less than that of the
original oil (i.e., the "total acid number" increases), although
but little increment is brought about in the "free acid number."
Blown oils develop much more heat on mixing with sulphuric
acid than the original untreated oils.
The following figures were obtained by Thomson and Bal-
lantyne* in the course of a series of experiments on the oxidation
of rape and sperm oils by blowing hot air through them : —
RAPE OIL.
Original
Partly
blown after
5 hours.
More fully
blown after
20 hours.
Commercial
Blown Rape
Oil.
Specific gravity at 15° "5,
0-9141
0-9275
0-9615
0-9672
Percentage of free acid (calcu- |
lated as oleic acid), . . \
5-10
5-01
7-09
4-93
Percentage of unsaponifiable ^ rt.Rri
0'76
2-80
matter, . . . . /
Total acid number,
173-9
183-0
194-9
197-7
Iodine number,
100-5
88-4
63-2
63-6
Specific temperature reaction )
135°
253°
(p. 149), . . • . • !
Percentage of insoluble acids ) 04. "(j
(Hehner number), . . ^
...
85-94
82-40
Molecular weight of insoluble )
acids, . . . . ( j
...
327
317
Percentage of soluble non- \ ,
volatile acids, . . . f Q'r2 <
...
9-20
11-16
Percentage of soluble volatile ( )
acids, . . . . )
0-82
1-90
Iodine number of soluble \
66-5 70-2
acids, . . . . \ ;
I
1
SPERM OIL.
Before blowing.
After blowing for
25 hours.
Specific gravity at 15° '5,
Free acid (calculated as oleic)
0-8799
1-97
0-8989
3-27
Unsaponifiable matter, .
Total acid number,
36-32
130-4
34-65
142-3
Iodine number,
82-1
67-1
Commercial blown oils usually present nearly the same density
and viscosity as castor oil, but differ therefrom in not dissolving
freely in alcohol, whilst they are readily soluble in petroleum
spirit, and mix readily with the heavier petroleum hydrocarbons,
thus enabling homogeneous .lubricating mixtures to be produced.
* Journ. Soc. Chem. Ind.t 1892, p. 500.
LUBRICANTS. 321
Castor oil itself when similarly blown, undergoes analogous
changes, becoming still more viscid, and acquiring the property
of being miscible with hydrocarbons (ordinary castor oil is
almost insoluble in petroleum hydrocarbons, &c.) ; accordingly,
blown castor oil is often spoken of as " soluble castor oil." The
same term, however, is sometimes applied to the oil treated with
sulphuric acid (Turkey red oil).
Oxygen Process. — A process has been brought out under
the auspices of "Brin's Oxygen Co." whereby commercially
pure oxygen (containing 90-93 per cent, of actual oxygen) is
used instead of air for the purpose of "boiling" linseed oil for
varnish oil and linoleum, and similarly blowing other oxidisable
oils, either in presence of a small quantity of driers, or without
them.* In carrying out this process it is found unnecessary to
blow the gas through the oil ; a steam jacketted pan is provided
capable of being closed by a cover, and containing an agitator
consisting of vertical rods or vanes moving round horizontally.
When the oil to be treated has become heated nearly to 100° C.,
the agitator is set in motion, and oxygen led in to the space
above the oil ; the splashing oil drops present a large absorbent
surface, so that the oxygen is absorbed, at first comparatively
slowly but later on with great vigour, so that although a rapid
stream of gas is delivered into the pan it is absorbed more
rapidly than it is supplied, producing a partial vacuum. As the
action goes on the oil heats greatly, so that ultimately it becomes
necessary to cool the jacket by admitting water into it. It is
claimed that the oxidising action is under better control by this
treatment, and that a superior result can be effected in a much
shorter time, so that the extra cost of the oxygen gas is amply
recouped.
A somewhat similar process has been subsequently patented
by E. Opderbeck f for making '; consistent fish fat, train, and
other oils," by heating them to 90°-100° C., and then intimately
commingling them with compressed oxygen.
MISCELLANEOUS USES OF OILS, FATS, &c.
MANUFACTURE OF LUBRICANTS.
The substances employed to diminish the friction between sur-
faces in motion relatively to one another are of very various kinds
according to the nature of the mechanism, £c., to be lubricated ;
thus for watches and chronometers on the one hand, and railway
axles on the other, widely different substances are respectively
* English Patent Specs., 12,652, 1886; 18,628, 1889.
t English Patent Spec., 24,153, 1892.
_ 21
322 OILS, FATS, WAXES, ETC.
best suitable ; whilst the spindles of cotton spinning jennies,
the piston boxes of steam engines, and the bearings of shafting
generally, represent other different classes of moving objects for
each of which special kinds of lubricants are requisite. Formerly
animal and vegetable oils and fats were almost exclusively used
for lubricating purposes, the finer qualities being employed for
the more delicate machinery and the coarser varieties and dirtier
greases for the greasing of cartwheels and similar rough purposes ;
the introduction of railway travelling and the extended use of
machinery of all kinds led to the modification of some of these
materials by partial saponification with lime or alkalies so as to
produce an imperfect soap containing much unsaponified fat, and
to the admixture with them of more or less viscous hydro-
carbons, more especially the "rosin oils" prepared by the
distillation of rosin, and certain higher boiling fractions obtained
in the treatment of petroleum shale oils, coal and other tars,
and similar substances. At the present day " mineral oils JJ of
this latter kind are most extensively used, either alone or in
combination with saponifiable oils, although for certain special
purposes the latter are still preferable. Obviously only those
kinds of mineral oil are available that do not readily give off
inflammable vapours on account of risk of fire, and the drying
up of the lubricant by evaporation ; moreover, lighter oils of this
kind have not sufficient " body," especially for heavy machinery.
Of the animal oils, sperm oil stands pre-eminent, neat's foot oil,
tallow, and lard oil being also valuable ingredients largely used,
and to a lesser extent whale oil and various fish oils ; whilst olive
oil, palm oil, and rape oil, and to a lesser extent cotton seed,
sesame, and groundnut oils, &c., are also extensively employed.
In all such cases it is imperative that no free mineral acid should
be present, as otherwise bearings, (fee., are apt to be rapidly
corroded : hence oils refined by acid processes (p. 259) are usually
regarded as inadmissible as ingredients in first-class lubricating
oils, unless the small quantities of admixed mineral acid have
been thoroughly removed by a subsequent washing with an
alkaline fluid. There appears also to be good reason for regarding
the presence of any considerable percentage of free organic acids
as objectionable for similar reasons, more especially in the case
of bearings made of gun metal and other copper alloys, inasmuch
as in presence of such acids the copper is apt to become oxidised,
producing corrosion and pitting • hence oils refined by alkaline
treatment are preferable. Cotton seed oil thus refined (for
the purpose of removing resin, p. 260) owes much of its value
to the circumstance that it is practically destitute of free acids,
which to a great extent counterbalances the objection to its use
that, as a considerable proportion of drying glycerides is present,
it possesses a rather marked tendency to absorb oxygen and
thicken or " gum " in use.
LUBRICANTS.
323
Animal and vegetable oils liable to contain free mineral acids,
may be conveniently examined as to the presence of such
constituents by the process described on p. 123; or the oil
may be well shaken up with distilled water, and the aqueous
liquor separated and examined, whilst the amount of free organic
acids may be determined by the titration method described on
p. 116. A practical test as to the relative tendency to gumming
is to place equal quantities (drops) of the oils to be examined on
an inclined plane, noting the distance run down by each sample
in a given time, and the time required before the oil ceases to
run, owing to the increased viscidity through oxidation ; thus,
the following figures are quoted from Appleton's Dictionary of
Mechanics, representing the run of each oil in inches : —
Sperm Oil.
i
Gallipoli
(OJive) Oil.
Lard Oil.
Rape Oil.
Linseed
Oil.
Best.
Common.
1st clay,
32
19
10
10-25
14
17-5
2nd
50
45
14
10-5
18
18
3rd
53-5
55
18
10-75
19
18
4th
54
59
18-5
10-75
19
18-25
5th
54
62
19-5
11-75
19-25
18-5
6th
54
64
20-5
Still
19-25
Still.
7th
54
67
21
...
19-75
...
8th
54
67-5
21-25
Still.
...
9th
68
21-5
...
....
...
Only comparatively small amounts of unmixed animal and
vegetable fats and oils are used alone at the present day as
lubricants ; a large proportion of the lubricating agents employed
consist of hydrocarbons only, and the remainder are much more
frequently mixtures of hydrocarbons with saponifiable oils, than
substances free from petroleum and rosin oils, and such like
hydrocarbons.
One advantage gained in the case of such mixtures (apart from
cheapness) is, that greasy rags, engine waste, &c., impregnated
with oil, are much less likely to heat spontaneously through
oxidation on storage (p. 132), when a large fraction of the oil is
nonspontaneously oxidisable hydrocarbon, than would be the
case were the oil wholly composed of glycerides and such like
saponifiable bodies.
W. Brink finds * that the solution of a small quantity of
caoutchouc in a lubricating oil consisting of mineral hydrocarbons
increases its viscosity and tends to prevent gumming, without
introducing any corresponding disadvantages. Yarious metallic
* English Patent Spec., 17,163, 1889.
324 OILS, FATS, WAXES, ETC.
soaps, more especially aluminium oleate, are often added to
lubricating oils for the purpose of increasing their " viscosity ;"
it is open to much question, however, whether such an addition
really adds to the true lubricating power of the composition, and
whether it should not be looked upon simply as an adulteration
or falsification giving a fictitious appearance of consistency to
the oil.
Lubricating materials other than pure fats and oils, may be
conveniently classified in the following divisions : —
1. Solid, semisolid, or more or less viscid liquid compositions
of animal and vegetable oils and fats, with hydrocarbons from
petroleum or destructive distillation (shale and paraffin oils), or
resin oils containing little or no inorganic matters intermixed.
2. Solid or semisolid greases containing a considerable propor-
tion of saponaceous matters (alkali or lime soaps of fatty or
resinous acids), together with more or less additional mineral or
organic " antifriction " substances (ground mica, steatite, plum-
bago, seaweed jelly, &c.)
3. Excessively coarse and generally dark coloured greases,
consisting of byeproducts of various industries, the refining of
which is too costly to permit of the materials being purified
sufficiently to enable them to be utilised in other ways — e.g.,
" Yorkshire grease," and grease from engine waste (p. 236),
containing too much hydrocarbons, &c., to be worth distilling for
socalled 'k stearine" and "oleine " (p. 277) ; "dead oils" obtained
in coaltar distillation ; certain kinds of " foots " obtained in
refining ; pitchy and tarry matters of various kinds not available
for other purposes, and so on.
Lubricants of the first class include " engine oils," " engine
tallow," and similar compositions ; "cylinder oils" for lubricating
the piston rods, &c., of steam engines ; " machinery oils " for
shafting, bearings, crank axles, and the like ; " spindle oils " for
quick moving light machinery, like the spindles of cotton
spinning jennies ; watchmakers', clock, and " turret " oils,
specially adapted for delicate machinery like chronometers, and
not liable to thicken by cold — and a large variety of subordinate
kinds. Those of the second class are chiefly compositions used
for the axle boxes of locomotive stock (railway trucks and
carriages, &c.) Coarse greases of the third class are used for
cartwheels and rough machinery, such as the pumping engines
employed in mining, where, through the circumstances of the
case, high class lubricants are unnecessary.
Lubricants of the First Class — Lubricating Oils. — The
examination as to the practical lubricating value of materials
and compositions of this class is rather a mechanical than a
chemical problem. A laboratory test greatly relied on as an
indication of their suitability for the particular purposes in view,
is the determination of their relative efflux rates at given tern-
LUBRICATING OILS. 325
peratures. The socalled "viscosity" values thus obtained by
means of one or other of the various forms of efflux viscosimeter
described in Chapter v. (or better still, the figures obtained by
means of appropriate large scale testing machines, &c., whereby
the conditions obtaining during actual use can be nearly imitated)
are generally of more practical value to the consumer than
chemical analyses of the substances; especially when coupled
with valuations of the flashing point (p. 125) and the degree of
volatility — i.e., the rate of loss by volatilisation on heating to
known temperatures. On the Continent considerable stress is
often laid on the determination of the " congealing point " (vide
p. 67). For an outline of the standard methods and appliances
in use for the purpose, vide Journ. Soc. CJiem. Ind., 1890, p. 772.
Lant Carpenter summarises the general experience gained as
to the character and behaviour of the various oils used for
lubricating as follows : —
1. A mineral oil flashing below 300° F. (149° C.) is unsafe on
account of causing fire.
2. A mineral oil evaporating more than 5 per cent, in ten
hours at 140° F. (60° C.) is inadmissible, as the evaporation
creates a viscous residue, or leaves the bearing dry.
3. The most fluid oil that will remain in its plabe, fulfilling
all other conditions, is the best for all light bearings at high
speeds.
4. The best oil is that which has the greatest adhesion to
metallic surfaces, and the least cohesion in its own particles ; in
this respect fine mineral oils are 1st, sperm oil 2nd, neat's foot
oil 3rd, and lard oil 4th.
5. Consequently, the finest mineral oils are best for light
bearings and high velocities.
6. The best animal oil to give " body " to fine mineral oils is
sperm oil.
7. Lard and neat's foot oil may replace sperm oil when greater
tenacity is required.
8. The best mineral oil for cylinders is one having specific
gravity 0-893 at 60° F. (15° -5 C.), evaporating point 550° F.
(288° C.), and flashing point 680° F. (360° C.)
9. The best mineral oil for heavy machinery has specific
gravity 0-880 at 60° F. (15° -5 C.), evaporating point 443° F.
(229° C.), and flashing point 518° F. (269° C.)
10. The best mineral oil for light bearings and high velocities
has specific gravity 0-871 at 60° F. (15° -50.), evaporating point
424° F. (218° C.), and flashing point 505° F. (262° C.)
11. Mineral oils alone are not suited for the heaviest
machinery on account of want of "body" and higher degree
of inflammability.
12. Well purified animal oils are applicable to very heavy
machinery.
326 OILS, FATS, WAXES, ETC.
13. Olive oil is foremost amongst vegetable oils, as it can be
purified without the aid of mineral acids.
14. The other vegetable oils admissible, but far inferior, stated
in their order of merit, are gingelly, groundnut, colza, and
cotton seed oils.
15. No oil is admissible which has been purified by means of
mineral acids.
A. H. Allen regards the following characters as those which
should be taken into consideration in forming an opinion as to
the suitability of a lubricating oil for a given class of work : —
1. The viscosity or "body" of the oil at the temperature at
which it is to be used.
2. The temperature at which the oil thickens or actually
•solidifies.
3. The flashing point or temperature at which the oil gives
off inflammable vapours in notable quantity.
4. The volatility or loss in weight which the oil suffers on
exposure in a thin film to an elevated temperature.
5. The " gumming " character or tendency of the oil to become
oxidised.
6. The relative proportions in which the fatty and hydrocarbon
oils of a mixture are present.
7. The proportion and nature of the free acid, if any, in the
oil.
8. The tendency of the oil to act on metals.
9. The presence of mineral matters, such as the metallic bases
of soaps, &c.
As regards the degree of volatility of a lubricating oil, J. Carter
Bell considers that it would be well for insurance companies to
lay down a hard and fast rule that no lubricating oil should be
used in any mill that has a flashing point lower than 350° F.
(177° C.), and that loses more than 5 per cent, in twelve hours at
140° F. (60° C.)
Lubricants of the Second Class — Carriage and Waggon
Greases. — For the axle boxes of railway rolling stock a peculiar
kind of imperfect soap is found to answer well, usually made by
melting tallow and palm oil together, and then thoroughly inter-
mixing a solution of sodium carbonate in water, for which purpose
Morfit's steam twirl (Chap, xix.) answers well ; or a boiled palm
oil soap is dissolved in hot water and thoroughly intermixed with
melted tallow, the emulsified mass being then cooled so as to
solidify.
Richardson <fe Watts * give the following receipts as furnishing
compositions of this kind that have been used with excellent
results, that marked "summer" running for 1,200 miles : —
* Chemistry applied to the Arts and Manufactures, vol. i., part iii.
p. 744.
LUBRICATING GREASES.
327
w
nter.
Summer.
Cwts.
qrs.
Ibs.
Lbs.
Cwts.
qrs.
Ibs.
Lbs.
Tallow, .
3
3
0
= 420 4
2
0
= 504
Palm oil,
o
2
0
= 280 i 2
2
0
= 280
Sperm oil,
0
1
7
35 0
0
27
= 27
Soda crystals,
Water, .
1
12
0
3
14
12
= 126
= 1,440
1
12
0
0
8
2G
120
= 1,370
20
2
5
2,301
20
2
5
2,301
These quantities are reckoned to give 1 ton = 2,240 Ibs. of
grease, allowing about 2J- per cent, for loss.
A. H. Allen gives the following composition of a similar
German waggon grease : —
Tallow, .
Palm oil,
Rape oil,
Caustic soda,
Water, .
24-6
9-8
1-1
5-2
59-3
100-0
The following composition, containing a smaller proportion of
saponaceous matter, has been patented by Hervieux and Bedard *
as a superior form of axle grease : —
Codfish oil,
Beef tallow,
Rosin,
Soft soap, .
24 parts.
16 „
1 „
2 ,
A somewhat analogous imperfect lime resin soap is used for
railway trucks unprovided with axle boxes, carts, and waggons,
and similar vehicles ; this is made .by elutriating slaked lime
(by stirring up with water and running the " milk of lime "
through a succession of settling tanks), and thoroughly inter-
mixing the limemud with rosin oil in the cold ; the resulting
mass is often intermixed with coarse greases and other sub-
stances of the third class, and sometimes with mineral substances
possessed of antifrictional qualities j thus the following com-
position has been patented by A. Purvis f as an improved
lubricant capable of resisting unusually high temperatures : —
Japanese tallow,
Russian tallow,
Olive soft soap,
Lard oil,
Castor oil,
Carbonate of lime,
Carbonate of soda,
* English Patent Spec., 4190, 1889.
t English Patent Spec., 13,936, I860
2 cwt.
3
2
108 Ibs.
108
10
10
328 OILS, FATS, WAXES, ETC.
The mass is heated and well intermixed, with the addition of
J cwt. of finely pulverised mica, or of china clay, or of the two
together. After standing twenty-four hours it is again heated,
and 20 Ibs. of zinc oxide added ; after thoroughly commingling
the mass is then subjected to hydraulic pressure so as to squeeze
out any water present.
Numerous analogous mixtures, consisting essentially of tallow
or oil, soap of some kind, and solid powdery matter (such as
graphite, steatite, or sulphur) are in use as antifriction com-
positions.
Greases of the Third Class. — These are the most dangerous
lubricating materials in use from the point of view of liability
to inflammation ; refuse coaltar dead oils, anthracene oils, creosote
oils, &c., have frequently a relatively very low flashing point, and
when once set on fire are not easily extinguished. Such com-
pounds should not be used at all in a mill or similar building
where great damage by fire might be occasioned.
Analysis of Lubricating Oils and .Greases. — Oils, &c.,
consisting wholly of organic matters will obviously leave no
ash on careful incineration, whereas if any soapy material or
other inorganic " antifriction " constituent be present, more or
less residue will be left when a known weight of substance is
cautiously heated (e.g., in a platinum dish) and the residual
carbon burnt off. An examination of this residue may be made
as regards the quantity of alkali contained, the amount of lime,
alumina, steatite, &c., present, and so on.
Organic suspended matters, such as Irish moss or seaweed
jelly, lime or other soaps insoluble in ether or petroleum spirit,
<fec., may be conveniently sought for by thinning the material
with the solvent, and passing through a weighed filter, finally
washing out all soluble matters ; the residue may be weighed, a
portion incinerated to obtain the proportion of inorganic matters
present, and the remainder further examined as may seem
requisite. When metallic soaps (alumina, iron, &c.) are present,
the metallic basis can be conveniently removed by thining the
grease with ether, &c., and agitating with water strongly acidu-
lated with hydrochloric acid.
When saponaceous matters are present (e.g., when the "foots"
from oil refining by alkaline processes (p. 260) are used as in-
gredients, or when lime and rosin spirit, or soda and palm oil,
<fec., are used, as with certain kinds of waggon grease), the
methods employed in soap analysis are available with suitable
modifications ; thus the total alkali present may be conveniently
found by shaking with ether and a slight excess of standard
acid (hydrochloric or nitric), separating the watery part and
back-titrating the excess of acid not neutralised. By adding
phenolphthalein to an alcoholic solution of the oil or grease,
and cautiously dropping in standard acid, and shaking after each
LUBRICATING OILS AND GREASES. 329
addition, the amount of alkali or alkaline earth present other-
wise than as soap may be at least approximately determined ;
and by further diluting with water, adding ether, petroleum
spirit, carbon disulphide, or other convenient solvent, and excess
of standard acid, the total alkali, tfcc., may be determined as
above ; whilst after separating the solution of oil in ether, &c.,
the fatty and resinous acids set free may be titrated therein in
the usual way (p. 116).
Glycerides (animal and vegetable oils and fats) and liquid
waxes (sperm oil, &c.) are determined as with ordinary oils
(p. 162) ; after neutralisation of free fatty acids (or alkalies)
excess of standard alkali is added with alcohol, and the whole
boiled some time with an inverted condenser and the alkali not
neutralised determined ; the product diluted with water and
shaken with petroleum spirit gives a watery solution of the soap
formed by saponification of the glyceride, from which the con-
tained fatty acid may be separated and subjected to examination;
whilst the petroleum spirit contains in solution the hydrocarbons
present in the original grease, together with non-fatty acid oxi-
dised matters, such as cholesterol from woolgrease, <fcc., the
higher alcohols formed by saponification of sperm oil, and the like.
When requisite these may be further examined by the acetyla-
tion process (p. 186).
As a general rule, the chemical analysis of a given lubricant
affords very little information as to its suitability for any parti-
cular purpose ; but certain laboratory determinations are often of
considerable value, more especially the determinations of rate of
loss of weight on heating to given temperatures for specified times ;
of the efflux " viscosity " at specified temperatures ; and to a lesser
extent of the specific gravity. The "flashing point" and the
somwhat higher temperature of firing ("ignition point") are also
important, especially with mineral oiis. The principal chemical
tests of practical value are those for free mineral and organic
acids, more especially the former. The chief utility of analysis
in the case of lubricating oils is to decide whether they are of
the composition stipulated for in a contract — e.g., as to containing
a given percentage of sperm oil intermixed with hydrocarbons,
and so on ; or to see whether otherwise genuine — e.g., in the case
of rape or castor oil, as to whether adulterated with other sub-
stances, such as cheaper oils or hydrocarbons ; or in the case of
blown oils whether artificially thickened by addition of soft
soap, aluminium oleate, rosin, and so on.
Occasionally it is required to find out whether rosin oils have
been admixed with mineral oil lubricants ; for this purpose the
glacial acetic test described on p. 57 may be conveniently used,
rosin oils being readily soluble in that solvent whilst mineral
oils are practically insoluble therein.
Rate of Absorption of Oxygen. — According to O. Bach
330
OILS, FATS, WAXES, KTC.
the facility with which a lubricating oil absorbs free oxygen is
a useful measure of its "gumming" tendency. By sealing up in
a glass tube containing 100-125 c.c. quantities of oil of from 3 to
5 c.c., after displacing all air by oxygen, and heating for ten
hours to 110°C., a more or less considerable absorption of gas
takes place, readily determined by opening the sealed-up end of
the tube under water, and noting the amount of inrush. Thus
various kinds of oils gave the following numbers : —
1 gramme of Valve oil (mineral)
Valveoline
Lubricating oil
Oleonaphtha
socalled "Cod oil:" sp. gr. 0 963
Olive oil
Rape seed oil
Cotton seed oil
Rosin oil
absorbed O'l c.c. of oxygen.
0-45
07
8-6
76-3
144-0
166-0
111-0
181-0
Little or no acidity is shown by the water sucked in with
mineral oils, but with others with which the absorption of
oxygen is large, a strong acid reaction is manifest, especially
in the case of rosin oil.
TURKEY RED OILS.
The chemical differences between the two kinds of oils treated
with sulphuric acid known under the name of " Turkey red oils "
have been already described (p. 143, et seq.)* In the practical
* Since that description was written a paper by P. Juillard has appeared
on the action of sulphuric acid on olive oil, and the nature of olive Turkey
red oil (Journ. Soc. Chem. Ind., 1893, p. 528, from Bulletin Soc. Ind.,
Mulhouse, 1892, p. 413). The first action at 0° to 5° is described as the
direct combination of one and of two molecules of sulphuric acid with olein
forming mixed glycerides, containing simultaneously the radicals of oleic
and oxystearosulphuric acids, and respectively indicated by the formulae —
O.CO.C17H34.0. S03H
C3H5<|O.CO.C17H33
O.CO.C17H33
and C«H,
O.CO.C17H34. O.S03H
O.CO.C17H34.O.S03H
O.CO.C17H33
By the further action of sulphuric acid, these give rise to other more
complex mixed glycerides containing simultaneously the radicals of sul-
phuric and oleic or oxystearosulphuric acids, and also that of a " poly-
merised " oleo-oxystearic acid, viz. : —
(O.CO.C17H34.O.CO.C17H33
C3HJO.CO.C17H33
( 0 . S03H
( 0 . CO . C17H34 . 0 . CO . C17H33
and C3H5 \ 0 . CO . C17H34 . 0 . S03H
( 0 . S03H
Commercial olive Turkey red oil chiefly consists of the sodium salts of these
acids and of their derivatives and products of decomposition (oleic, oxy-
TURKEY RED OILS. 331
manufacture of the castor oil products it is generally considered
indispensable to prevent the temperature from rising materially
above 35° or at most 40° C., otherwise secondary reactions take
place, leading to evolution of sulphurous acid, and production of
inferior products. The oil is run into a wooden tank, preferably
lined with sheet lead, and provided with cocks at different
heights to facilitate the running off of wash liquors, &c. ; the
sulphuric acid is then gradually run in with continual agitation,
either by hand- worked paddles or by a mechanical agitator.
Considerable differences in the practice of various makers occur
in this stage of the process, the precise details of working being
usually regarded as trade secrets ; in some cases the acid is run in
at one operation, more especially when the proportion employed
is smaller; in others part added at one time, and the rest at
intervals ; sometimes half being added one dav, and the other
half the next day. The proportion of acid used also varies
considerably/'5" from 15 to 40 per cent, of the weight of oil used.
After standing 14—24 hours, a solution of common salt is run in
and the whole well agitated with the object of removing excess
of free sulphuric acid not converted into compound acids, glycerol,
glycerosulphuric acid, and such like substances soluble in water,
without removing the soluble compound sulphuric acids formed,
these being much less soluble in brine than in plain water. If
during this washing the liquor become much heated, considerable
loss is brought about because dilute hydrochloric acid is formed
which rapidly hydrolyses the compound acids present ; plain
water is, therefore, sometimes used for a first washing, and brine
or, better still, sulphate of soda solution for subsequent ones. A
certain amount of soda or ammonia is then run in to the washed
oil and well admixed, so as to neutralise part (but usually not all)
of the free acidity ; finally enough water is added to bring down
the percentage of oleaginous matter -present to the requisite
extent, 50 or even less in some cases. The ultimate product is
consequently a sort of emulsion of undecomposed fatty matter
and free acids disseminated through a watery solution of the
soaps formed by the action of the alkali added on the free fatty
acids and compound sulphuric acids formed ; if properly prepared
so as to contain the latter in sufficient quantity, castor Turkey
red oil can be diluted with water without allowing oily drops to
separate until after standing some considerable time ; and may
be dissolved in ammonia and diluted with water without becoming
seriously turbid through separation of oil, &c. If much precipi-
tation is visible solid fatty glycerides are present, due to adulter-
stearic, oleostearic, oleo-oxystearic acids, &c. ) formed during the process
of washing out the uncombined sulphuric acid.
For a summary of the bibliography of the chemistry of Turkey red oils
vide Journ. Soc. Chem. Ind., loc. cit.
* J. A. Wilson, Journ. Soc. Chem. Ind., 1891, p. 26; 1892, p. 495.
332 OILS, FATS, WAXES, ETC.
ation of the original castor oil with rape or cotton seed oil,
&c.
According to P. Loch tin * the risk of spoiling the product
prepared from castor oil and sulphuric acid by overheating is
much less than is commonly supposed, firstly because no decom-
position involving the formation of sulphuric acid is produced at
temperatures not exceeding 70°, excepting that due to albuminoid
impurities ; and secondly, because in his view only the free fatty
acid is of use in the dyeing process, some of the best preparations
only containing 2 to 5 per cent, of sulphuric anhydride (SO3) per
100 of fatty acids (ricinoleosulphuric acid theoretically corre-
sponds with a ratio of 80 parts S03 to 298 of ricinoleic acid, or
27 per 100). Moreover, the product of saponification by alkali
(necessarily containing no compound sulphuric acid) gives very
fine shades in practical dyeing, although the tendency to frothing
causes the colour to be a little uneven. The alkali added, he
considers, should be ammonia and not soda or potash, because in
printing steam colours the alkali is volatilised and the free fatty
acid left on the cloth. In winter 20 to 30 parts, and in summer
15 to 20, of concentrated sulphuric acid are used (in Russia) per
100 of castor oil ; about one half of the acid is stirred gradually
into the oil during nine hours of a working day \ the mixture is
allowed to stand all night, and the next day the rest of the acid
is stirred in and the mixture allowed to stand until a sample
taken out exhibits a clear solution, when a few drops are shaken
with distilled water in a test tube : if allowed to stand too long
a cloudy fluid is obtained, just as when the action has not been
sufficiently prolonged. At the proper time, an equal bulk of
cold water is added to the fluid, when the oil separates and floats
on the diluted acid solution ; if a larger proportion of free fatty
acid (hydrolysed sulphuric compounds) is desired, hot water is
used instead of cold.
Formerly this hydrolytic decomposition was usually regarded
as the chief thing to be feared and avoided in manufacturing
Turkey red oils ; but recently such oils have been placed on the
market under the name of "oxyoleates" by Messrs. Schmitz <fc
Tcenges, of Heerdt (Dlisseldorf), in the preparation of which the
salted out fatty acid is purposely heated to 105° to 120° C.,
whereby practically all sulphur is eliminated in the form of
sulphurous and sulphuric acids. f According to P. Werner,!
these products are, for certain applications, superior to the usual
Turkey red oils containing sulphurised acids.
Analysis of Turkey Red Oils. — In order to hydrolyse the
compound sulphuric acids present, a weighed quantity is agitated
with about twice its volume of saturated brine, and about one-
* Journ. Soc. Chem. Ind., 1890, p. 498.
t English Patent, 14,430, 1891.
I Journ. Soc. Chem. Ind., 1893, p. 40.
ANALYSIS OF TURKEY RED OILS. 333
tenth its volume of strong hydrochloric acid, whereby hydrolysis
is speedily brought about ; the product is then shaken up with
ether, the ethereal solution evaporated to dryness, and the residue
purified by solution in alcohol and nitration to remove saline
matters, and evaporation till all alcohol is driven off (J. A.
Wilson). The residue is examined so as to determine the
amount of unaltered glycerides present along with the free acid
by the ordinary methods described on pp. 116, 157. The pro-
portion of ricinoleosulphuric acid originally present is ascer-
tained by determining the total amount of barium sulphate
obtained from the acid brine, and subtracting therefrom the
amount present as ordinary sulphate obtained by agitating
the oil with brine and ether in the same way, but without the
addition of hydrochloric acid. Obviously the weight of com-
pound sulphuric acid deduced from the corrected weight of
barium sulphate thus obtained will be very different according
as it is reckoned as ricinoleosulphuric acid or diricinoleosulphuric
acid (p. 146), 233 parts of barium sulphate corresponding with
378 parts of the first and with 658 of the second, and con-
sequently with 518 parts of a mixture of the two in equivalent
proportions.*
Another mode of determining the relative proportions of
sulphurised and non-sulphurised acids present is to titrate with
standard alkali twice, using litmus as indicator in one case, and
phenolphthalein in the other ; the sulphurised acids are given
by the first titration, and the others by the difference between
the two. Scheurer Kestner recommends ammonia as the alkali,
notwithstanding the uncertainty of the indications of phenol-
phthalein therewith.
Juillard f condemns this method of examination as giving
inaccurate results, in the light of his own more recent re-
searches (supra; vide also p. 147), more especially when
diricinolein sulphuric anhydride is present, as is usually the
case. He considers that the essential determinations are those
of the fatty acids in the usual way, and of sulphuric acid and
glycerol after hydrolysis of the oil by boiling with dilute
hydrochloric acid. In view of the different shades yielded in
dyeing and printing by the various components of the oil, a
determination is desirable of the molecular weights of the
fatty acids present in the soluble and insoluble states. This
may be accomplished by Raoult's method, care being taken to
use enough water to bring into solution the whole of the
* 402 was found by Scheurer Kestner as the equivalent weight of mixed
compound sulphuric acids formed in one case, 480 being the corresponding
value of the non-sulphurised acids simultaneously produced (riciuoleic
acid = 298 ; diricinoleic acid = 578).
-\Journ. Soc. Chem. hid., 1892, p. 357; from Bulletin Soc. Chim., Paris,
1891, 6, p. 638.
334 OILS, FATS, WAXES, ETC.
soluble acids. As usually prepared, Turkey red oils contain
some 45 or 50 per cent, of oil capable of being separated
by means of hydrochloric acid and brine, the balance being
water and small quantities of saline matter, &c. Of the
separated oil generally about one-fourth consists of unaltered
glycerides. The alkali added is usually insufficient to neutralise
all the free acid, as a rule only about one-third being neutralised.
On addition of water and ammonia to the product a clear
emulsion or solution is formed if solid glycerides are absent ;
but a more or less turbid fluid on account of precipitation if
these are present through use of adulterated oil, ttc.
In order to examine Turkey red oil (from castor oil) for
adulteration with cotton seed oil and other glycerides, J. A.
Wilson recommends (loc. cit. supra) that a weighed quantity of
oil (100 grammes) should be saponified by boiling with methy-
lated spirit (250 c.c.) and pure caustic potash (20 grammes) for
an hour, with inverted condenser attached ; after evaporating off
the alcohol, the residue is dissolved in half a litre of water, and
the soap decomposed with a slight excess of sulphuric acid, boil-
ing the whole for an hour. To avoid bumping, a piece of pumice
stone coiled round with platinum wire should be placed in the
flask. After standing, the fatty acids are collected by siphoning
off the acid liquid through a filter, and washed several times with
hot water, and then dried at 100°, and examined further. The
specific gravity at 98°, as taken with a Westphal balance, varies
considerably according as the fatty acids are derived from castor,
olive, or cotton seed oil ; thus —
Castor oil acids, . . . 0 "892 at 98° C.
Olive oil acids, . . . 0'851 ,,
Cotton seed oil acids, . . . 0'872 ,,
The fatty acids derived from pure castor Turkey red oil, not
sophisticated with any other oil, do not deposit more than traces
of solid matter at 15° -5, whilst much more is obtained with olive
oil, and still larger amounts with cotton seed oil. The melting
points of the latter two acids, when tested by the capillary tube
pressure method after solidification, are —
Cotton seed oil acids, . . . 44° C.
Olive oil acids, .... 40° C.
The neutralisation numbers of the fatty acids do not differ
much —
Castor oil acids, . . . 180 to 184
Olive oil acids, ... 173 to 170
Cotton seed oil acids, . . . 171 to 175
The iodine number of the castor oil acids is very variable, being
dependent on the age of the castor oil, and the method of pre-
paring the Turkey red oil, especially the amount of sulphuric
ANALYSIS OF TURKEY RED OILS.
335
acid used ; so that no indications of any value as regards adul-
teration can be derived by its means.
The acetyl test, on the other hand, gives indications that are
of service in this direction : the fatty acids are boiled for an hour
and a half with four-fifths their weight of acetic anhydride with a
reflux condenser, and the acetylised product washed with hot
water till the washings are neutral to delicate litmus paper. A
weighed quantity of the acetyl product is then exactly neutralised
with alcoholic potash in the cold (whereby the " acetyl acid
number" is obtained, p. 187); excess of potash is then added
(about 1| times the first amount), and the whole boiled half an
hour to saponify acetyl derivatives, the unneutralised potash
being finally titrated. The amount of potash neutralised during
this second part of the titration (acetyl number) varies consider-
ably, according as pure castor oil has been employed, or castor
oil admixed with olive or cotton seed oils ; so that whether the
observed " acetyl number " is wholly due to the saponification of
acetyl derivatives, or (as seems more probable, p. 189) is partly
due to the hydration of anhydrides formed by the action of acetic
anhydride on fatty acids, in any case it affords a means of
detecting adulterations ; thus Wilson gives the following aver-
ages:—
1
1
Acetyl Acid
Number.
Acetyl Number.
Sum (socalled
"Acetyl Saponifi-
cation Number").
Castor oil maximum, .
,, minimum, .
I Olive oil, .
| Cotton seed oil, .
144-0
149-2
1587
179-0
143-4
138-7
106-3
53-0
287 '4
287-9
265-0
232-0
These acetyl numbers are considerably higher than those yielded
by the fatty acids obtained on saponifying olive and cotton seed
oils not treated with sulphuric acid, quoted on p. 188, suggesting
that either a considerable amount of oxystearic acid, or some
analogous substance, is formed by the action of sulphuric acid on
olein and saponification of the product ; or else that the forma-
tion of anhydrides under the influence of acetic anhydride takes
place more readily with the fatty acids obtained after treatment
with sulphuric acid, than with those formed by the saponification
of the original oils.*
Hydrocarbons (petroleum, rosin oils, Arc.) are easily detected
* In all probability, the modification of the acetyl test proposed by
Lewkowitsch (determination of "distillation acetyl number" instead of
"titration acid number," pp. 190, 198) would give better results than
those obtained by Benedikt and TJlzer's method, errors due to formation,
of anhydrides being thus eliminated.
336 OILS, FATS, WAXES, ETC.
in Turkey red oil by the process ordinarily used for the purpose
described on pp. 119, 124.
CURRIERS' GREASE, SOD OILS, AND DEGRAS.
During certain operations for tanning and currying skins,
various forms of oil and grease are worked into the skin
mechanically, and the excess subsequently removed, partly by
pressure, partly by the emulsifying and saponifying action of
alkaline solutions. When these fluids are decomposed by an
inorganic acid an oily mass results, partly consisting of free fatty
acids and partly of undecomposed glycerides. When tallow has
formed part of the original grease or "dubbin" employed, the
resulting recovered grease is of thicker consistency than that
obtained when only liquid oils have been employed, such as olive
oil, whale or cod oil, or menhaden oil. The greases thus obtained,
or regained by pressure only, are sometimes known as " sod oils "
or "degras"; when cod oil and similar substances are absorbed
in skins and exposed to the air, a certain amount of oxidation is
brought about rendering the regained oil even better for use than
the original unoxidised material ; accordingly it is sometimes the
practice (more especially in France) to prepare sod oil (Moellon)
for currying by absorption in skins used solely for the purpose,
and subsequently wrung out again after sufficient exposure to
air. Part of the good effect produced by sod oil and grease that
has been already used previously is supposed by some to be due
to the presence of tanning matters therein dissolved out from the
leather and contained in a condition peculiarly adapted to the
finishing of the tanning process in another skin ; others believe
that the beneficial effect is at least partly due to the solution in
the grease of nitrogenous matters not affected by tanning and
their subsequent removal by squeezing out the greasy solution,
especially if the operation is done hot. The recovered degras at
any rate contains more or less nitrogenous matter, which is left
undissolved as a resinoid mass when the material is treated with
light petroleum spirit ; further, a considerable amount of oxyoleic
acid (or some similar oxy acid, such as dioxypalmitic acid) is
usually present, and in the case of degras made from train oils,
more or less cetylic alcohol and similar bodies produced by the
hydrolysis or saponification of their compound ethers, together
with cholesterol ; the presence of these substances enables fatty
matters to become emulsified with water and thus to penetrate
the tissues more readily, just as in the case of lanolin applied to
a living skin (infra). *
Artificial degras and curriers' greases and dubbin are prepared
* For analyses of various kinds of de"gras, and a discussion of their general
nature, vide Journ. Soc, Chem. Ind., 1891, p. 557 ; 1892, p. 639.
LANOLIN. 337
by intermixing tallow and cod oil or similar materials, red oil
(crude oleic acid from the candle factory, Chap, xvi.) and wool-
grease sometimes entering into the composition, together with
neutral soap, or imperfectly made soap prepared by heating
together oil with an amount of alkali insufficient to saponify it
completely. These products, however, are generally regarded
as greatly inferior to that prepared by the oxidation of cod or
other fish oils in contact with skins, so that for the finer kinds
of French leather only the latter are employed.
Sod oils obtained by simple pressure from skins treated with
olive, cod, or menhaden oil are valuable when properly refined
for the lubrication of delicate machinery (clocks and watches, &c.),
not being liable to clog and thicken.
MANUFACTURE OF LANOLIN.
Wool, as cut from the sheep's back, is largely impregnated
with a greasy material, suint, the inspissated perspiration of the
animal • this partly consists of various natural potash salts and
soaps soluble in water, partly of cholesterol and isocholesterol
and their stearic and other compound ethers, and to a small
extent of cerylic cerotate, and other waxy organic matters.
When solvent processes are employed for dissolving out the
grease (e.g., by means of ether or carbon disulphide) the sub-
stance obtained by distilling off the solvent is a tarry brown
mass of unpleasant odour, of specific gravity at 15° about 0-973,
melting at near 40°, sparingly soluble in alcohol, and only very
difficultly saponifiable, as the cholesterol ethers are compara-
tively very stable ; the " woolgrease " thus obtained is usually
distilled by means of superheated steam, whereby a mixture is
produced mainly consisting of free fatty acids and cholesterol,
from which " wool stearine " is obtained by expression. Methods
for cleansing wool by means of grease solvents have not come
largely into use in Britain, it being usually considered that the
heating requisite to remove the residual solvent from the wool
does more injury than the action of soap in the ordinary wet
process of wool scouring. Opinions on this point, however, are
by no means unanimous.
On the Continent wool cleansing by means of solvents has
made much more progress, and a variety of different forms of
apparatus have been patented in which the use of ether, fusel oil,
carbon disulphide, light petroleum spirit, benzene, &c., has been
claimed.*
By treatment with water, fleeces yield a solution of potash
* For a description of Singer & Judell's arrangements in which carbon
disulphide is the solvent, ride a paper by Watson Smith, Journ. Soc. Chem.
Ind., 1889, p. 24.
22
338 OILS, FATS, WAXES, ETC.
soaps in which the cholesterol and other compound ethers, <tc.,
are emulsified; the extraction from the watery product thus
formed of a purified emulsion for medicinal purposes was de-
scribed by Dioscorides in the first century A. P., under the name
of 'OIOVKOS; a more refined preparation of the kind has of late
years been somewhat largely employed under the name of
lanolin. To prepare this material, Braun & Liebreich * subject
the suds in which fleeces have been washed (or a mixture of
woolfat and soap water forming an analogous emulsion) to centri-
fugal action, whereby a separation is effected somewhat analogous
to that produced in a cream separator ; watery soap solution
flows away, whilst a soft grease along with solid dirty particles is
retained. The former is subjected to treatment with acids, etc.,
for the recovery of the fatty acids contained in the soap
(Chap, xii.) ; the latter is purified by kneading with water,
melting, and filtration, or solution in appropriate solvents,
followed by further kneading with water until all soluble im-
purities are washed away. The purified greasy matter thus
obtained possesses a remarkable power of forming a soft lard-like
mass by the intimate commingling of water and grease so as to
form a stiff semisolid emulsion. On account of the peculiar
utility of this product as a vehicle for enabling drugs, etc., to be
passed into the body by rubbing on the skin lanolin impreg-
nated with the desired active material, and its use as an
emollient unguent, either alone or in combination with other
materials, it has of late years come somewhat prominently before
the public ; as also have various other substances differing there-
from in 110 essential particulars except the trade name, and in
possessing varying degrees of purity.
Several modifications of Braun & Liebreich's centrifugal
separation process have been subsequently introduced. In one
of these, calcium chloride, or other similar salt, is added to the
water so as to form insoluble lime salts or other metallic soaps ;
the separation of the grease is thus facilitated, whilst by means
of hot acetone the cholesterol ethers, waxes, etc., present are
subsequently dissolved out from the soaps ; after distillation
of the solvent the residual purified woolgrease is treated with
oxidising agents to remove animal odour and lighten the colour,
and is then kneaded with water till the requisite consistency
is attained. Other • processes of a fractional solvent character
are also employed to separate from the crude " anhydrous
lanolin " i* some of the waxy ingredients, and thus obtain a
product consisting principally of cholesterol, isocholesterol, and
their ethers, and in consequence better adapted to form a semi-
solid emulsion with water, suitable as an unguent, &c.
Some of the products sent into the market and sold as
* English Patent Spec., 4,992, 1882.
t Vide Levinstein, Journ. Soc. Chem. Ind., 18S6, p. 579.
LANOLIN. 339
"purified woolgrease," or under various fancy names, are of
much less desirable character than others. Levinstein gives the
following tests as those by which the purity of commercial lanolin
may be ascertained : —
1. If 2 to 3 grammes of lanolin be heated with 10 c.c. of a
30 per cent, caustic soda solution, no ammonia must be dis-
engaged.
2. 10 parts lanolin heated with 50 of distilled water must
yield a clear oil. Impure lanolin becomes frothy and turbid.
3. If oily, the lanolin thus separated must be free from
glycerol.
4. If rubbed with water with an iron spatula on a ground
glass plate, the oil must be capable of taking up at least its own
weight of water, forming a sticky and paste-like mass ; if impure,
the mass will have a soap-like smoothness, and will not adhere
to the spatula.
Langbeck * describes the following process for preparing a
purified lanolin : — The wool is washed twice in water at a
temperature not exceeding 110° F., and dried by pressure
or centrifugal action, whereby soluble potash salts are mostly
removed ; the residual wool is then scoured with a mix-
ture of potash ley and olive oil, whereby all the "woolfat''
is removed and the wool thoroughly cleansed. The watery
emulsion is evaporated and treated with alcohol of 40 to 60 per
cent., which dissolves out potash soaps, .leaving behind crude
"woolfat," purified by solution in benzene or carbon disulphide,
filtration, and distillation of the solvent. The product, after
further purification and decolorisation with animal charcoal
(preferably " prussiate waste "), and subsequently with peroxide
of hydrogen, produces an excellent white basis for pomades,
ointments, &c., containing 20 to 30 per cent, of mechanically
intermixed water. The unpurified. woolfat forms a valuable-
lubricant and leather grease.
A. Seibel has recently introduced a sulphurised lanolin f for
medicinal and other purposes prepared by heating lanolin to
120° C., with about 20 per cent, of flowers of sulphur, whereby
most of the sulphur is dissolved ; after allowing to subside, the
supernatant sulphur-containing liquid is poured off and heated
to 230°, whereby much sulphuretted hydrogen is formed, together
with the sulphurised lanolin ; like ordinary lanolin, this mixes
freely with water without separation, forming a soft semisolid
emulsion.
* Journ. Soc. Chem. Intl., 1S90, p. 356.
t German Patent, No. 56,49].
340 OILS, FATS, WAXES, ETC.
CHAPTER XV.
ADULTERATION OF OILS AND FATS, &c.
THE adulterations mostly practised in the case of oils and fats,
&c., may be broadly divided into two classes — viz., (1) those
where some weight-giving ingredient is added of wholly foreign
nature, as where an undue proportion of water is mechanically
admixed with soft fats, such as butter and lard, or where starchy
matters are added to the latter substance ; and (2) those where
the adulterant is a lower priced substance of tolerably similar
nature, as where cotton seed oil is admixed with olive oil, hemp
seed oil with linseed oil, or oleomargarine with cow's butter. In
some cases mineral hydrocarbons (petroleum distillates) or
destructive distillation oils (paraffin oils, rosin oil, &c.) are
admixed with animal and vegetable oils; or substances largely
consisting of unsaponifiable matters derived from woolgrease,
&c., with tallow and similar saponifiable solid fats ; here the
nature of the adulteration is rather of the first class than of the
second, inasmuch as by appropriate processes the adulterating
impurity may (to a greater or lesser extent) be analytically
separated from the material examined, and directly determined
quantitatively ; whereas when two closely similar natural oils,
<fec., are admixed, in most cases it is difficult, if not impossible, to
effect any quantitative separation of constituents whereby the
-extent of the admixture can be directly determined, although in
many cases the fact of the admixture, and some rough idea of
its extent, can be arrived at by indirect means — e.g., by the
alteration in the melting point of the mixed fatty acids obtain-
able on saponification, or the increase (or decrease) in the iodine
number or the saponification equivalent ; or by the production
• of some particular colour change with a given chemical reagent,
not shown by the natural unadulterated oil, &c.
In most cases of the kind, moderate certainty can only be
ensured by making comparison tests side by side with the
substances examined, and with known mixtures of pure oils, &c. ;
and here a great difficulty is at once encountered in obtaining
•standard samples of pure materials. In many instances this can
only be done satisfactorily by preparation of the standards in the
laboratory itself — e.g., by expressing hand-picked samples of
seeds, &c., so as to ensure that the seeds themselves shall not be
mixtures of various kinds, and the oils extracted shall be free
from all other sophistications. Even with all possible care in
preparing pure substances for comparison, there still remains a
certain amount of possibility of error, owing to the natural
ADULTERATION OF OILS, FATS, ETC. 341
fluctuations brought about by differences in the soil and climate,
the degree of cultivation, and similar causes. Accordingly, the
analytical detection of adulteration in oils and fats, <fec., not only
depends for the most part on very different principles from those
involved in mineral analysis, e.g., for metals, but also is a matter
permitting of much less quantitative certainty.
The methods adopted in testing commercial samples of oils,
fats, &c., necessarily vary with each substance examined, but in
general consist of a suitable selection from the various methods
above described, based on the physical and chemical properties
of the oils, £c. ($§ 2 and 3) ; more especially —
The physical texture, colour, taste, and odour of the sub-
stance examined.
The effect on polarised light, and the refractive index.
The specific gravity of the substance, or of the fatty acids
thence obtainable.
The fusing and solidifying points of these fatty acids.
The solubility in various solvents.
The efflux velocity at various temperatures.
The value of the " free acid number."
The percentage of unsaponifiable matters present (including
water, suspended substances, and inorganic matters).
The nature of the elaidin formed, and its degree of con-
sistency.
In the case of drying oils, the result of tests of rate of
inspissation through oxygen absorption.
The effect of qualitative reagents in producing colour
reactions (nitric acid, sulphuric acid, zinc chloride, &c.)
The degree of heat evolution on mixture with sulphuric
acid.
The nature and consistency of the product formed with
sulphur chloride.
The quantitative result of Kcettstorfer's test (sapoiiification
equivalent).
„ „ Hehner's test (insoluble acid
number).
„ „ Reichert's test ( volatile acid
number).
„ „ Hiibl's test (iodine number).
„ „ Benedikt and Ulzer's test (acetyl
number).
The results of various special tests applicable in certain
particular cases.
The following particulars respecting the normal properties of a
few typical oils and fats, &c., and the effect thereon of various
adulterations, will serve as illustrations of the methods usually
342 OILS, FATS, WAXES, ETC.
adopted in practice ; for more full details, and for particulars
respecting other substances, analytical treatises specially dealing
with the subject must be consulted.* The methods of analysis
applicable in the case of grease recovered from suds have been
already discussed in Chap, xn., and those employed in the case
of certain manufactured oils, &c. (Turkey red oils, butter sub-
stitutes, lubricants, &c.), in Chap. xiv. ; soap analysis generally
is dealt with in Chap. xxi.
As regards the general principles of detection of adulteration,
it 'is to be borne in mind that the object of sophistication is
essentially to sell a cheaper article at the price of a more costly
one, by admixing the former with the latter ; hence the relative
price of different kinds of oils and fats, &c., at any given time,
largely affects the question as to whether certain kinds of
adulteration are likely to be practised or not. Although con-
siderable variations in prices necessarily occur in the market
from time to time, still it is possible to draw up a rough
classification of oils, tfec., according to their relative values when
genuine. The following list is given by A. H. Allen (on the
authority of Mr. T. Duggan), indicating the usual order of price,
subject to market fluctuations : —
1. Olive oil. t/11. Colza and rape oil.
2. Sperm oil. 12. Seal oil.
3. Neat's foot oil (genuine). 13. Niger seed oil
( Bottlenose oil. 14. Linseed oil.
4 to 6. j Lard oil. 15. Whale oil.
( Castor oil. 16. Cotton seed oil.
7. Cod oil. 17. Menhaden oil.
>- ( Arachis oil. 18. Japan fish oil.
• 8 to 10. j Sesam«5 oil. ^ ] 9. Mineral oils.
.( Poppy seed oil. 20. Rosin oil.
Olive Oil. — The natural variations in the quality of genuine
oil of olives are much less marked than might a priori be
expected, considering the wide range of country over which the
olive is grown for the purpose of oil production, and the number
of varieties that have been induced by centuries of cultivation
in different climates and on different soils of the different species
of Olea. Thus 0. europcea (var. sylvestris) was alluded to by
Dioscorides as a thorny tree growing wild ('EXa/a aypta] ; but
losing its thorns by cultivation (like the sloe bush, the parent of
the garden plums), giving the variety 0. europoea (var. sativa)
or 'EA«/a r^Mtpa; which again has been the parent of numerous
distinct kinds of olive trees producing fruit of very different
sizes; thus the socalled "French" olive of the present day is
much smaller than the "Spanish" olive. Apart, however, from
these subspecies of 0. europcea grown in Greece, Phoenicia,
* E.g., Allen's Commercial Organic Analysis; Benedikt's Analyse der
Fette und Wachsarten ; the Analyst, passim, &c.
OLIVE OIL. 343
Palestine, and the south of Europe since the commencement of
the historic period, and thence introduced and acclimatised into
such parts of America, Australia, and elsewhere as possess suit-
able soils and climates, other oil-bearing species are utilised in
other countries — e.g., 0. ferruginea (0. cuspidata) in Afghanistan
and other Himalaya regions, and 0. capensis at the Cape of Good
Hope.
Even with the best known southern European varieties, notable
differences in the quality of the oil extracted are found to exist
according to circumstances, more especially according as the fruit
has thoroughly ripened on the trees, or has been plucked before
quite ripe and stored; and according as the oil has been extracted
by gentle pressure in the cold, or by hot pressure, especially when
accompanied by grinding processes whereby the stones are also
broken up and expressed : indeed the differences in quality due
to these causes appear to be quite as strongly marked as those
due to soil, climate, and degree of cultivation. The finest
qualities of all are obtained by handpicking olives from the trees,
selecting those not over ripe, but ripe enough to allow oil to
exude slightly on gentle pressure between the finger and thumb,
and pressing very gently by hand in cloths : the " virgin oil "
thus produced is subsequently agitated with water, and allowed
to stand so as to remove mucilaginous matter, the purified oil
being skimmed off. A slightly inferior, but still fine, grade of
oil is obtained by crushing ripe olives (preferably with edge-
stones, but without breaking up the olive kernels), and then
pressing cold with comparatively little pressure. The residual
marc (known in Italy as Sanza or Nocciulo) is broken up, stirred
with boiling water, and then pressed again with somewhat
stronger pressure ; the second marc (Buccia) is then ground
again with heavier millstones so as to crush the olive stones
(if this were not done at the first. crushing), and is then again
stirred up with boiling water and subjected to the heaviest
pressure attainable with the appliances used : in small mills
these are usually rough screw presses (p. 200, et seq.), but in larger
ones hydraulic presses are employed (p. 207, et seq.) Finally,
the residual oil (several per cents.) is extracted from the marc
by means of carbon disulphide or other solvents (p. 231). The
details of the processes used for extracting olive oil vary widely
in different districts and countries ; thus in some establish-
ments the stones are separated from the pericarp and the two
treated separately ; a superior oil is thus obtained from the
pulp, whilst " olive kernel oil " is extracted from the stones by
grinding them to a coarse meal and then pressing or treating
with carbon disulphide, tfec. Excepting in being darker coloured
and more unpleasantly smelling, the oil thus obtained is said not
to differ materially from the lower grade oils obtained from the
fruit pulp ; it often contains a large percentage of free fatty acids
344 OILS, FATS, WAXES, ETC.
rendering it more readily soluble in alcohol than ordinary olive
oil, thus resembling the " huiles tournantes " derived from the
pulp (infra).
In this kind of fashion several qualities of olive oil are ulti-
mately obtained, more especially "virgin" and "salad" oils of
finest flavour, generally greenish through presence of chlorophyll,
and of specific gravity near to '916 at 15° ; "huiles d'enfer," * or
somewhat lower grades of inferior flavour (sometimes with more
or less marked acrid aftertaste and disagreeable odour) ; "pyrene"
and " sulphocarbon " oils (the former obtained by hot pressing
and the latter extracted by carbon disulphide or other solvent)
generally unfit for edible purposes, brownish yellow, and of specific
gravity -920 to -925 at 15°; and "huiles tournantes" obtained
from more or less fermented stored fruit, and in consequence
considerably rancid, and containing large amounts (25 to 30 per
cent.) of free fatty acids. The denser varieties deposit solid
matters (mostly palmitin) on chilling somewhat sooner than the
lighter ones.
The total acid number of various grades of olive oil has been
found by different authorities to lie between 185 and 206,
corresponding with the saponification equivalent 272 to 303 ; the
better grades, however, generally furnish a total acid number
near to 191 (saponification equivalent 294), and an iodine number
near to 83. f Any considerable addition of rape oil would raise
the saponification equivalent materially, whilst admixture with
poppy seed oil, and to a lesser extent with sesame, cotton seed,
and rape oils, distinctly increases the iodine number. Maumene's
test (p. 147) indicates a smaller degree of heat evolution on
mixing with sulphuric acid in the case of olive oil than with
most other oils ; so that by making comparative experiments
with pure olive oil and the substance examined side by side,
indications of want of purity are obtainable ; lard oil, however,
gives about the same heat evolution as olive oil. Sophistication
with arachis oil is moderately easily detected thus,]: although
many other tests fail to show its presence.
* Socalled because the oil (mixed with water to separate mucilage by
standing) is stored in large underground tanks or reservoirs so as to avoid
exposure to air as much as possible.
t Olive oil usually consists of one-fourth glycerides of solid saturated
acids (palmitic, &c. ), and three-fourths liquid glycerides, mostly oleiii.
This composition would correspond with an iodine absorption of about 67 ;
the somewhat higher values usually found consequently suggest the presence
of a small quantity of linolic acid. In confirmation of this, Hazura and
\GriIssner have obtained small quantities of sativic acid (p. 128) from the
products of oxidation of the fatty acids of olive oil.
+ Renard's test for groundnut oil is said by A. H. Allen to be sufficiently
delicate to indicate clearly an admixture of 10 per cent, of that substance
with olive oil, although failing with only 4 per cent. The small quantity
of arachin naturally contained in olive oil does not materially interfere.
The oil to be examined is saponified and the fatty acids separated and
ADULTERATION OF OLIVE OIL.
345
Admixture with heavier oils, such as cotton seed oil, tends to
raise the specific gravity; whilst, conversely, addition of rape oil
tends to lower it ; thus Souchere gives the following table in-
dicating the effect of such admixtures on the relative density at
15° of pure olive oil : —
Specific Gravity
Percentage Added.
Oil.
at 15s of Pure
Oil.
10
20
so
40
50
Olive, . .
•9153
Colza, . .
•9142
•91519
•91508
•91497
•91486
•91475
Sesame,
•9225
•91602
•91674
•91741
•91818
•91890
Cotton seed,
•923
•91607
•91684
•'J1761
•91838
•91915
Arachis, .
•917
•91547
•91564
•91581
•91598
•91615
The elaidin test (p. 137) serves to distinguish adulteration
with many oils giving soft elaidins ; a distinct softening of the
product as compared with that obtained with pure oil treated
side by side is noticeable when only a few per cents, of poppy
seed or linseed oil are present, and with somewhat larger
proportions of cotton seed, rape seed, or sesame oils ; moreover,
the elaidin formed with pure olive oil is nearly colourless or pale
yellow, whereas much darker tints are generally produced with
adulterated oils ; based on which property are numerous modifi-
cations of the nitric acid test proposed by various observers for
the purpose of examining olive oil.
Examination of the cohesion figure (p. 48), formed when oil
is placed on water, has been recommended by Tomlinson as a-
useful test of the purity of olive oil. A drop of oil is allowed to
fall gently on the surface of pure water contained in a chemically
clean basin of sufficiently large size, at a temperature not below
15°C.; with pure olive oil the drop slowly spreads out into the-
shape of a large disc with slightly recurved edges ; little spaces
shortly appear round the edge, the film commencing to retract
again, so that the edge resembles a string of beads. The spaces
between the beads soon open out more, and the edge becomes
toothed ; portions become detached, reuniting themselves in some
dissolved in five parts of rectified spirit, and precipitated with alcoholic
lead acetate ; or the oil is directly saponified with litharge by boiling with
that substance and water. The resulting lead soaps are agitated several
times with ether to dissolve out lead oleate (hypogaeate, &c. ).; the residual
lead stearate, palmitate, and arachate are decomposed by hot dilute hydro-
chloric acid, and the fatty acid cake formed on cooling and standing, dis-
solved in five parts of hot rectified spirit per one of original oil. On cooling,
crystals of arachic acid arc deposited if earthnut oil were originally pre-
sent ; from the weight of these, corrected for solubility in the mother
liquors, an approximate notion of the proportion of earthnut oil present can
be deduced, on the assumption that 100 parts of this oil correspond with
five of arachic acid.
346 OILS, FATS, WAXES, ETC.
places to the main oil film enclosing polygonal spaces bounded
by fine beads, and covered by a dew of oil so fine as to be visible
only with difficulty. About 35 seconds are requisite for the
entire succession of changes. With sesame oil the film first
formed soon begins to contract again, ultimately forming a figure
consisting of a central spot with distinctly marked rays, between
which other smaller rayed spots appear, the whole resembling a
spider's web loaded with dew ; about 60 seconds are required to
complete these changes. Mixtures of olive and sesame oils give
figures of intermediate character, the features of the one or the
other figure predominating according as the first or the second
oil forms the majority of the mixture ; and analogous differences
in the olive oil figure are produced by admixture with other
oils.
Baudouin's test for the presence of sesame oil is to shake up
10 c.c. of the sample for some minutes with 5 c.c. of hydro-
chloric acid, specific gravity 1'17, in which 0*1 gramme of sugar
has been dissolved. On separation of the oil from the watery
liquid, the latter is found to be tinted rose colour, more or less
marked according to the proportion of sesame oil present. As
little as 1 per cent, may be thus detected if the agitation be
prolonged for at least ten minutes (A. H. .Allen). Or a lump of
sugar on which fuming hydrochloric acid has been dropped may
be shaken up with the oil. On the other hand, according to
Villavecchia and Fabris,* olive oil of undoubted purity from
various localities in Italy gives the same red coloration to the
aqueous layer as other oil to which some 5 per cent, of sesame
011 has been added ; but if the agitation be only kept up for one
minute, in the case of such pure olive oils, the watery layer
immediately separates and remains colourless for at least two
minutes ; whilst the milky oily layer remains greenish or
yellowish. If only a minute quantity of sesame oil be present,
however, this oily layer turns red; the coloration of the oil,
rather than of the watery fluid, is the distinctive part of the
test (vide also p. 153).
Becchi's test (p. 306) for cotton seed oil gives useful indica-
tions of the presence of that adulterant, provided that the
refining of the cotton seed oil has not been carried so far as to
bring about the entire withdrawal of the constituent that acts
on the silver nitrate.
In many cases evidence of adulteration is obtainable by saponi-
fying the oil, separating the fatty acids, and determining their
fusing and solidifying points (p. 69) side by side with the corre-
sponding acids obtained from genuine oil, or mixtures of knoivn
composition, as the precise numbers obtained vary according to
the particular mode of manipulation adopted. Values varying
from 22° to 29° C. for the fusing point, and from 21° to 25° as
* Journ. Soc. Chem. Ind.t 1893, p. 67.
ADULTERATION OF OLIVE OIL.
347
the solidifying point, have been recorded by different observers.
Dieterich gives the following comparative values in different
cases, using the same process throughout : —
Melting Point. Solidification Point.
Olive oil (average of
19 samples), .
26° to 28° -5 23° -5 to 24° -6
3
parts olive oil to 1
of arachis oil,
cotton seed oil,
29
30
26
27'3
sunflower seed oil,
25
20-5
sesame" oil,
28
25
linseed oil, . 24 '5
19-5
'
colza oil, . 23 0
19
The figures thus deduced, however, are rarely sufficiently deci-
sive of themselves to warrant any accurate deduction being
drawn as to the nature and extent of the adulteration.
Much the same remark applies to tests' based on the amount
of solubility in various menstrua — e.g., mixtures of alcohol, water,
and glacial acetic acid (Valenta's test, p. 55), although in certain
cases this method gives useful corroborative indications, especially
when carried out side by side with genuine oil and mixtures of
known characters.
Admixtures of hydrocarbons may be detected by completely
saponifying the oil with alcoholic soda or potash, evaporating off
most of the spirit and adding water, shaking up with ether,
separating the ethereal liquid and evaporating off' the solvent ;
with pure oil only infinitesimal amounts of unsaponified matter
(phytosterol, &c.) will be left, whereas hydrocarbon oils, if
present, will be obtained in much larger quantity after evapora-
tion of the ether. This test may be made a quantitative one by
using a weighed amount of oil and evaporating a known fraction
of the ethereal solution in a weighed vessel (vide p. 119).
Occasionally metallic compounds are found in solution in olive
oil or substances purporting to be such ; thus copper (added to
communicate a chlorophyll-like green shade) is occasionally
present. Lead compounds are said to be occasionally added for
the purpose of communicating a sweeter taste to the oil. Metallic
impurities of this kind may be detected as described on p. 122.
Several special instruments have been invented for the purpose
of examining olive oil, in order to detect adulterations, based on
different physical properties — e.g., the thermal araeometer (p. 82);
the oleorefractometer (p. 51); and the diagometer (p. 53). The
polariscope may also be utilised, olive oil being slightly dextro-
gyrate, and most other oils Isevogyrate.
Very similar processes suffice (mutatis mutandis) for the
examination of other oils of the olive class — e.g., almond oil, oil.
of ben (or behen), and groundnut (arachis) oil — and to some
extent of oils of the semidrying class, such as cotton seed oil and
348 OILS, FATS, WAXES, ETC.
sesame oil. With the cheaper oils of this kind, hydrocarbons and
deodorised fish oils are the most likely kinds of adulterants ;
the former are detected and determined as described on p. 119;
the latter largely increase the heat evolution with sulphuric acid,
and in some instances give special colour reactions with that acid
and other reagents.
Rape Seed, and Colza Oils. — Several species of Brassica
exist, and several varieties of the rape plant have been developed
by successive cultivations ; the oils from these are generally
termed indiscriminately "rape" or "colza" oils in Britain. On
the Continent, however, the different kinds are still frequently
distinguished by separate names. Thus Schadler divides these
oils into three classes, viz. : —
Colza oil (Colzaol or Kohlsaatol) from the original plaiih, " kohlsaat "
(Brassica campesfris).
L'ape seed oil (Rapsol or Rapsamenol) from a developed variety,
"raps" (Brassica campevtris var. nap us, or Brassica no pus
oleifera.
Riibsen oil (Rubol or Riibsenol) from a different variety, " rubsen "
(Brassica campestris var. rapa, or Brassica rapa oleifera.
Each class is further subdivided according as the plant is an
annual or a biennial, the former yielding " summer oils," and the
latter " winter oils." Thus—
Winter rape seed oil from winter raps (Brassica napus oleifera biennis).
Summer ,, ,, summer raps ,, ,, annua).
Winter rubsen oil from winter riibsen (B. rapa oleijera biennis}.
Summer ,, ,, summer riibsen ,, ,, annua).
Brassica nigra and Brassica alba are now more usually desig-
nated Sinapis nigra and Sinapis alba respectively (black and
white mustard), being plants different in many respects from the
cole or kohl, the seeds of which (kohlsaat) furnish the term
" colza " by corruption. Similarly, the allied Brassica juncea is
now generally known as Sinapis juncea, and Brassica cJiinensis
(Chinese cabbage) as Sinapis chinensis.
Cole or rape seed is largely cultivated in various parts of
Europe, especially France, Belgium, Germany, and Hungary ;
also in Roumania, Russia, India, and China. Much is shipped
from the Black Sea and Baltic ports, the expression being usually
carried out in large mills after the fashion described in Chap, ix.,
the seeds being crushed between rollers, steamed to coagulate
mucilage and increase fluidity, and subjected by hydraulic
pressure before cooling.
The yield is usually from 30 to 45 per cent, according to the
variety employed. Schadler gives the following averages : —
Summer rubsen and summer raps, . . .30 to 35 per cent.
Winter ,, winter ,, . . . 35 to 40 ,,
Winter colza, . . . . . . . 35 to 45 ,,
LINSEED OIL. 349
Much mucilage accompanies the crude oil ; this is generally
eliminated by the sulphuric acid refining process (p. 259), in
some cases supplemented by an alkaline treatment to get rid of
free acid, injurious for lubricant purposes.
Rape seed oil usually exhibits a total acid number of 175 to
179, corresponding with the saponification equivalent, 320 to 325,
the iodine number being 98 -5 to 105.* The fatty acids isolated
on saponification melt at 18° to 22°, whilst the specific gravity of
the oil at 15° ordinarily lies between -911 and -9175. Accord-
ingly, the usual result of adulteration with other fixed oils is a
rise in specific gravity, and a fall in saponification equivalent.
Linseed and other drying oils raise the iodine number ; fish and
drying oils increase the heat evolution on mixture with sulphuric
acid. Thus Thomson and Ballantyne found the "specific tempera-
ture reaction" (water = 100) for rape oil to be between 125 and
144, whereas that for linseed oil was 270 to 349, cod liver oil
giving 243 to 273, and menhaden oil 306 (p. 149). Pure rape
seed oil is practically immiscible with glacial acetic acid at the
ordinary temperature, and has a lower efflux velocity (higher
viscosity), than most oils likely to be used as adulterants.
Hydrocarbon oils are detected in the usual way (p. 119).
Linseed Oil. — The oil expressed from the seeds of the flax
plant (Linum usitatissimum) is generally known as linseed oil ;
usually it is extracted on the large scale in crushing mills by the
process described in Chap. ix. ; but small quantities are prepared
for home consumption in different parts of the world, more
especially Russia, on a much smaller scale. The seeds as found
in commerce are rarely all of one kind, more or less considerable
admixtures of the seeds of other plants being often present, the
result of which occasionally is to seriously impair the quality of
the oil ; this sometimes arises from intentional admixture, more
especially in the case of hemp seed, which is stated to be inva-
riably added to the extent of 5 per cent, and upwards to all
linseed shipped from the Black Sea ports ; but quite as frequently
it is accidental, on account of other plants being grown along
with flax — e.g., mustard and rape ; this is more especially the
case with the red variety of Indian seed. The presence of
mustard seed in any considerable quantity is liable to render
the oilcake acrid and unsuitable as a cattle food.
Linseed is chiefly imported from the Baltic ports, Russia
(Black Sea), and India ; but it is also grown in considerable
quantity in various parts of Europe, especially Poland, in Egypt,
and the Brazils. Seed grown in hotter climates is reputed to
yield oil comparatively defective in drying power and of lighter
colour than that produced in colder regions ; possibly, however,
* Hence, some considerable amount of linolin or other drying glyceride
must be present, since the iodine number of erucin is 72 "4, and that of
rapin (isomeride of ricinolein) 81 •?•
350 OILS, FATS, WAXKS, ETC.
this is chiefly due to« admixture of other seed oils and not to
actual differences in the oil contained in the flax seed. When
subjected to pressure, some 20 to 22 per cent, of superior " cold
drawn " oil can be extracted ; in Poland, Russia, and other
countries this is used as an article of food, being not unpleasantly
tasting. Later runnings prepared by hot pressure are darker in
colour and have a disagreeable acrid flavour, rendering them only
suitable for technical purposes. If the seeds are expressed com-
paratively "green," much more watery mucilage accompanies the
oil ; after keeping some months they dry somewhat and a better
yield of oil with a lessened admixture of vegetable extractive
matter results. Schadler describes the average yield as being —
Cold pressed oil, . . . . 20 to 21 per cent.
Hot pressed oil, . . . 27 to 28 ,,
Obtained by solvents, . . , 32 to 33 ,,
The proportion of oil obtained, however, varies somewhat wdth
the source of the seed ; thus Italian linseed yields somewhat
more than Russian, and white Indian some 2 per cent, more
than red Indian. Again, the yield varies according as the seed
has been allowed to ripen fully, or as the plant has been harvested
earlier for the flax crop, in which case a smaller yield of oil is
usually obtained.
In practice, pure linseed oil is never met with commercially,
and can only be obtained by carefully handpicking the seed
before expression. When freshly expressed, after refining by
sulphuric acid (p. 259), it has a specific gravity at 15° of
•932 to '937, averaging close to '935 (Allen) : if any considerable
admixture of rape or other lighter oil is present, the specific
gravity falls to -930 and lower. If, on the other hand, the oil is
old and has absorbed oxygen, the specific gravity is more or less
considerably raised.
Linseed oil contains some 10 or 15 per cent, of glycerides of
solid fatty acids (palmitin, myristin, &c.) The remaining liquid
glycerides consist of those of oleic, linolic, linolenic, and isolino-
lenic acids, in the relative proportions 5, 15, 15, and 65 per cent,
of the sum of the four (Hazura and Griissner). The total acid
number is variously stated by different observers at 189 to 195-2,
corresponding with a saponification equivalent of 287 to 297,
representing a mean molecular weight of fatty acids of 274 to 285.
By directly titrating the acids prepared as carefully as possible
to avoid oxidation, molecular weights varying between 282 and
295 have been observed in many cases ; but perceptibly higher
values up to 307 have been noticed in some instances, leading to
the belief that a higher homologue of linolic acid, C00H.1(3O0, was
present (p. 34).
The iodine number of linseed oil has been very variously stated
by different observers. Dieterich found different samples to give
ADULTERATION OF LINSEED OIL. 351
values between 161 '9 and 180-9 ; Benedikt found 170 to 181 ;
Holde 179 to 180 ; Thomson and Ballantyne 175-5 to 187*7 accord-
ing to the time allowed (vide p. 180). Lower values down to 149
have been recorded by other observers ; but in view of the results
of later researches on the difficulty of completely saturating
glycerides with iodine unless a considerable time is allowed and
a large excess of iodine employed, it would seem very doubtful
whether these lower values are correct : probably 180 to 185 is
nearer the true ultimate value for pure linseed oil.*
The fatty acids separable from linseed oil have been found by
various observers to melt at temperatures lying between 17° and
24°, solidifying at 13° to 17°-5 ; as linseed oil occurs in commerce,
a small proportion of these acids is usually present in the free
state, free acid numbers being obtained varying from 0*7 to 8-0,
corresponding with amounts of free acid from 0-4 to upwards of
4 per cent, of the total acids present.
Linseed oil is especially characterised by the high heat evolu-
tion brought about by admixture with sulphuric acid (Maumene's.
test, p. 147) ; in the absence of fish oils, any considerable admix-
ture of rape or other oil giving less heat evolution can be readily
detected in this way. Livache's test (p. 133) also affords an
indication as to whether semidrying oils or drying oils of inferior
quality have been admixed, inasmuch as the increment of weight
after a few days, when no further increase is noticeable, is from
14 to 15 per cent, in the case of fresh genuine linseed oil, but
considerably less if any large admixture of other oils be present.
A simpler test based on the shorter time required by genuine lin-
seed oil to dry thoroughly, as compared with adulterated samples
and other drying oils, is the "film test" described on p. 133 ; the
character of the dried film formed is also taken into account,
whether resinoid and brittle when cold, or hard and varnish-like
but tough, or inclined to be readily broken up and crumbly;
such a practical test, although not quantitative in character, is
* Assuming linseed oil to contain only SO per cent, of unsaturated
glycerides in the relative proportions given by Ha/ura and Griissner
(siipra), the calculated iodine number would be 1S2 05.
Proportional Amount Iodine Number of
Present. Glyceride.
Olein, 0-8 x -05 x 86 -20 = 3 "45
Linolin, 0'8 x -15 x 173'57 20'S3
Linolenin, O'S x -15 x 262*15 - 31 "46
Isolinolenin, 0'8 x "63 x 262*15 = 136 "31
192-05
whence it would seem probable that the proportions of linolenin and iso-
linolenin deduced by Hazura and Griissner are a little overstated, at least
so far as these values are applicable to average qualities of oil.
352 OILS, FATS, WAXES, ETC.
often of great value.* Moreover, an old sample of oil that has
already taken up some amount of oxygen, although by no means
deteriorated for many ordinary applications thereby, would be
indicated as of inferior quality by Livache's test if alone relied
on ; but would not be shown to be deficient in drying power by
the " film test." Such an oil, however, would possess a lower
iodine number than fresh oil, even if otherwise genuine, inasmuch
as the oxygen taken up appears to be largely added on to the
unsaturated carbon groups just as iodine is.
Fish oils (cod, menhaden, &c.) possess high thermal values by
Maumene's test, and high iodine numbers, so that adulteration
therewith is not indicated by either reaction. Boiling with
caustic soda develops a peculiar reddish colour when these oils
are present ; chlorine gas blown through the oil causes a great
darkening in tint not observed with pure linseed oil. The
sulphuric acid test (p. 151) gives simply a dark brown clot with
genuine linseed oil, but a reddish brown spot if fish oils are
present.
Hydrocarbons are not unfrequently added as adulterants ; of
these, mineral oils lower the specific gravity, and rosin oils raise
it, so that a suitable mixture of the two has little or no effect.
The test described on p. 119 enables this admixture to be readily
detected and the quantity determined ; if any considerable
amount is present the film test indicates the fact, as the film
remains a long time sticky with only small quantities, and never
properly hardens and dries wTith larger proportions.!
Rosin (colophony) is another adulterant often added along
with other substances ; to detect and determine this admixture
the oil is dissolved in a little pure alcohol, and the free fatty
acids and resin acids titrated by standard alkali; water is added
to the neutral mass, and the glyceridic oils separated by gravi-
tation or petroleum spirit (p. 118) ; the aqueous fluid is acidu-
lated, the mixed fatty and resinous acids separated and weighed,
and the resin determined therein, as in the case of rosin soaps
(yellow soaps, Chap, xxi.)
Hemp seed oil is a frequent constituent of linseed oil, owing
to the admixture of hemp seed with linseed before reaching the
crushing mills ; to detect such an admixture the oil is stirred
with concentrated hydrochloric acid, when a more or less marked
* The h'lm test is often modified by mixing the oil to be tested with three
times its weight of white lead, so as to form a paint which is then applied
by a brush to a clean surface ; a precisely similar trial is made side by side
with a standard sample of oil, and the rates of drying compared. If
nondrying oils be present, even in only small quantity, the rate of drying
is markedly slackened.
t Eosin oils, being strongly dextrogyrate, can be detected by the polari-
scope (p. 50), pure linseed oil being faintly laevorotatory. Sesame oil is
also dextrorotatory; the sugar test (p. 346) serves to detect it if present.
SPERM OIL. 353
green coloration is developed if hemp seed oil be present, pure
linseed oil giving a yellow colour.
Sperm Oil. — Two varieties of sperm oil proper are obtained
from the Cachelot whale (Pliyseter macroceplialus) ; one from the
blubber by the ordinary processes of rendering, the other from
the "head matter" or contents of the cranial cavities. This
latter usually contains a larger* proportion of solid constituents,
so that on standing it soon becomes more or less pasty or semi-
solid from the separation of spermaceti. This solid constituent
also deposits from the blubber oil on standing and chilling, but
to a somewhat lesser extent.
Sperm oil thus freed from spermaceti is pale yellow and nearly
odourless when prepared at comparatively low temperatures from
fresh blubber, £c. ; although, like all other fish and blubber oils,
possessed of a marked unpleasant smell and darker colour when
extracted by greater heat from partly decomposed blubber. Its
specific gravity at 15° usually lies between -875 and -884 : it has
but little tendency to become rancid, or to " gum " and thicken
by exposure to air, whilst its viscosity is but little affected by
change of temperature, so that it forms a valuable lubricating oil.
Its total acid number lies between 123 and 147, averaging near
132, corresponding with the saponification equivalent 426 ;* its
iodine number is near 84. The fatty acids obtained on saponi-
fication melt at near 13°, and possess an iodine number near 88,
and the average molecular weight 281-294 (Allen — oleic acid =
282, physetoleic acid = 254). Their specific gravity at 15° is
near -899 ; nitrous acid solidifies them readily.
On saponification sperm oil yields 60-63 per cent, of insoluble
fatty acids, separated from the monohydric alcohol simultaneously
formed which constitutes 39-41-5 per cent, (theoretical values for
cetyl physetoleate, cetylic alcohol = 50-6 per cent., physetoleic
acid 53-1 per cent. ; for dodecatyl physetoleate, dodecatylic
alcohol, 44-1 per cent., physetoleic acid, 60'2 per cent.)
Sperm oil is often adulterated with cheaper vegetable and
animal oils, the presence of which is usually detected by the
lowering of the percentage of alcoholiform constituents produced
on saponification, and by the circumstance that the viscosity of
genuine sperm oil is affected less by temperature variations than
that of most other oils, so that if other oils be present the differ-
ences between the efflux viscosity rates (p. 94) at different
temperatures (e.g., 15°C., 50°C., and 100°C.) will be considerably
increased. Further, such admixture tends to lower the saponi-
fication equivalent. Hydrocarbon oils increase the saponification
equivalent and the amount of ether residue obtained by the process
described on p. 119 ; but this residue, consisting largely of fluid
hydrocarbons, is readily distinguishable from the alcoholiform
residue obtained with pure sperm oil, more particularly by the
* Cetyl physetoleate = 478. Dodecatyl physetoleate = 422.
23
354 OILS, FATS, WAXES, ETC.
acetyl test (p. 186). Vegetable and animal glyceridic oils lead
to the presence of more or less considerable amounts of glycerol
in the products of saponification ; genuine sperm oil gives but
little. Fish and sharkliver oils give special colorations with
sulphuric acid on account of the biliary constituents present.
Tallow. — The terms " tallow " and " suet," especially the
former, are often used indiscriminately to denote both the solid
adipose tissues of various quadrupeds (more particularly the ox
and sheep), and the fatty matters thence rendered by suitable
treatment so as to separate them from the nitrogenous cellular
tissue ; preferably, however, the term " suet " should only be ap-
plied to the untreated animal fatty tissues, whilst the word "tallow"
should only imply the fatty matters thence extracted and freed
from cell walls, &c. In this sense " tallow " includes the rendered
fats obtained from the ox, sheep, goat, stag, and other quadrupeds,
excluding the horse and hog, the fats from which are generally
known as " horsegrease " (maresgrease) and "lard" respectively.
According to the breed, age, and sex of the cattle or sheep
from which the tallow is obtained, the hardness of the substance
varies ; the mode of feeding and climate also produce variations ;
whilst, as in the case of hog's lard, the consistency of the product
differs considerably with the part of the carcase furnishing the
fatty tissue. These variations, however, so far as is known, do
not affect the general character of the fat as regards its consti-
tution; whether harder or softer it essentially consists of the
glycerides of oleic, stearic, and palmitic acids, the former being
present in the larger proportion the softer the fat. In general,
veal tallow (from calves) is softer than that similarly obtained
from oxen ; whilst cow tallow and bull tallow are harder still :
these are all generally included in the term " beef tallow."
" Mutton tallow " from sheep (ewes and rams) is usually harder
than beef tallow, but not invariably : " goat's tallow " (often
included in mutton tallow) much resembles that substance. In
the trade a variety of grades exist, in many cases known by
special names either denoting the country from which the
material is shipped ("River Plate tallow," " Australian tallow,"
" Eussian tallow," &c.) or given for some other reason — e.g.,
P. Y. C. tallow = Petersburg yellow candle (or prime yellow
candle), a particular quality irrespective of source ; " Prime
Butchers' Association tallow," or " North American," mostly
shipped from New York ; " Western," imported from New
Orleans: "tripe tallow" and "town tallow," grades usually
softer and somewhat inferior because of admixture with waste
dripping, kitchen grease, and other similar materials. In many
cases large admixtures of other foreign substances are added —
e.g., cotton seed stearine ;* woolgrease and Yorkshire grease, and
* According to R. Williams cotton seed oil is often used as an adulterant
in the case of softer tallows (vide Journ. Soc. Chem. Ind., 1888, p. 186).
TALLOW. 355
the stearines thence obtained by distillation and pressure ; bone
grease ; together with solid non-fatty matters such as China clay,
whiting, starch, &c., the presence of which is easily recognised
by applying a solvent and filtering (p. 123).
The specific gravity at 15° of tallow lies between 0-925 and
0-940, values between 0-925 and 0-929 being obtained with beef
tallow, and somewhat higher ones, between 0-937 and 0-940, with
mutton tallow (Hager). Dieterich found slightly higher values
up to 0-952. The melting point and solidifying point vary
considerably, 41° to 51° being recorded by different observers for
the former, and a few degrees lower for the latter. The fatty
acids obtained on saponification also vary similarly with the
hardness — i.e., the proportion of olein, the melting point being
usually near 47° with tallow of good quality. The solidifying
point as determined by Dalican's process (p. 74), sometimes
termed the " titre " of the tallow, affords the best criterion of
quality, so far as such physical tests go: 44° represents a mixture
of equal quantities of stearic and oleic acids, lower values being-
obtained when oleic acid preponderates, and higher ones when
stearic acid is in excess. On the Continent, it is often stipulated
that the solidification point shall not fall below 44° when the
tallow is intended for candlemaking ; whereby not only are the
softer genuine (or comparatively so) tallows excluded, but also
those largely adulterated with such substances as cotton seed
oil, cotton seed stearine, Yorkshire grease, stearine from dis-
tilled grease, £c., as the presence of these materials tends to
lower the melting point of the mixed fatty acids obtained.
Woolgrease and Yorkshire grease products are especially ob-
jectionable in this connection, because they contain more or less
considerable quantities of cholesterol hydrocarbons and other
unsaponifiable substances, which not only directly diminish the
amount of stearic acid present, but also further diminish the
quantity of solid fatty acids obtainable by pressing, as they
interfere with the proper "seeding" or crystallisation of the
press cake (vide p. 367). The determination of these unsaponi-
fiable matters in tallow adulterated therewith, is carried out as
described on p. 119.
Fresh tallow contains very little free fatty acid ; but tallow
that has become more or less rancid often contains considerable
amounts, up to 12 per cent, (calculated as oleic acid); 25 per
cent, was found by Deering in a sample six years old. When
tallow is not particularly rancid, and yet contains a considerable
amount of free acid, it is very probable that it has been
adulterated with distilled " stearine " (largely consisting of free
fatty acids). The total acid number usually lies between 193
and 198, representing the saponification equivalent 283 to 293,
averaging near 288, and corresponding with a mean molecular
weight of fatty acids of near 276 (palmitic acid = 256, oleic
356 OILS, FATS, WAXES, ETC.
acid = 282, stearic acid — 284). The iodine number has been
found by different observers to lie between 35 and 45, with an
average of about 40 ; since pure olein has the iodine number
86 "2, this indicates an average amount of olein. of somewhat less
than 50 per cent, (about 46), and a proportion of solid glycerides
of somewhat above 50 per cent, (about 54). According to the
author's experience, in the absence of adulterations the deter-
mination of the iodine value can be made into a useful test of
quality for candlemaking purposes, the proportion of solid fatty
acids obtainable being greater the less the iodine absorption ;
but when pressed coker butter or palm kernel oil has been
added, the iodine number is reduced without a corresponding
increase in amount of solid fatty acids of high melting point
obtainable ; and the same remark applies to wToolgrease, wool
stearine, and similar substances. When circumstances permit, the
best indications as to adulterations of this kind are obtained by
saponifying, separating the fatty acids, allowing them to crystal-
lise, and expressing them in a small experimental laboratory
press, determining the quantity and melting point of the press
cake, and subjecting the expressed oleic acid to examination as
regards its iodine absorption, elaidin reaction, colour reactions
with sulphuric and nitric acids, tfec., heat evolution with sulphuric
acid (Maumene's test. p. 147), amount of unsaponifiable matters
present, and so on ; samples of genuine tallow of different
qualities being examined side by side in the same way.
Muter and Koningh* recommend a process based on somewhat
similar principles, where the solid and liquid fatty acids are
separated by conversion into lead salts and solution of lead oleate,
&c., by ether, wherein lead stearate and palmitate are but
sparingly soluble. By carrying out the saponification and subse-
quent processes in a uniform prescribed way, the quantity and
characters of the liquid fatty acids ultimately separated from the
soluble lead salt, afford useful indications respecting adultera-
tion. Thus, they found that the iodine number of the liquid
acid obtainable from pure tallow, is uniformly close to 90,
substantially identical with that theoretically requisite for pure
oleic acid. Lard, on the other hand, gives a liquid acid possessing
a distinctly higher iodine number, close to 93; whilst the liquid
acids from cotton seed oil give a considerably higher iodine
value, near to 135.
Tallow that has become rancid by keeping generally whitens
during the process ; owing to the large amount of decomposition
with formation of free fatty acids that occurs (supra), such tallow
is unsuitable for lubricating purposes ; the byeproducts of the
decomposition, moreover, cause soap made from such tallow to
" work foxy," or become discoloured of a brownish red, so that
for milled or other toilet soaps intended to be white or tinted
* Analyst, 1889, p. 61 ; 1890.
BEESWAX. 357
delicate shades, such tallow should be avoided in the manufacture
of the " stock soap " used.
Beeswax. — A good deal of dispute has taken place at various
times as to whether the wax of the bee, wasp, and similar insects
is a distinct product of secretion due to their own special life
action, or is simply precontained in the pollen and nectar of
flowers, &c., serving as their food, and isolated therefrom by
digesting away or otherwise removing the other constituents.
This latter view appears probable, inasmuch as when bees are
fed upon sugar only, they appear to be incapable of developing
wax to any notable extent. On the other hand, although the
character of bee food necessarily varies much in different parts
of the world, yet the chemical constitution of beeswax does not
differ anything like so widely. Samples of beeswax from numerous
localities in Europe, Asia, South America, and Australia, all pos-
sessed very similar compositions (Hehner*) — viz., they essentially
consisted of a mixture of about 1 part of free cerotic acid to 6 of
myricin (vide infra) ; a result hardly compatible with the notion
that the wax pre-existed as such in the pollen and nectar of the
very wide variety of flowers, &c., furnishing food to the bees
in these different quarters of the globe. Andaquia wax (wax
of Apis fasciata, largely used for candlemaking in South
America) appears to be substantially identical with the ordinary
beeswax of Apis mellifera ; and the same remark applies to
Antilles wax (Apis fasciata ?), and to Madagascar wax (Apis uni-
color), although frequently beeswax of tropical and subtropical
origin is darker coloured and less readily bleached than that
produced in more temperate climates. f The wax of the Eastern
Archipelago, again, differs but little from that obtained from
other sources, although mainly produced by a different species
(Apis dorsata).
In order to obtain beeswax the ^ombs are simply drained of
honey and then melted in hot water and stirred about ; the wax
collects on the top as an oily layer, which is removed after cooling
and hardening ; after remelting by heat alone (without water)
and casting into blocks, the "virgin" wax is ready for the
market. A large proportion is used for numerous purposes
without further preparation ; for certain purposes bleaching is
requisite, effected either by means of exposure to air and sunlight
in thin shavings (p. 268), or by means of chemicals, preferably
dilute sulphuric acid and potassium dichromate (p. 266).
Beeswax is readily soluble in carbon disulphide and fusel oil ;
it dissolves in about 10 parts of boiling ether, less completely in
cold ether, benzene, or petroleum ; in cold alcohol it is nearly
* Vide Analyst, 1883, vol. viii., p. 16.
t Wax from the vicinity of Bordeaux appears to be the variety most
difficult to bleach; whether from some local peculiarity in 'the flowers
frequented by the bees; or for some other reason, is unknown.
358 OILS, FATS, WAXES, ETC.
insoluble, but dissolves in about 300 parts of boiling spirit. In
the case of most solvents, some parts of the wax dissolve much
more freely than other portions ; thus in the case of hot alcohol
a small quantity of " cerolein " is left undissolved, consisting of
fatty matter, principally palmitin and olein ; the proportion of
this constituent varies in waxes of different origin, but is never
large, so that the presence of fatty glycerides in any quantity is
only due to adulteration. Natural wax contains a considerable
amount of free acid (from 12 to 16 per cent., calculated as cerotic
acid — Hehner) ; that bleached by means of dichromate usually
contains somewhat more (17 to 18 per cent.) ; but airbleaching
appears to produce no measurable increase in the free acidity.
The free acid in raw wax appears to be chiefly cerotic acid,
C2-H54O2, together with a little melissic acid, C30H"6002, ; by
treating the wax with limited quantities of hot alcohol these are
dissolved out, myricin (the palmitic ether of myricylic alcohol,
iC30H61 . O . C16H0jlO) constituting the great majority of the un-
dissolved part.
Beeswax has at 15° C. the specific gravity nearly -96 (numbers
varying between '956 and '975 being recorded by different
observers). At 98° to 99° the specific gravity is '818 to '827
(Allen). Airbleaching seems to produce little or no alteration
in the density, but chemically bleached wax is usually rendered
a little more dense by the process. The melting point is always
close to 63°, values varying between 61° and 65° being recorded
by numerous observers ; the melted substance re-solidifies at one
or two degrees lower than the temperature of complete fusion.
The free acid number has been found by Hehner, Hiibl, Buisine,
and other observers to be subject to comparatively little varia-
tion, almost invariably lying between 17 and 21 in the case of
unbleached wax, corresponding with 12*5 to 15*5 per cent, of
cerotic acid) ; whilst the ester number (p. 162) lies between 72
and 76 (corresponding with 87 to 92 per cent, of myricin) ; the
sum of the cerotic acid arid myricin thus calculated is generally
a little above 100, showing that some amount of other consti-
tuents of lower molecular weight is also present. In confirma-
tion of this the iodine number has been found to be appreciable,
though low, averaging about 10 (8*3 to ll'O, Buisine), indicating
the presence of a perceptible amount of unsaturated compounds
(possibly hydrocarbons). On saponification with continued boil-
ing (for at least an hour) with excess of alcoholic potash, genuine
beeswax furnishes 53 to 54 per cent, of crude myricylic alcohol
(Benedikt), corresponding with 81 '8 to 83'4 of myricin (myricylic
palmitate).*
* Wax bleached by the air process is often admixed with a few per cents,
of fatty matter which seems to facilitate the bleaching action in some way
not thoroughly understood. A small quantity of oil of turpentine is some-
times added for the same reason ; in this case the bleaching is probably
SPERMACETI. 359
Beeswax is often largely adulterated, more especially with
paraffin wax and allied hydrocarbons (cerasin and similar high-
melting mineral waxes) ; stearic acid ; colophony, burgundy
pitch, and other similar resinous matters ; and solid weighting
materials, such as china clay, barium sulphate, yellow ochre,
starch, and sulphur. Vegetable waxes (carnauba wax, &c.) are
often added ; and in some cases several per cents, of water are
artfully worked into the mass. This last admixture is readily
detected by the methods described in Chap, vi., p. 122. Mineral
adulterations are readily detected by incinerating the wax and
burning off carbonaceous matters so as to obtain the clay, &c., as
residue. By dissolving in ether, warm oil of turpentine, chloro-
form, benzene, or other suitable solvent, these substances, as
well as starchy matters, and other analogous adulterants, are left
undissolved, and may be obtained by filtration and washing.*
Stearic acid, if added in any quantity, is detected by the increased
free acid number, and by the melting point and general characters
of the acids ultimately obtained from the soap formed on shaking
the wax with hot alcohol, and titrating with standard alkali and
phenolphthalein (p. 118). Glycerides, similarly, may be detected
and, to some extent, estimated by the formation of glycerol on
saponification ; whilst adulteration with carnauba wax may be
detected by the examination of the fatty acids formed by saponi-
fying the impure myricin left insoluble on agitation with alcohol
and alkali, palmitic acid (m.p. 62°, and equivalent 256) being
the chief constituent formed from genuine wax, whilst carnauba
wax mostly produces cerotic acid (m.p. 79°, and equivalent 410).
The presence of hydrocarbons is indicated by the decreased ester
number ; or the wax may be carbonised by heating 5 grammes
with 50 c.c. of concentrated sulphuric acid to 130° 0. in a
capacious flask for ten minutes ; much sulphurous acid, &c., is
evolved, and the mass chars, finally becoming nearly solid ; the
acid is washed out with water, adherent water removed by
alcohol, and the residue treated with ether, preferably in a Soxhlet
tube (p. 238), whereby the hydrocarbon is dissolved out, along
with a little wax that has escaped the action of the acid. By
repeating the acid treatment this is removed, and the cerasin, &c.,
finally obtained in a weighable fcjrm.f
Spermaceti. — The true origin of spermaceti (formerly regarded
as whale-spawn, Sperma ceti) appears to have been unknown,
quickened by the formation of peroxide of hydrogen during the oxidation
of the turpentine by the oxygen of the air in contact with water (ride p. 269).
* Traces of flour are often normally present in pressed or rolled wax
owing to the use of flour for dusting over the rollers or press to prevent the
wax from sticking (Allen).
t Respecting the detection of adulterations of beeswax, vide Journ. Soc.
Ohem. Ind., 1890, p. 771 ; 1891, pp. 728, 729, 860, 1014. For the
bibliography of beeswax and the waxes used for its adulteration, vide ibid.,
1892, pp. 756, 757.
360 OILS, FATS, WAXES, ETC.
long after it had come into some amount of use for the prepara-
tion of unguents ; its employment for candlemaking, like that of
whale oils for burning in lamps, seems practically to date from
somewhat upwards of a century ago when the whale fishery
began to be extensively pursued for commercial purposes. Even
at the present day, however, considerable misapprehension
appears to exist both as to the species of cetacea yielding it
and the part of the body from which it is derived. Whilst the
best known source is the "head matter" of the Pltyseter macro-
cephalus (p. 300), which largely consists of solid crystallised
spermaceti when taken from the dead carcase, it is also the fact
that considerable quantities are obtainable from the blubber oil
of the same cetacean ; during winter this oil sets so far solid by
deposition of spermaceti that it requires to be steamed to enable
it to be removed from the casks. Moreover, analogous if not
identical solid deposits form on similarly chilling for lengthened
periods the blubber oils of various other species (vide p. 301).
The semisolid oils containing scales of spermaceti will not bear
any great degree of pressure during filtration to separate the
solid matter, as this very readily passes through even the most
impervious filter cloths : accordingly the first operation consists
of " bagging " — i.e., the material is placed inside long bags of hair
or canvas where gravitation only effects a separation between
the solid and liquid constituents. The "bagged sperm" is then
transferred to square bags, forming a soft flaky mass : a pile of
bags and boards is formed in successive alternate layers, and by
placing weights on the top of the pile, at first small but subse-
quently greater, most of the remaining fluid oil is gradually
squeezed out until the mass is sufficiently firm to bear hydraulic
cold pressure carried out in presses closely akin to those used
for stearine After cold pressing, the sperm cake is remelted,
granulated, and pressed several times over at gradually increasing
pressures and temperatures so as to remove the last portions of
fluid oil, a refining treatment with potash (p. 261) being inter-
polated between the last pressings so as to remove not only the
last traces of colouring matter, but also free fatty acids formed
by hydrolysis. Finally, a glistening white mass is obtained,
mainly consisting of cetylic palmitate (016H31 . O . C16H33O),
melting at near 45° C.,* and of specific gravity near '810 at 99°.
The pressings from these various operations are methodically
worked up, in such fashion as ultimately to obtain a second
quality of spermaceti of somewhat lower melting point : the
potash foots obtained during refining yield on acidulation with a
mineral acid a mixture of impure spermaceti and palmitic acid ;
* According to L. Field (Journ. Soc. Arts, vol. xxxi., p. 840), the
spermaceti extracted from the blubber oils of the true bottlenose whale
(Balcena rosirata) has a slightly higher melting point than that from the
sperm whale or cachelot (Physeter macrocephalus).
SPERMACETI. 3G1
when this is worked up with the other runnings a considerable
amount of free fatty acids is contained in the ultimate product.
30 per cent, and upwards of such free acids (essentially palmitic
acid) are sometimes present in spermaceti of this lower grade.
Spermaceti is sometimes adulterated with free stearic and
palmitic acids (not derived from the foots, as above described),
hard pressed glycerides (pressed tallow), and animal waxes and
paraffin wax. These latter additions raise the saponification
equivalent, whilst free fatty acids and glycerides lower it. The
detection of these adulterants is effected in ways substantially
the same as those above mentioned with respect to beeswax.
362 OILS, FATS, WAXES, ETC.
§ 6. The Candle Industry.
CHAPTER XVI.
MATERIALS USED IN CANDLEMAKING.
ORIGIN OF CANDLES.
IN all probability the earliest forms of illuminating agents of the
nature of candles (i.e., containing something serving the purpose
of wick surrounded by more or less solid combustible matter
adherent thereto) were simple links or flambeaux consisting of
fibrous vegetable stalks, &c., soaked in natural bitumen or
asphalt, vegetable resin, or animal fatty matter ; these being-
obvious developments of the yet simpler primeval torches con-
sisting of splinters of pine and similar woods, either naturally
full of resinous matter, or externally smeared therewith.
Lamps, or reservoirs of fluid oil furnished writh a wick for
burning, seem to have been invented at a very early period of
the world's history, and to have speedily superseded the primeval
resinous wooden torch for general household purposes amongst
the earlier civilised nations, although for outdoor illuminations,
and especially amongst the Scandinavians and other northern
tribes, pine splinter torches and similar rude contrivances of the
flambeau character were still chiefly used.
Rushlights, where the pith of rushes served as wick and where
the combustible matter was tallow or other animal fat applied
by dipping the pith in melted grease, and superior forms where
wax was used instead of tallow, moulded by hand round the rush
whilst rendered plastic by means of warmth, * appear to have
been in considerable use amongst the Romans, hempen or flaxen
unspun wicks taking the place of rush pith in the better kinds of
wax lights ; thus in Herculaneum the remains of a chandler's
•establishment have been unearthed, whilst numerous passages in
various Latin authors indicate that the torch (tceda), the lamp
{lucerna), the tallow candle or rushlight (sebaceus), and the wax
* Such a candle, believed to date from the 1st century, is in the British
Museum.
CANDLE MATERIALS. 363
light (cereus) were all in use in the early centuries of the Christian
era;* the oil lamp being still the most extensively used illuminant
amongst the well to do classes, wax lights ranking next.
With the exception that wax tapers were largely used for
ecclesiastical purposes, as well as private illumination, during
the middle ages, and that some improvements were consequently
introduced as regards their general size and finish, little advance
in the art of candlemaking seems to have been brought about
until the fifteenth century, when the process of "moulding" was
introduced by the Sieur de Brez ; but the manufacture of rush-
lights and of " dip " tallow candles, as well as of waxen tapers,
had by that time become a trade of itself, having to a consider-
able extent passed out of the region of ordinary household
operations carried on by each family for the supply of its own
wants, and into the hands of special candlemakers (candelarii, or
chandlers), who made tallow and other candles for sale to the
general public, at any rate in the larger towns. In country
districts, however, rushlights and tallow candles, of more or less
rough home-made manufacture, still continued to be the only
available means of artificial illumination other than oil lamps,
for the great majority of the population; a state of matters,
indeed, not entirely obsolete even at the present day in some
highly rural localities. In some savage countries highly olei-
ferous nuts, strung together on a fibrous twig, are burnt like
candles ; as one is consumed the next one becomes lighted and
burns till exhausted.
Combustible Materials. — At the present time the com-
bustible matters (in addition to the wicks) used for candle-
making may be divided into four classes — viz., (1) those natural
glycerides which are sufficiently solid at ordinary temperatures
to admit of being used for the purpose, or which yield sufficiently
solid glycerides by pressure; more especially tallow and similar
animal fats, together with vegetable products of corresponding
consistency, such as coker stearine, piney tallow, and the solid
fats of the Stillingia, Bassia, and other genera. (2) Substances of
waxy character, such as beeswax and the vegetable waxes, essen-
tially consisting of nonglyceridic compound ethers ; also including
spermaceti. (3) Free fatty acids of sufficiently high melting point,
obtained from natural oils and fats by saponification processes,
and mechanical separation of more fluid ingredients. (4) Paraffin
wax and analogous hydrocarbons of mineral origin, or formed by
destructive distillation. Of these the substances of the latter
two classes are those most largely used, more especially the last,
in this country, although "stearine" candles are somewhat pre-
ferred on the Continent. The trade in wax and spermaceti
candles is comparatively small, although by no means insigni-
* Vide Leopold Field, "Cantor Lectures, " Journ. Soc. Arts, vol. xxxii.,
p. 821, et seq.
364: OILS, FATS, WAXES, ETC.
ficant in actual amount ; whilst the use of unsaponified glycerides,
whether as tallow " dip " candles, consisting of such glycerides
only, or as " composite '' mixtures of glycerides and free fatty
acids, is steadily diminishing in favour of the other kinds of
illuminants, although far from being extinct, especially in the
case of iiightlights, which are largely made of coker stearine.
In the manufacture of tallow dip candles no special preparation
of the tallow for use is requisite further than the rendering and
purifying processes already described (Chaps, x. and xi.) ; the
harder varieties are usually preferred, although if too hard there
is more risk of cracking. In the case of beeswax, air and light-
bleached wax (p. 268) is employed in preference to that bleached
by chemical processes, especially such as involve the use of chlor-
ine ; for, irrespective of a greater tendency to become yellowish
on keeping, such chemically bleached waxes are apt to possess a
crystalline grain which spoils the appearance of the candle, and
when bleached by chlorine, to give off fumes of hydrochloric acid
when burnt, owing to the formation of chloro-substitutioii com-
pounds during the bleaching process. Paraffin wax and the
analogous waxy hydrocarbons obtained from ozokerite, &c.,
require no further treatment for caiidlemaking other than the
pressing and purifying processes gone through during their
manufacture for the purpose of raising the melting point to the
requisite extent (compare p. 230). The isolation of solid free
fatty acids from natural glycerides, however, is a somewhat
complex operation capable of being carried out in several ways.
MANUFACTURE OF "STEARINE."
The numerous processes proposed, and more or less actually
used on a manufacturing scale for the isolation of solid fatty
acids from appropriate glycerides, may be classified under the
following heads : —
1. Processes where the glycerides are saponified by alkalies,
alkaline earths (such as lime), or other suitable basic materials,
by boiling under ordinary pressure ; to effect which operation a
more or less considerable excess of base is usually found necessary
in order to complete the saponification.
2. Processes analogous to the preceding, except that the opera-
tion is carried out at a somewhat higher temperature obtained
under increased pressure ; excess of base is in this case unneces-
sary, for, in general, practically complete saponification and
hydrolysis can be thus easily brought about even when consider-
ably less base is present than is chemically equivalent to the
fatty acids formed, and although the temperature does not rise
sufficiently high to decompose any considerable fraction of the
glycerol set free.
MANUFACTURE OF STEARINE. 365
3. Processes where hydrolysis is effected under the influence
of acids, especially sulphuric acid ; in this case the liberated
acids are usually distilled over by the aid of superheated steam,
so as to separate them from nonvolatile pitchy matters formed
as bye products ; in Bock's process (infra} this distillation is
unnecessary. More or less glycerol is usually destroyed by the
action of the acid.
4. Processes where hydrolysis is brought about under the
influence of water alone (under great pressure, or as highly
superheated steam). In these processes the glycerol is often
largely destroyed by the heat (sometimes completely so), a much
higher temperature being requisite than in the case of methods
of the second class.
The Chevreul-Milly Process — Alkaline Saponiflcation
Process in Open Pans under Ordinary Pressure. — The first
attempts to utilise solid free fatty acids for candle material, were
made about 1825 by Chevreul and Gay Lussac, employing
alkalies (potash and soda) to effect the saponification of tallow ;
for a variety of reasons, this process proved to be commercially a
failure ; but a few years later, by substituting lime for alkalies
and otherwise employing more suitable arrangements, M. de
Milly succeeded in making the manufacture of " stearine "
candles from tallow a sufficiently remunerative undertaking to
render it a practical industry. As carried out at the present
day, the process differs little in essential points from what it was
more than half a century ago, the chief differences lying in the
scale on which the operations are effected, and the frequent use
of mixtures of vegetable and other substances with tallow (e.g., a
mixture of palm oil and tallow or other suitable fatty matters)
instead of tallow only,* a better quality of mixed fatty acids
being thereby usually obtained — i.e., a mixture which allows the
solid acids to crystallise and "granulate" more readily, so as to
be more easily pressed for the separation of liquid acids.
The fatty matters being generally purchased in casks, by means
of a steam jet applied at the bunghole, the fats are melted out
into a tank, whence they are pumped or run by gravitation into
the decomposing pan, usually constructed of wooden staves
(preferably of oak) strongly bound together, and forming a large
tub or tun, sometimes lined with sheet lead. This is provided
with a stirring arrangement, consisting of a central vertical shaft
with arms carrying paddles and rakes, so as to intermix the
contents thoroughly (Fig. 78). Quicklime, in the proportion of
12 to 15 pounds per 100 of fat, is mixed with water to a cream
and run into the tun,f and the whole heated up by steam blown
* In France the use of palm oil is much less frequent than in Britain, thus
leading to some slight differences between many kinds of French "stearine,"
as compared with British.
t Assuming the mixture of fatty matters to have a mean saponification
3G6
OILS, FATS, WAXES, ETC.
in through a perforated horizontal coil at the bottom of the tub,
or a series of jets distributed over the bottom, and the whole
kept agitated for some hours, [a cover being placed over the
tub to keep in splashes,
and steam being blown
through gently so as to
keep the whole boiling.
Glycerol is thus set free,
and a mixture of lime-
salts formed (mostly
stearate, palmitate, and
oleate), practically in-
soluble in water, and
solidifying on cooling to
a hard mass known as
"rock;" the aqueous
glycerol solution or
"sweet water" is run
off and utilised for
glycerol extraction.
To isolate the fatty
acids, the rock is boiled
Fig. 78.
up in a lead-lined vat with steam, diluted sulphuric acid bein^
added in slight excess of the quantity requisite to saturate
all the lime present.* Sulphate of calcium separates out,
whilst the free fatty acids swim up to the top ; after standing
and cooling somewhat, these are skimmed off and boiled up,
firstly with highly dilute sulphuric acid to decompose the
last traces of lime soap, and then with water, using wet steam,
so as thoroughly to wash out all sulphuric acid and admixed
mineral matters. Finally, the fluid fatty acids are transferred
to shallow cooling pans, such as the series indicated in Figs.
79 and 80. Here the melted fatty acids are run from a
trough, F, through nozzles, D D D, into the uppermost of the
pans, C C C, supported by a wooden framework, A A, and iron
crossbars, B B B. When the pans are filled, the stream of melted
equivalent of 280, the quantity of liine (CaO) theoretically equivalent to the
fatty acids formed would be 28 parts per 280, or 10 per cent. ; with fatty
matters of higher saponification equivalent, proportionately less lime would
be required, and vice versa. Some excess of lime, however, is requisite in
order to ensure tolerably complete action ; moreover, in practice, quicklime
is not pure CaO, a little moisture, calcium carbonate, and more or less
siliceous and clayey matter being present, all of which are inert so far as
effecting saponification is concerned. A first class quicklime, made from a
pure limestone, may contain (when freshly burnt) some 95 per cent, of CaO
(exclusive of calcium carbonate) ; but 85 to 90 per cent, is more nearly the
usual average, and less with very poor limes.
* For every 56 parts of actual lime, CaO, used, 98 parts of actual
sulphuric acid, HJ304, are required ; roughly, 2 parts of B.O. V. (brown oil
of vitriol) to 1 of quicklime.
STEARINE ; CRYSTALLISATION.
367
matter is shut off by means of the spigot, E. In these cooling
pans they solidify to a semicrystalline mass on cooling and stand-
ing ; for the purpose of pressing out the fluid acids, this solidifi-
cation is best allowed to take place in metal dishes, so that the
solid cakes formed are obtained in the form of slabs about an
inch or three-fourths inch thick, and of such size as to fit into the
cake boxes of the hydraulic press used ; the temperature during
«• M U 4!
Fig. 79.
Fig. 80.
this period should lie between 21° and 32° C. (70° to 90° R), so
that whilst the "seeding" or crystallisation of the solid acids
(mostly stearic and palmitic) may take place completely, as little
oleic acid as possible may be retained in the body of the crystals
formed. The slabs of " separation cake " finally consist of a
spongy mass of granular or crystallised solid acids, with liquid
oleic acid (containing solid acids and colouring matters in solu-
tion) disseminated through the interstices. By enveloping them
in press cloths, and placing them in the cake boxes of a hydraulic
press, the brownish liquid acids are gradually squeezed out, and
the comparatively colourless solid crystals retained. Instead of
directly pressing the granulated cakes, it is often preferable to
rasp them into shreds by a machine, and to press the raspings ;
a more complete expression of liquid acids is thus brought about.
The press cake left, however, still retains a certain amount of
368
OILS, FATS. WAXES, ETC.
liquid acids, rendering its fusing point too low ; to remove these
the press cakes are melted by steam, cast afresh into slabs in
shallow trays, allowed to stand to granulate at a temperature of
about 30° C., rasped to coarse powder, and again pressed in a
different machine where the cake boxes are heated by the regu-
lated admission of steam into the plates, in the body of which
channels are hollowed out for the purpose. Fig. 81 represents
n form of horizontal hot press thus arranged, steam being ad-
mitted to the plates by the pipes, E E. A A A represent the
packets of raspings undergoing pressure ; B the piston of the
hydraulic ram working in the cylinder, C ; D the framework ;
P a chain whereby the plates are drawn asunder for the removal
of the cakes when the operation is finished ; G water supply
pipe to ram cylinder from accumulator. The temperature of the
hot press varies somewhat with the kind of material employed,
but is generally not far from 50° (122° F.) for stearine of high
JIM.
Fig. 81.
melting point ; for inferior stearine melting more easily, the
temperature is proportionately lower.
The hot press cake finally obtained is melted by means of steam
along with a little water acidulated with sulphuric acid, and then
vigorously agitated with the acid fluid for some time for the
purpose of removing traces of lime salts still retained ; finally
the acid liquor is run off, and several successive boilings-up
•carried out with plain water. The purified mixture of stearic
and palmitic acids is then cast into blocks for use in the candle
factory ; small quantities of vegetable wax, beeswax, £c., are
sometimes added to "break the grain" — i.e., to prevent the
formation of visibly large crystals during solidification.
Even when the fatty matters employed are highly rancid and
impure, an almost perfectly white " stearine " can be thus manu-
factured by the lime process. The yield of pure solid hot pressed
acids, however, is materially influenced by the presence and
OPEN PAN PROCESS.
369
nature of abnormally large proportions of oleine (existing in
softer fats, &c.) or other substances (e.g., woolgrease), not only
on account of the diminution in amount of solid fat acids present,
but also because of the increased amount of these acids removed
in the "red oils" (vide infra).
Fig. 82 represents a general view of the disposition of the
apparatus used in the
saponification of fatty
matters by the open pan
process.* A, tub from
which lime is emitted.
B, leadlined vats with
steam pipes for boiling
lime and fats. C, similar
decomposing vats where
the rock is boiled with
sulphuric acid. D D, rack
holding pans for caking
mixed acids. E, cold
press. F, hydraulic
pumps. G, pan for re-
melting press cake. H,
hot press. I, vat for
melting hot pressed
stearine for final wash-
ing with water and cast-
ing into blocks.
Moinier and Boutigny
modify the Chevreul-
Milly process by sub-
mitting the melted tal-
low, &c., to a preliminary
treatment with hot water
and a current of impure
sulphur dioxide (pro-
duced by the action of
hot sulphuric acid on
sawdust, charcoal, &c.) ;
after an hour the lime-
cream is added and the
whole well agitated,
whereby the mass in-
creases in consistence
with considerable froth-
ing, by and bye becoming pasty. The sulphur dioxide is then
shut off and the rock finished by boiling up with steam, ifcc., as
usual. The yield of fatty acids is stated to be thus increased
* L. Field, Journ. Soc. Arts, vol. xxxi., p. 859.
24
370 OILS, FATS, WAXES, ETC.
by some 4 per cent. The hot press cake is finally refined by
boiling up first with water acidulated with sulphuric acid, then
with water alone, white of egg (1 egg per 100 Ibs.) being intro-
duced whilst boiling so as to coagulate and remove impurities
as in clarifying coffee, &c.
On p. 375 are given some analyses of original fatty acid mixture,
cold press cake, and hot press cake, £c., illustrating the eifect of
the process in separating oleic acid from the solid fatty acids,
and the increment inf melting point thus effected. The hot press
grease usually contains enough solid fatty acids to raise its fusing
point to at least that of the original mixture of fatty acids before
cold pressing ; it is generally worked up along with fresh fatty
acids by fusing therewith and granulating the mixture in trays for
the cold press. The outer edges of the hot press cake retain some
amount of more fusible grease, and are therefore usually pared
off and worked up along with the rest of the hot press grease.
The "red oil" or "oleine" running from the cold press contains
a considerable quantity of palmitic and stearic acids in solution,
the precise amount depending on the temperature at which the
pressing is conducted ; on chilling somewhat, more or less solid
fatty acids separate, usually in a finely divided form. When it
is desired to obtain red oils containing as large a proportion of
oleic acid and as little solid acids as possible, the oil is chilled
and the resulting somewhat pasty mass passed through a filter
press, such as shown in Figs. 56, 59, the greasy solid fatty
acids thus obtained being worked up with fresh batches of the
original mixture of acids ; for the manufacture of oleine soap
this treatment is not indispensable, but inasmuch as the solid
fatty acids are considerably more valuable than the fluid ones,
it is obviously desirable to obtain as large a proportion of the
former as possible. For the same reason it is essential that the
saponification of the fats used should be as nearly complete as
possible, not only because all the stearic and palmitic glycerides
that escape saponification are lost so far as solid fatty acids are
concerned (being expressed fluid during the pressing operations),
but also because their presence tends to prevent the proper
crystallisation of the solid acids, and thus to increase the pro-
portion of these contained in the red oils. In actual practice, it
is impossible to carry the decomposition in open pans to absolute
completeness without seriously prolonging the operation, which
entails extra cost ; so that a few per cents, (and sometimes much
more, up to 10 or 12 per cent.) of the glycerides used are gener-
ally left undecomposed in the rock, ultimately finding their way
into the red oils.
When the tallow used has been adulterated by mixing in
woolgrease or similar material containing unsaponifiable matters,
these substances are generally also ultimately contained in the
red oils, thereby diminishing the proportion of " stearine '*
COMPOSITION OF "ROCK." 371
obtainable, partly because of the smaller proportion of solid
glycerides present in the adulterated tallow, and partly because
the presence of woolgrease, like that of unsaponified fat, tends to
interfere with the crystallisation of the acids, and hence causes
the red oils to retain more solid acids. Moreover, when the red
oils are made into soap, a deteriorating effect (for certain pur-
poses) is brought about in the resulting soap j on solution in
water and standing, soap containing such unsaponifiable matter
is apt to throw up an oily film, rendering the solution liable to spot
and grease goods rinsed through the soap solution. Accordingly,
it is preferable to buy tallow by analysis, the price varying accord-
ing to the proportion of solid fatty acids present (estimated by
Dalican's process, p. 74, or otherwise) and deductions being
made for unsaponifiable constituents. As yet, however, this sys-
tem does not seem to have been widely adopted in this country.
Composition of "Rock." — The following analyses represent
the general composition of open pan "rock" as obtained on the
manufacturing scale ; A being normal rock made from genuine
tallow mixed with about one-fourth its weight of palm oil ; and
B rock from tallow adulterated with woolgrease containing a
considerable amount of cholesterol and other unsaponifiable
matters : —
A B
Lime present as lime soap (CaO),
Lime used in excess (CaO),
Fatty anhydrides* present as lime soap,
Unsapoiiined glycerides, .
Unsaponifiable organic matter,
Water and carbonic acid (C02), combined with
the excess of lime; sand and grit, &e
uncombined water (moisture),
7-50 6-27
1-95 241
73-30 61-20
5-55 8-40
2-75 12-00
8-95 9-72
100-00 100-00
Since 100 parts of triglycerides of mean molecular weight near
285, represent about 92 parts fatty anhydrides, the fatty anhy-
drides present in these two samples represent respectively about
80 and 66 parts of original glycerides per 100 of rock j hence
the proportion of glycerides originally used which remain
5*55
unsaponified are (A) -7- - x 100 = G'5 per cent, and
v ' 80 + 5-55
(B)— — - x 100 = 11 '3 per cent. — i.e., in the first case
6t> + O"4:0
about Jg-, and in the second about l, of the original glycerides
escaped sapoiiification.
* "Fatty anhydrides "= fatty acids, less an equivalent of water —
p.g., in the case of stearic anhydride ^ j85Q J- 0 ; so that the sum of the
fatty anhydrides and the lime combined with them as lime soap, represents
the actual amount of lime soap present. In the above two instances the
amounts of lime soap are (A) 73'30 + 7'50 = 80 35 ; (B) 61'20 + 6'27 = 67 '47.
372 OILS, FATS, WAXES, ETC.
Analysis of Hock. — This is conveniently effected by taking
a known weight of an average sample and boiling it with water
to which an excess of standard acid (preferably hydrochloric) has
been added, until completely decomposed ; on standing, the
liberated fatty acids, £c., form a cake on the top, which is care-
fully removed, dried, and weighed ;* the free fatty acids therein
are then titrated in alcoholic solution with standard alkali, and
the examination for admixed glycerides and unsaponifiable
matters proceeded with, as in the case of separation cake (vide
infra, p. 378). The excess of acid in the watery fluid is back
titrated, so as to obtain the acid neutralised by the total lime
present, which is thence calculable ; whilst the lime present
as lime soap (combined with fatty acids) is similarly calculated
from the amount of alkali neutralised by the fatty acids. For
example, 10 grammes of a given sample of rock were boiled with
water and 50 c.c. of normal acid ; on back titration 16 '7 c.c. were
found to be unneutralised ; hence 33*3 c.c. were neutralised,
equivalent to 0-932 CaO = 9*32 per cent, of total lime. The
separated fatty acids, &c., weighed 8-215 grammes, and neutralised
25'9 c.c. of normal alkali, equivalent to 0*725 gramme, or 7 "25
per cent, of CaO ; whence 0-932 - 0-725 = 0*207 gramme of
excess of lime was present, or 2*07 per cent. On further ex-
amination (p. 378) the separated fatty acids were found to con-
tain 0*535 gramme of unsaponified glycerides and 0*235 grammes
of unsaponifiable matters. Hence the actual fatty acids pre-
sent in the 8*215 grammes of cake obtained amount to
8*215 - (0*535 + 0*235) = 7-445 grammes. In order to reckon
the fatty anhydrides equivalent to this amount of fatty acids,
18 parts of water must be subtracted for 56 of CaO combined
1 R
with them as lime soap — i.e., ^ x 0-725 = 0-233 gramme of
water must be subtracted, leaving 7-445 - 0-233 = 7'212 grammes
of fatty anhydrides present as lime soap.
Hence the whole analysis is —
Lime present as lime soap (CaO), . 0'725 grammes = 7'25 per cent.
,, in excess, .... 0'207 ,, = 2D7 „
Fatty anhydrides present as lime
soap 7-212 ,, = 72-12 ,,
Unsaponitied glycerides, . . 0'535 ,, = 5*35 ,,
Unsaponifiable matter, . . .0 235 ,, = 2 '35 ,,
Combined water, CC>2, sand, mois-
ture, &c. (by diflerence), . . 1'086 „ = 10'SG
10-000 100-00
Total lime soap present, 7 "25 + 72*12 = 79*37 per cent.
Total lime present, . 7 '25 + 2 "07 = 9 -32 „
* If the quantity is too small for accurate determination in this way the
liberated fatty acids, &c. , may be dissolved by ether, and the ethereal
solution separated and evaporated, &c., as in the parallel case of soap
analysis (Chap, xxi.)
AUTOCLAVE PROCESS. 373
Milly Autoclave Process — Saponiflcation with Alkalies
(Lime) under Increased Pressure. — As practically carried
out, this process is virtually a combination of the previous
process, and that subsequently described due to Tilghmanns,
where fats are hydrolysed by the action of water under high
pressure. The tallow and palm oil or other fatty mixture is
pumped into a stout copper pressure vessel or autoclave, and lime
made into a thin cream with water added in much smaller pro-
portion than in the open pan process, usually 2 to 3 parts of
lime per 100 of fat, or somewhere about one-quarter of the
theoretical amount instead of an excess. High pressure steam is
then gradually blown in from a boiler until the pressure amounts
to at least 7 or 8 atmospheres, and preferably 12 to 15, especially
when tallow only is used, as in many Continental factories.
After some hours continuance of digestion under pressure the
fat is practically completely saponified and hydrolysed, partly by
the lime, partly by the action of water only, the presence of the
lime soap formed by the saponification greatly facilitating the
hydrolysis ; the mixed " sweet water," fatty acids, and lime soap
are blown off into a tank, where the latter separate from the
watery glycerol solution, and are then treated with sulphuric
acid precisely as in the open pan process, saving that as much
less lime is used, a proportionately smaller quantity of acid is
requisite. The further operations of separating solid fatty acids
by pressure, etc., are identical in the two processes.
The remarks above made respecting the objectionable results
brought about when any considerable amount of glycerides escapes
saponification, and when the tallow is adulterated with wool-
grease or other unsaponifiable matters, obviously apply equally
in the present case. As regards the former point, the following
figures were obtained by the author in a set of experiments on a
manufacturing scale made with the. object of tracing out the
effect of increased time in diminishing the amount of unsaponified
grease. A series of charges was worked off in the same auto-
clave, the mixture of fats (tallow and palm oil), and the proportion
of lime used, and the pressure being as nearly as possible the
same throughout, but the times being different. The fatty acids
obtained (after separation from lime by sulphuric acid) were
analysed so as to obtain the data for determining the proportion
of grease unsaponified during the digestion. The figures ulti-
mately obtained on averaging a number of trials were —
Time in Hours.
Unsaponified Grease Reckoned per 100
parts Originally Employed.
4*
5|
74
9-4
5-8
3-1
374
OILS, FATS, WAXES, ETC.
During the first hour or two the rate of decomposition of the
fats employed was rapid, from f to ^ being converted at the end
of 2 hours ; subsequently the action was much slower, becoming
practically complete at the end of 6 to 6J hours, not more than
about -Jg- then remaining unconverted.
The following analyses indicate the composition of the " rock "
obtained by the autoclave process ; they principally differ from
those above cited for open pan rock, in that whereas in the open
pan process excess of lime is used, so that the rock contains all
the fatty acids as lime soap ; in the autoclave lime process a
deficiency of lime is employed, so that the fatty acids are obtained
partly as lime soap and partly as free acids : —
1 L
II.
in.
Lime present as lime soap (CaO),
3-20
2-38
2-52
Fatty anhydrides combined therewith,
Free fatty acids, ....
31-90
57*75
22-62
58-50
23-94
66-30
Unsaponified glycerides, .
5-90
G-60
3-20
Unsaponifiable organic matter,
0-70
1-33
1-85
Grit and mineral matters ; water, .
0-55
8-57
2-19
100-00
100-00
100-00
100 parts of the fatty glycerides used originally represent
about 95 of free fatty acids and 92 of fatty anhydrides, whence
100 parts of rock represent in these three cases respectively about
95, 86, and 96 parts of fatty glycerides that have been saponified
and hydrolysed ; whence the proportions of glycerides not acted
upon are —
I.
II.
III.
5-90
95 + 5-90
6-60
86 + C'60
3-20
96 + 32
100 = 5-8 per cent.
x 100 = 7-1
x 100 = 3-2
In general, with unadulterated tallow, the autoclave process,
properly worked, saponifies and hydrolyses about 95 per cent.
of the glycerides used, leaving some 5 per cent
unacted
on ; if, however, too low a pressure be applied, the proportion of
undecomposed glycerides may amount to considerably more than
this unless a proportionately longer time be allowed, involving
greater cost for fuel, labour, &c.
The " separation cake " or mixture of fatty acids obtained by
decomposing with sulphuric acid the "rock" formed in the
IODINE TEST APPLIED TO SEPARATION CAKE, ETC.
375
autoclave or open pan process consists of the solid fatty acids
produced (chiefly stearic and palmitic) ; the liquid acids (mainly
oleic) ; and whatever undecomposed glycerides and unsaponifiable
organic matters may be present ; the latter two ingredients
obviously vary with the degree of perfection or imperfection
attained in saponification, and with the purity of the materials.
The ratio between solid and liquid fatty acids also varies some-
what with the character of the tallow and other fatty matters
used; in general, it is not far from 2 to 1. In examining such
materials, the author has found the '"'iodine test" (pp. 177, 179,
et seq.) particularly useful, especially in the case of press cake in
different stages of pressing. The further the pressing (hot after
cold) is carried, the smaller the quantity of oleic acid left in the
"stearine;" but no amount of hot pressing will completely
eliminate " unsaturated " acids,* from 1 to 2 per cent, being
retained even when the pressing has been carried to the utmost
possible extent permissible for commercial purposes in the pre-
paration of articles of exceptionally high melting points, and
larger proportions up to 4 or even 5 per cent, in products less
thoroughly hot pressed. Even crystallisation several times from
alcohol of a mixture of palmitic and stearic acid does not succeed
in removing all the oleic or other iodine-absorbing acid present.
Thus the following typical figures may be cited, obtained by the
author with the fatty acids manufactured from a mixture of
tallow and palm oil : — f
Percentage of Oleic
Acid by Iodine Test.
Melting Point in
Capillary Tube.
Separation cake (mixture of fatty acids
before pressing), ....
32-0
Cold-pressed cake, ....
11 -5
52° -8 C.
Once hot pressed, . . . . .
5-6
54° -2
Twice ,, .
2-5
56° -1
Three times hot pressed,
1-3
56° '2
,, twice recrystallised from
alcohol, ....
0-8
56° -25
Red oils (oleine) from cold pressing,
71-5
Grease from hot pressing,
14-9
51° -6
The percentage of solid fatty acids contained in red oils can be
deduced approximately from the determination of the oleic acid,
reckoning 111 -02 parts of acid per 100 of iodine consumed, as
indicated by the equation —
* Possibly isoleic acid (m.p. 45°), and not oleic acid, remains.
t When a pressed stearine is examined, presumably only containing a
small percentage of oleic acid, 5 grammes may be conveniently taken for
analysis ; on the other hand, with a substance containing a high percentage
of oleic acid, proportionally less should be weighed up, usually from 0'2
to O4 gramme.
376 OILS, FATS, WAXES, ETC.
Oleic Acid. Saturated Iodine Addition
Product.
Ci8H3402 + I2 C]8H34T202.
If the percentage of unsaponified grease and unsaponifiable
organic matters present be known = a, and that of oleic acid
thus determined = 6, the percentage of solid fatty acids is
approximately 100 - (a + b).
Muter' s process for the determination of the proportion of
oleic acid present in a mixture of that substance with solid fatty
acids (stearic and palmitic) is based on the solubility of lead
oleate in ether. In the case of a glyceride, a quantity of sub-
stance not exceeding 1*5 grammes is saponified with excess of
alcoholic potash ; with free fatty acids it is dissolved in the same
solvent ; water is added and the alcohol boiled off; dilute acetic-
acid is then added to neutralise excess of alkali, until a decided
permanent turbidity is produced, and then dilute caustic potash
with continuous agitation until the liquid just clears again. The
clear solution is then precipitated by lead acetate in slight
excess, and stirred until the lead soap settles thoroughly ; the
supernatant liquor is poured off, and the precipitate washed by
boiling with a large bulk of distilled water and decanting.
Perfectly neutral lead stearate + palmitate + oleate is thus
obtained; the precipitate is transferred to a flask of about 100 c.c.
capacity and digested for some hours (with frequent agitation)
with absolute ether ; the ethereal solution of lead oleate is
filtered into a stoppered graduated tube holding 250 c.c., and the
filtrate and washings decomposed by agitation with about 20 c.c. of
a mixture of 1 volume strong hydrochloric acid and 2 volumes
water. Finally, a known fraction of the ethereal fluid is drawn
off and evaporated to dryness ; whence the weight of oleic acid
is deduced. The ethereal solution is conveniently drawn off by
means of a side tap fixed to the graduated tube about one-fifth of
the way up from the bottom, so as to be above the level of the
acid watery fluid ("Muter's oleine tube"); or it may be blown
off by the washbottle device (p. 120).
De Schepper and Geitel have constructed the table quoted on
p. 377, exhibiting the relative proportions of commercial "oleine"
(impure oleic acid) of solidifying point 5° -4, and commercial
" stearine " (stearic and palmitic acids) of solidifying point 48°
present in a sample of separation cake of given solidifying point
(compare pp. 75, 76).
The " filter cake " obtained from the red oils when these are
chilled and passed through a filter press varies considerably in
composition ; besides particles of fibre (derived from filter press
coverings, &c.) and dust, &c., filtered out, portions of unsaponified
grease separate in the solid state from the cooled red oils, and
smaller quantities of unsaponifiable matters (cholesterol, &c.) con-
tained in the grease originally used.
RED OIL FILTER PRESS CAKE.
377
Solidifying Point of
Separation Cake.
Percentage of Commercial
Stearic Acid.
Oleic Acid.
Degrees C.
5-4
0
100
10
2-5
97-5
15
6-6
93-4
20
12-1
87-9
25
18-5
81-5
30
27-2
72-8
32
31-5 68-5
34
36-6 63-4
36
43-0 57-0
37
46-9 53-1
38
50-5 49-5
39
54-5 45-5
40
589 41-1
41
63-3
367
42
68-5
31-5
43
73-5
26-5
44
78-9
21-1
45
83-5 16-5
46
89-0 ll'O
47
94-1
5-9
48
100-0
0
The following analyses represent its usual composition : —
Free fatty acids, solid, .
,, ,, liquid (oleic acid),
Unsaponified glycerides,
Unsaponifiable organic matters,
Fibres, dust, &c., ....
54-2
25-0
11-2
4-3
5-3
100-0
51-4
21-5
12-3
4-9
9'3
100-0
Since the great majority of the unsaponified glycerides con-
tained in the rock find their way into the red oils, whilst these
latter constitute the smaller half of the fatty acids obtained (the
" stearine " amounting to upwards of 50 per cent, of the total
acids) it results that the percentage of unsaponified glycerides
present in the red oils is usually more than double that in the
separation cake. The same remark applies to the unsaponifiable
organic matters. If the red oils be distilled by means of super-
heated steam the unsaponified glycerides present mostly become
hydrolysed during the operation, so that "distilled oleine" is
practically free from glycerides. On the other hand, a small
proportion of the oleic acid becomes decomposed during the
process, forming hydrocarbons (compare p. 278), so that the
unsaponifiable organic matters usually become notably increased
in amount. The following analyses indicate the composition of
378
OILS, FATS, WAXES, ETC.
different samples of red oils and "distilled oleines," and illustrate
these points : —
Red Oils.
Distilled Oleines
Tallow and
Tallow-
Palm Oil.
only.
Free fatty acids,
86-5
87-85
90-0
89-65
Unsaponified glycerides, .
Unsaponifiable organic matters, \
hydrocarbons, &c., . . /
11-7
1-8
11-30
0-85
1-6
8-4
2-95
7-40
100-0
100-00
100-0 100-00
Analysis of Red Oils, Separation Cake, and Similar
Products. — This is carried out substantially in the way indi-
cated on p. 162. The "free acid number," A, being determined,
and also the " total acid number," K, the data are obtained for
calculating the percentage of free fatty acids and unsaponified
glycerides present if the mean molecular weight of the fatty acids
is known or assumed. The unsaponifiable organic matters being
determined (by the methods described on p. 119) and the per-
centage of these constituents subtracted from 100 (as also that
•of any water or other foreign substance accidentally present), a
sufficiently close approximation to the truth is obtained by
multiplying the difference, D, by
A. -r \&- ~~ A j X
/ TZ" A \
centage of free fatty acids, and by -.—
- for the per-
l-Oo
x 1-05
-7T- for that
(K-A)x 1-05
of the undecomposed glycerides ; for if E be the mean equivalent
of the fatty acids, E + 12-67 is that of the glycerides (p. 165);
and as E usually lies between 255 and 285, the ratio of E to
E + 12-67 will lie between 1 to 1-050 and 1 to 1-045, and may
safely be taken as 1 to 1 -05 ; so that the weights of free fatty
acids and glycerides will be substantially in the ratio of A to
(K-A) x 1-05, whence the percentages will be —
Free fatty acids
Glycerides
A + (K - A) x 1-05 '
(K - A) x 1-05
A + (K - A) x 1^05 '
Thus supposing that a given substance contains 5 per cent, of
unsaponifiable matter, &c., and consequently that D = 95 ; if
the free acid number, A, be found = 175-0 and the total acid
number, K, = 195-0, so that K - A = 20, the composition will
be —
ANALYSIS OF RED OILS, ETC. 379
Free fatty acids 1?5 + 20°x = = 89*28
20 x 1-05 21
175 + 20 x 05 196
Unsaponifiable matters, &c., . . . . = 5 '00
100-00
From these figures it results that the value of E is close to
286; for 1,000 parts of substance contain 892 '8 of free fatty acids
neutralising 175-0 of KOH ; whence
175-0 : 56-1 : : 892'8 : x = 2S6'2
Similarly the mean equivalent of the glycerides is close to
286-2 + 12-67, or nearly 299.
Several attempts have been made to substitute metallic oxides
for lime in the autoclave lime process, more especially magnesia
and zinc oxide. At ordinary pressure these bodies usually act
upon fatty glycerides (such as tallow) appreciably more slowly
than lime, probably on account of their greater insolubility in
water; but it is claimed that under pressure this difference is
not observed, but rather the contrary, so that a much smaller
proportion of zinc oxide, will effect the saponification and hydro-
lysis of fatty matter than is necessary in the case of lime : thus
in the British patent specification of Poullain, E. F. Michaud,
and E. K Michaud (No. 5,112, 1882) from 2 to 5 parts of zinc
oxide are directed to be used per 1,000 of fatty matter (0'2 to 0'5
per cent.), heat being continued for 3 to 4 hours under a pressure
of 100 to 130 Ibs. (7 to 9 atmospheres). It is claimed that the
smaller proportion of base employed renders it necessary to use
much less acid to obtain pure free fatty acids than would other-
wise be required ; whilst for certain purposes — e.g., manufacture
of scouring soaps — it is not necessary to dissolve out the zinc
at all. As regards magnesia, comparative experiments with
lime and magnesia show that the action of the latter is always
inferior to that of the former (vide Journ. Soc. Chem. Industry,
1893, p. 163).
A somewhat analogous process has been proposed, where
ammonia is used as saponifying agent, fatty matters and aqueous
ammonia being heated together under pressure. Ammonia soaps,
if formed, are so far wanting in permanency that by blowing
steam through them they are decomposed, ammonia passing off
(collected for use over again), whilst free fatty acids and glycerol
solution remain. It does not appear that this system has as yet
been adopted so largely as to rank as an established practical
manufacture; but if sufficiently complete decomposition is obtain-
able in a moderate time, a priori the method would seem to be
of a workable character.
380 OILS, FATS, WAXES, ETC.
Stein, Berge, and de Roubaix have patented * the use of
solution of sulphurous acid or alkaline bisulphite as hydrolytic
agent ; from 2 J to 3 per cent, of solution is added to the fat in a
pressure vessel, and the temperature raised to 170° to 180°,
whereby a pressure of some 18 atmospheres is attained ; the
reaction is said to be complete in about 9 hours. The tempera-
ture should not exceed 200° C.
Hydrolysis of Fats by means of Sulphuric Acid.— It has
long been known that free fatty acids are obtainable from
glycerides by acting upon them with sulphuric acid, the glycerol
being largely converted into glycerosulphuric acid (p. 144),
subsequently more or less decomposed by the heat, and the fatty
acids being to some extent similarly acted upon, especially in the
case of oleic acid. The " Wilson " process (sometimes called the
"Dubrunfaut" process), the outcome of various methods originally
patented in England by Gwynne, Jones, and Wilson (Price & Co.)
in 1840 to 1843, substantially depends on these reactions, with
the further addition of purification of the fatty acids by distilla-
tion with superheated steam ; the melted fats (more especially
palm oil) are heated in a stout copper vessel (the " acidifier ") to
about 300° to 350° F = 149° to 177° C., by means of superheated
steam ; sulphuric acid is then run in to the extent of 3 to 5 per
cent., the whole intermixed, and allowed to stand some hours ;
during this period the glycerides are broken up, and foreign
organic matters present mostly carbonised. In general, the less
the quantity of sulphuric acid used, the higher is the temperature
employed. The acid mixture is then run off and boiled up with
water by means of wet steam, so as to wash out sulphuric acid
and other products soluble in water; after standing for some
hours to settle, the crude fatty acids are separated and heated to
about 240° F. (116° 0.) to complete the removal of water; finally
superheated steam at a higher temperature is passed through,
the precise temperature varying with the nature of the fatty
matter used, but being usually near 560° F. (294° C.)
Under these conditions the fatty acids are volatilised, and are
condensed along with most of the steam in a series of copper
serpentine refrigerating pipes exposed to the air, the escaping
vapours being deodorised as far as possible by a water shower
to absorb acrolein, &c., and subsequently burned, much as in the
somewhat analogous case of rendering animal fats (p. 247). The
fatty acids thus obtained contain a much larger proportion of
solid acids, and less fluid oleic acid than those obtained by the
lime saponification process from the same material, whether by
the open pan or autoclave method ; it would seem very probable
that this is due to the transformation by the action of sulphuric
acid of oleic acid into isoleic acid (melting at near 45° C.), as in
the case of the action of zinc chloride on oleic acid (p. 142) ; or,
* German patent, No. 61,329.
SULPHURIC ACID PROCESSES.
381
possibly, stearolactone or oxystearic acid is formed. According*
to Lant Carpenter,* tallow which will only yield about 50 per
cent, of its weight of
candle material when
treated by the lime
process, gives by the
sulphuric acid process
at least 75 per cent, of
such material of but
slightly inferior quality.
Of this, about three-
fourths is ready for
candlemaking without
further treatment ; the
other fourth, when
pressed and redistilled,
yields some 75 per
cent, of its weight of
stearic acid, and 25
of oleic acid ; ulti-
mately, only about 5
parts of oleic acid per
100 of fat are obtained.
A considerable pro-
portion of black pitch
(often amounting to
15 per cent, and up-
wards) is obtained as
bye product, whilst the
glycerol obtainable
from the acid liquors,
&c., is much less in
quantity and more
costly to isolate than
that from the lime
process ; accordingly,
whilst the larger yield
of solid fatty acids
renders the acid method
more economical from
one point of view, it
must be taken into
consideration, per con-
tra, that pitch instead
of oleine is obtained as part of the product,! and that glycerol
* Spon's Encyclopaedia, p. 581, et seq.
t By distillation at a higher temperature the pitch left on the first
distillation affords a certain proportion of fatty acids of inferior quality.
382
OILS, FATS, WAXES, ETC.
is lost, thus materially diminishing the apparent advant-
ages.
Fig. 83 illustrates the general character of the plant 'used in
the process.* A is the tank into which the tallow, &c., is melted
by means of a steam jet directed upwards into the bunghole of
the cask. B, one of a series of leadlined tanks, in which the grease
is heated before treatment with sulphuric acid, so as to boil off
water. C, pump with suitable taps and connections enabling it to
pump up the hot grease into the " acidifier," D; or into the tank,
H, supplying the still, I, after the sulphuric acid has been washed
out with water. E, acid tank supplying acidifier. F F, super-
heaters. G G G G, washing vats, where the acidified grease is
boiled up with water and steam to wash out sulphuric acid, &c.
H, grease tank supplying still, I, through which superheated
steam is blown, the vapours being condensed by the refrigerator,
K, and copper cooling coils contained in the tanks, k. L, scrubber
to condense acrolein, &c. M, pipe leading uncondensed vapours,
«fec., away to combustion flue for destruction.
Fig. 84 represents Knab's apparatus for continuous distillation
Fig. 84.
by superheated steam. A is the distillation vessel, into which
the fatty acids to be distilled are run through the supply funnel,
C, at intervals regulated by the rising and falling of the float
valve, D. Superheated steam enters by the pipe, F (furnished
with regulating valve and safety valve, E), and passes in small
streams through the molten fatty acids from the horizontal coil
* L. Field, "Cantor Lectures,1' 18S3 (Journ. Soc. Arts, vol. xxxi., p. 861),
DISTILLATION OF FATTY ACIDS. 383
at the base. The vapours pass off through the neck, G, to the
condenser ; the most easily condensed fatty acids are collected in
H, and drawn off from time to time through the cocks, J J,
whilst the other vapours pass on. K K is a blow off pipe for
removing residual pitch at intervals, the supply of fatty acids
through C being temporarily shut off. Heat is applied by means
of a bath of molten lead or other suitable metal contained in the
outer pan, B.
According to Schadler, the quantities of steam requisite for
distillation of a given quantity of fatty acids at different tem-
peratures are as follows : —
Temperature. Weight of Steam for 1 part of Fatty Acids.
200° to 230C
230° to 260C
290°
325° to 356C
7 parts.
3 to 4 parts.
2 parts.
1 part.
When the distillation temperature does not exceed 240°, the
distilled fatty acids are almost white ; at 260° a little coloration
is manifest ; at 290° this is more marked, whilst at temperatures
above 300° the distillate is yellow or brown.
Numerous other forms of apparatus for effecting distillation by
means of superheated steam have been constructed for particular
purposes — e.g., the purification of grease from cotton seed foots
(p. 261), of Yorkshire grease (p. 277), and similar substances ;
for the most part these differ from the above arrangements more in
details of construction than in general principles.
In Marix' arrangement for the distillation of free fatty acids
produced by hydrolysis or otherwise an air pump is applied, so
that a temperature of 250°-255° suffices for the distillation under
diminished pressure. A similar process has been patented by •
Lewkowitsch (English patent, 5,985, 1888), the pressure being
reduced by 10 to 13 Ibs., so that a temperature of about 460° F.
(238° C.) suffices, instead of about 600° F. (316° C.)
It is noticeable that when the products of distillation of a
charge of given material are collected in separate fractions, it is
found that in some cases the portions first passing over are the
most fusible, those coming over later possessing successively
higher and higher melting points ; whilst with other fatty matters
the reverse is the case. Thus, with palm oil the first distillate is
sufficiently solid to be used for candlemaking without any further
treatment, whilst the later portions are softer, and must be
pressed before they can be thus employed. With bone fat, on
the other hand, the successive fractions show a regular increment
in consistency. The following illustrative figures are given by
384
OILS, FATS, WAXES, ETC.
Payne as the melting points of the fatty acids collected in seven
different fractions : —
Fraction.
Bone Fat.
Palm Oil.
Degrees C.
Degrees C.
1
40
54-5
2
41
52
3
41
48
4
42
46
5
45
44
6
45
41
7
47
39-5
In almost all cases, however, the average melting point of the
distilled fatty acids exceeds that of the crude acids before
distillation.
Bock's Process. — In Wilson's process the hydrolysis of the
glycerides is mainly effected under the influence of comparatively
concentrated sulphuric acid at a tolerably high temperature (150°
to 180° C.), and subsequently completed partly by adding water
and boiling up with wet steam, and partly by distillation with
superheated steam ; Bock's process differs therefrom in that the
hydrolysis is mainly effected by comparatively dilute sulphuric
acid, the action of which is facilitated by the removal of the
nitrogeneous films or envelopes coating the fatty globules by
means of concentrated sulphuric acid acting at a much lower
temperature than in Wilson's process. Tallow, &c., is heated to
115° in an open vat * and well agitated with from 4 to 6 per cent,
of sulphuric acid, whereby the albuminous envelopes are charred
and broken up, but little or no hydrolysis effected. Water is
then added, and the blackened but still neutral fat boiled up
with the resulting dilute sulphuric acid for some hours until the
decomposition of the glycerides is complete, the degree being
judged by the mode of crystallisation of the fatty acids on cooling
a sample. When complete, the acid fluid is run off and neutral-
ised with lime, and the resulting aqueous crude glycerine solution
concentrated for sale. The blackened fatty acids are then sub-
jected to oxidation by means of bichromate or permanganate of
potash and sulphuric or hydrochloric acid, or of nitric acid, bleach-
ing powder, ifec., whereby the albuminous charred matters are
largely increased in density so that they subside, leaving the
fatty acids of a pale brown tint ; these are then washed and
crystallised, and subjected to cold and hot pressure in the usual
way, whereby a brown oil and a white stearirie are obtained.
The solid acids obtained are said to be whiter, of higher melting
point, and larger in quantity than those obtained from the same
* Lant Carpenter, British Association Reports, 1872, p. 72; vide also
Dinyler's Po'ylech. Jovrn., May, 1873.
HYDROLYSIS OF GLYCERIDES. 385
material by lime sapoiiification, probably through formation of
isoleic acid, stearolactone, or oxystearic acid, &c. (pp. 29, 39) ;
whilst 6 to 7 per cent, of glycerine solution at 38° T. (specific
gravity 1*19, containing about 70 per cent, of actual glycerol) is
obtainable. The plant is simple, all the operations being carried
out in one vessel ; and as only open steam is used there is no
danger of explosion as with autoclave processes. If desired, the
brown oleic acid can be distilled by means of superheated steam ;
or it can ba converted into palmitic acid by Radisson's process
(infra), for which purpose it is well fitted. 100 parts tallow
yield 95 of crude fatty acids, reduced to 93 by oxidation and
washing, of which 55 to 60 parts are obtainable as candle stearine,
melting at 58° to 60° C. (136° to 140° F.)
Hydrolysis of Glycerides by Water Only. — In 1854 a
patent was taken out by Tilghmann for the decomposition of
glycerides by means of water under great pressure, and corre-
spondingly high temperature ; in one form of apparatus a mixture
of fat and water was forced through a coil heated to about
420° C. (upwards of 800° F. ), the pressure approximating to a ton
per square inch (some 140 atmospheres). Various improvements
were subsequently made ; but the practical difficulties attending
the working of manufacturing operations of the kind prevented
the method being largely adopted. A modification of the process,
patented shortly after wards by Wilson & Payne (No. 1,624, 1854),
effects the same result in a much simpler way. The fatty
matter being heated in a still to about 300° C., steam from a
superheater is blown through it by means of a rose jet or false
bottom perforated with a large number of small holes, so that
numerous jets of steam rise through the mass. Hydrolysis takes
place, and the fatty acids and glycerol formed are volatilised and
carried over with the excess of steam to the condensers, where
the free fatty acids and glycerol in aqueous solution are obtained ;
the former condense first, so that by using a series of condensing
chambers, little but fatty acids are obtained in the earlier ones,
whilst chiefly watery glycerol condenses in the later ones, yielding
a very pure commercial glycerine by simple concentration after
separating the small quantity of accompanying fatty acids.
Fig. 85 represents the general character of this plant. Steam is
superheated in the superheater A, and passes into the retort, C,
covered in with a lid, E ; the vapours pass off to the condensers,
G, for fatty acids, and F for glycerol water. If the temperature
is too high (above 315°), much loss of glycerol occurs through the
formation of acrolein.
In France, the saponification of fatty matters by means of
water alone (without lime, <fcc.) is much more largely carried
out than in Britain, on account of the more frequent use of pure
" stearine " candles, instead of those made largely or wholly of
paraffin wax. Several different forms of apparatus are in use : for
25
386
OILS, FATS, WAXES, ETC.
a description of some of these exhibited at the Paris Exhibition,
vide B. Lach, Chem. Zeit., 13, pp. 1157, 1218, 1335, 1374; in
abstract Journal tioc. Ckem. Ind., 1890, p. 82.
Utilisation of Red Oils. — In the manufacture of candle
material from glycerides a more or less considerable propor-
tion of "red oils'" is obtained, the amount varying with the
Fig. 85.
method of saponificatioii or hydrolysis adopted, the nature of
the fatty matters used, and the temperature at which the cold
pressing is effected. Commercially, the " oleine " thus produced
is considerably less valuable than the solid "stearine;" whence,
cceteris paribus, it is desirable so to conduct the operations as to
obtain the maximum yield of solid products and the minimum of
liquid ones. In general: the red oils thus produced are utilised
by conversion into socalled " oil soap/'? by direct saturation with
soda ley of appropriate strength (vide Chap, xx.) ; but various
attempts to employ them as a source of other more valuable
products have been made. One such process, due to v. Schmidt,
consists in heating the red oils with about 10 per cent, of zinc-
chloride to a temperature of about 185°, whereby conversion into
more solid substances is brought about, chiefly by formation of
isoleic acid and stearolactone (vide p. 142). Another process
(Radisson's, vide infra) depends on the conversion of oleic into
palmitic acid by fusion with alkalies; whilst Ziirer has attempted*
to convert oleic into stearic acid by first subjecting to the action
of chlorine, and then treating the dichloride of oleic acid formed
* German Patent, No. 62,407.
KADISSON'S ARTIFICIAL PALMITIC ACID. 387
with nascent hydrogen evolved from zinc dust (or finely divided
iron or magnesium) and water heated under pressure.*
Radisson's Artificial Palmitic Acid. — It has long been
known that acids of the oleic family when fused with caustic
potash undergo a peculiar decomposition evolving hydrogen, and
breaking up so as to form two acids of the stearic family, of
which acetic acid is generally, if not invariably, one (p. 24) ;
e.g., oleic acid when thus treated breaks up, forming palmitic
acid in accordance with the equation —
Oleic Acid. Caustic Potash.
C18H3402 + 2KOH - C]6H31K02 + C2H3K02 + H2.
M. St. Cyr Radisson. has succeeded in carrying out this reaction
on a manufacturing scale, converting some 3 tons oleic acid
into palmitic acid per diem. The fusion is effected in a covered
iron cylindrical pan or " cartouche " with dished base, provided
with a mechanical agitator, and set in brickwork some distance
(nearly 6 feet) above the firebars of a grate, so that a large
hot air chamber is formed underneath, enabling the tempera-
ture to be more easily regulated. 1,650 Ibs. of oleic acid
and 2,750 of caustic potash ley, specific gravity 1-4, are run in;
when steam ceases to be evolved, a manhole in the cover is
closed, and the evolved hydrogen passes off by a pipe to a purifier
and gasholder for other use. The temperature requires to be
very nicely adjusted, 300° to 310° being the proper value, whilst
at 320° destructive distillation commences ; to avoid overheating
a Gifford steam injector is provided whereby the temperature of
the interior can be reduced when requisite. Some 36 to 40 hours
are required for completely working off a charge, including filling
the pan and emptying; the progress of the operation is judged
by sampling and testing the solidifying point of the acids
liberated from the mass by a mineral acid, preferably by
Dalican's method (p. 74). When complete, the contents of the
pan are run off through an outlet pipe into a tank containing a
small quantity of water, and the whole heated up by a steam jet.
The excess of potash present then dissolves, forming a strong ley
(specific gravity about 1'14) in which the potassium palmitate
is insoluble, floating up as a soap ; this is transferred to a decom-
posing vessel where the palmitic acid is set free by means of
sulphuric acid ; the acid is then distilled in the usual apparatus,
leaving some 3 per cent, of pitch, and furnishing a perfectly white
acid, melting at 50° to 53° C., burning with a clear smokeless
flame. About 87 per cent, of white palmitic acid is obtainable
* De Wilde and Eeychler had previously shown that by heating oleic
acid with a small quantity of iodine or bromine under pressure, some 70
per cent, becomes converted into stearic acid (Bulletin &oc. Chem., Paris,
1889, 1, p. 295).
388
OILS, FATS, WAXES, ETC.
in practice, the theoretical yield being 91 per cent, of the oleic
acid used. According to Lant Carpenter, the oleic acid produced
by Bock's process (supra) is better adapted to the purpose than
ordinary red oils prepared by alkaline saponification, a higher
yield of palmitic acid being thereby obtained. For further
details, vide Spon's Encyclopaedia of Arts and Manufactures,
p. 584.
CHAPTER XVII.
MANUFACTURE OF CANDLES, TAPERS, AND
NIGHTLIGHTS.
SEVERAL different kinds of process are or have been employed in
the manufacture of candles for the purpose of surrounding the
wick with a more or less uniform coating of solid combustible
matter. In the early and middle ages, when wax was the
material used by the more wealthy classes as illuminant, a
simple mechanical process of hand manufacture was usually
adopted, a lump of
wax being softened
by heat and kneaded
until sufficiently plas-
tic, then applied
round the wick, and
rolled into shape. A
similar process is still
employed, with the
difference that the
wax is applied by
" pouring " the just
melted material over
the wick so as to iii-
crust it with a layer
of wax ; after cooling,
another layer is simi-
larly poured over, and
so on, the candle
Fig> 8C being reversed in
position from time to
iime until the requisite thickness is attained; the still somewhat
plastic wax candles are then rolled into shape, some half dozen
at a time, on a smooth marble table with a board on which the
workman presses heavily; the finished candle consequently
exhibits concentric layers of wax, something like the rings of a
DRAWING WAX TAPERS.
389
tree. The process requires considerable skill to produce a per-
fectly even surface with truly central wick, especially in the case
of large sized candles ; to facilitate the " pouring" or " basting"
operation, the wicks are usually hung on a horizontal wheel
(Fig. 86) fixed over the projecting lip of a large basin holding
the melted wax, so that each is "basted" in turn. Large conical
altar candles (cierges) are still generally made substantially by
the older process, the plastic wax being rolled into a long thin
strip or ribbon, which is then coiled round the wick (previously
soaked in melted wax) and rolled into shape on the marble slab,
instead of being basted on.
In practice it is difficult to "mould" wax candles satisfactorily
oil account of sticking to the mould and shrinkage during solidi-
fication, and consequent tendency to crack ; but thin candles can
Fig. 87.
be "drawn" somewhat after the fashion of wire by running the
wick through a pan of melted wax, and subsequently making it
pass through a drawplate so as to reduce the layer of wax to
uniform thickness (Fig. 87). The wick is usually wound from
one drum on to another ; after one coating is applied it is wound
back again, this time passing through a somewhat wider draw-
hole, so as to give an increased thickness of wax ; as a rule,
however, neat tapers of more than about half an inch diameter
cannot be conveniently made thus, as the tendency to crack
becomes too great when the diameter increases beyond this
point. In whatever way the wick is coated, whether by " rolling,"
" pouring," or " drawing," the candles are ultimately finished by
cutting off the butt ends clean with a sharp knife (Fig. 88), and
trimming the other ends to conical tips. When tinted wax
candles are requisite usually only the last batches basted on are
390
OILS, FATS, WAXES, ETC.
coloured, as the tinting- materials are generally apt to clog the
wick, especially if solid ; for white candles airbleached wax
(p. 268) is employed, wTax blanched by chemicals (especially
chlorine) being- unsuitable (p. 267).
Fig. 88.
Dip Candles. — In the preparation of rough candles for house-
hold use in mediaeval times and even still more recently,* the
wicks used were generally rushes (Juncus conglomeratus) skilfully
Fig. 89.
peeled so as to leave the pith supported by one thin rib of green
rind, whence the familiar term "rushlight." These were soaked
(after drying) in melted tallow or kitchen grease, held up to
* Gilbert White, "Natural History of Selborne" 1789.
EDINBURGH WHEEL.
391
cool, and then dipped again carefully into the just melted grease
and quickly withdrawn, so that the film of adherent tallow
solidified before it had time to run down ; for which purpose
it was imperative that the grease should not be overheated.
The dipping was then repeated at intervals until the coating of
tallow was sufficiently thick. By and bye when tallow candle-
making became a trade of itself this method of manipulation was.
adopted on a larger scale with appropriate modifications ; linen
or cotton wicks supplanted rush pith, whilst the dipping was
effected by fixing a number of wicks (previously soaked in tallow)
on hooks driven side by side a little way apart into the bottom
of a piece of board or wooden lattice frame, so that by lifting the
board by means of a knob or handle on the upper side, all the
wicks attached could be simultaneously dipped and withdrawn.
To facilitate the dipping, the board with dependent candles was
attached to a rope passing over a pulley (Fig. 89) ; each frame of
candles when dipped being unhooked from the rope and suspended
from the periphery of a horizontal wheel so as to hang up and
harden ; by dipping in regular succession each one of a number
of frames thus suspended, each batch of candles became suffi-
ciently cooled and " set " to be ready for another dip by the time
its turn came ; the wheel thus slowly revolved, making one
revolution for each dipping of the whole series of frames suspended
therefrom. By attaching suitable weights to the end of the cord
as counterpoise the time is easily ascertained when the candles
have been dipped sufficiently often to be of the right weight.
To avoid the trouble of unhooking each frame and hanging it
up from the wheel a series
of separate radiating bars
have been substituted for
the complete wheel, each
bar being capable of oscil-
lating in a vertical plane
working 011 a pin in a
slot in the vertical axis.
Fig. 90 represents a form
of "Edinburgh wheel"
of this description ; each
bar, B B, carries two
dipping frames, one at
each end, the second
serving as counterpoise
to the first ; each frame
is successively pulled
down and dipped in the
tallow cauldron and then
Fig. 90.
raised again, the wheel being made to revolve partially so as to
bring the next succeeding frame over the cauldron. Various
392
OILS, FATS, WAXES, ETC.
subsidiary arrangements are sometimes applied for the purpose
of ensuring horizontality of the radiating bars when raised after
dipping even though the newly dipped end may be a little
heavier than its counterpoise.
The wicks may be suspended from the hooks by means of a
loop of cotton thread tied to them ; but a more convenient plan
is to double the wick, stringing the series over a rod as indicated
in Fig. 91. The rod with the dependent wicks is then dipped
by hand into a trough of melted tallow and hung up on a rack
or otherwise supported until the tallow is sufficiently set to
permit of another dipping ; or a series of rods are attached side by
side to a frame supported by cords and attached to an hdinburgh
wheel, ifcc. In order to impregnate the wicks with tallow in the
first instance and to get them all of the right length, the wick is
=$F$F$=^^
Fig. 91.
unwound from a bobbin, and wound round a square frame of
suitable size so as to form a sort of loose covering ; this is then
dipped bodily in hot tallow to within an inch or so of the top
of the frame, so as to fill up all the pores in the immersed
portion of the wicking : the entire row of strands at the bottom
of the frame is then cut through wyith a knife, and the different
doubled wicks separated, and strung on the rods as indicated.
Another mode of proceeding, formerly much used in the larger
dipping establishments, is to have the cauldron of melted tallow
movable, so as to pass in succession beneath each one of a series
of frames. Fig. 92 represents the section of an arrangement of
the kind : the two frames, D D, are connected by a cord passing
over pulleys supported by a beam arid posts, so that one counter-
poises the other ; by pulling the cords, E E, the one or the other
can be made to descend. A number of these pairs of frames are
arranged side by side (Fig. 93) the cauldron of tallow (kept fluid
by means of a brazier) running on a railway down one side of the
row and up the other, so that each one of the frames is dipped in
regular rotation. A sort of mechanical wiper is conveniently
connected with the cauldron, so that by moving a lever after the
candles have emerged from the molten tallow the drops of melted
grease that run down to the bottoms are removed. When well-
shaped candles are required, the irregularities may be smoothed
down by pulling each candle in succession by hand through a
series of holes in a drawplate (graded in diameter, the smallest
DIP CANDLES.
393
being the size ultimately required) so as to strip off a portion of
the outer coating, leaving the remainder fairly cylindrical.
A peculiar modification of the dipping process is sometimes
practised : the wicks are dipped in hot melted tallow as usual to
fill up pores; instead of applying the outer coatings by successive
dippings of the treated wicks, thin steel rods are dipped in the
tallow ; when the candles are of the requisite thickness they are
cooled completely, and the steel cores extracted ; the wicks are
then passed through instead, and fastened in position by a few
L_J
Fig. 92.
Fig. 93.
drops of melted tallow. A similar device is also employed in the
manufacture of certain kinds of night lights (infra), except that
the wickless hollow candles are made by casting instead of
dipping.
At the present day, although the manufacture of dip candles
made of unsaponified tallow is by no means extinct (there being
still some considerable demand, especially in country districts),
the quantity manufactured is much less than that of " moulded"
candles, mostly prepared from solid fatty acids ( socalled
"stearine") and paraffin wax, but sometimes from unsaponified
394 OILS, FATS, WAXES, ETC.
tallow or mixtures containing both free fatty acids and solid
unsaponified glycerides (composites). Tallow candles, when
blown out, generally emit an acrid vapour, due to the decomposi-
tion of the glyceride by the heat of the smouldering wick, with
formation of acroleiii ; this circumstance, together with their
comparative softness inducing "guttering," the necessity for
" snuffing," and the tendency to emit smoke and give a less
clear brilliant light than stearine and paraffin candles, has caused
them gradually to fall comparatively into disuse, especially
amongst dwellers in towns.
Wicks. — The nature of the wick employed in a candle very
greatly affects the way in which it burns, and consequently the
light emitted. In the old fashioned tallow dip candle, thick
twisted cotton wicks are still used ; these do not thoroughly
consume away, and consequently " snuffers " are requisite in
order to remove the charred smouldering cotton, otherwise much
less light is given out, and a smoky flame produced. By various
mechanical devices, attempts have been made to give to such
twisted wicks a tendency to bend outwards in the flame, so as to
come in contact with the air and consume spontaneously ; others
have sought to attain the same end by incorporating a thin wire
with the cotton strands. Palmer's " metallic wick " was an
analogous device, where a thread impregnated with powdered
bismuth was bound up with a number of others of ordinary
fibres by winding one round the bunch ; when burnt, the
bismuth formed a minute globule at the end of the wick, the
weight of which tended to draw the wick outwards ; so that the
carbonised cotton was burnt away, and the bismuth volatilised,
or was otherwise dissipated by combustion. De Milly attempted
to gain the same result by impregnating the wicks with boracic
and phosphoric acids, &c., so as to form a globule of fused
mineral matter. All such devices, however, have been super-
seded for the better classes of candle by the use of flat plaited or
" braided " wicks (first introduced by Cambaceres), where the
mode of construction imparts a natural tendency to bend
outwards. The precise mode of plaiting adopted considerably
modifies the way in which the wick burns, one kind of braiding
being better suited than another for certain kinds of combustible
matter ; thus, paraffin candles require a wick more tightly
braided than is requisite for stearine candles, whilst looser
wicks are used for wax and sperm candles. As a rule, the
plaiting of the wicks is not carried out in the candle factory, but
by spinners making a speciality of this particular line, and
delivering the braids in hanks of convenient size ; the machines
used much resemble those employed in the manufacture of
ordinary braids.
Wick Pickling. — Before conversion into candles, the wicks
are soaked or "pickled" in a suitable saline solution for some
MOULDED CANDLES. 395
hours ; they are then drained and finally wrung out by means of a
rapidly rotating centrifugal machine so as expel almost the whole
of the fluid without twisting the threads in any way, and finally
hung up to dry in a room heated by steam pipes. The object of
the pickling is, on the one hand, to counteract the accumulation
of mineral matter or "ash" in the wick as it burns, and on the
other, to prevent the too rapid burning away of the wick fibres
before the due quantity of melted fatty matter has passed along
them and been consumed in the flame. The choice of the parti-
cular solutions employed and their strengths is usually regarded
as a trade secret, each manufacturer having his own views on the
subject to which experience has guided him ; solutions varying
from 1 to 5 per cent, of saline matter in strength have been
recommended, such as borax (alone, or acidulated 'with a minute
quantity of sulphuric acid), salammoniac, saltpetre, phosphate of
ammonium, or mixtures of such salts ; although only very minute
quantities of saline matters ultimately remain in the dried wicks,
yet the effect thereby produced on the way in which the candle
burns is often very marked.
MOULDED CANDLES.
The art of moulding candles, instead of dipping them, is due
to the Sieur de Brez in the fifteenth century; but excepting for
the employment of this method in the manufacture of spermaceti
candles in the latter part of the last century, but little advance
was made in this direction until the introduction of " stearine "
(solid free fatty acids) as candle material instead of tallow, and
the subsequent employment of paraffin wax for the same purposes
a little after the middle of the present century. The earlier
moulding machines were socalled " hand frames " (still in use for
small operations and special sizes for which only a small demand
exists) containing a series of pewter moulds with removable-
mouthpieces, Fig. 94, depending downwards from a shallow
trough, Fig. 95, the top end being lowest and the butt end
uppermost. By means of a wire with a hook at the end the
wick was hooked through a narrow orifice at the conical lowest
end of the mould and brought upwards, and finally fixed to a
wire hook, n, by means of a knot on the wick, or preferably a
little loop of cotton thread tied to the wick ; so that by gently
pulling the wick downwards at the bottom and fixing it with
a peg, it was stretched in the axis of the cylindrical mould
(Fig. 96) ; or instead of a removable mouthpiece carrying a hook
like n, a short piece of wire was passed through the loop and
allowed to rest in a couple of shallow notches opposite to one
another in the upper rim of the mould, so that the wick depended
axial ly therefrom. Figs. 97 arid 98 represent an improved
modification of this arrangement, where, instead of having a
,396
OILS, FATS, WAXES, ETC.
VJ
Fig. 94.
Y
Fig. 96.
Fig. 93.
Fig. 97.
Fig. 98.
HAND MOULDING FRAMES.
397
separate wire for each candle, a whole row of wicks is simul-
taneously supported by a single rod, D D, which is with-
drawn when the candles are extricated from the moulds after
cooling. The use of this rod generally leaves a corresponding
mark or groove at the base of the finished candle, whereby a
hand made article can be
readily recognised. The
moulds being somewhat
warmed so as not to chill
the candle material too
quickly, the molten sub-
stance is poured into the
trough so as to fill all the
moulds, and also part of
the trough to allow for
shrinkage ; the whole is
then set by to cool, and
when the candles are suf-
ficiently set, the contents
of the trough are scooped
out with a trowel. Pre-
ferably, the frame carry-
ing the series of moulds is
immersed in a water tank
so as to facilitate the chill-
ing, the temperature of the
water varying with the
nature of the material
used and the dimensions
of the candles moulded ; it
being usually necessary
that the solidification
should go on at a par-
ticular rate, otherwise a
crystalline structure may
be developed by too slow
cooling, injuring the ap-
pearance of the candle, or
cracking may occur with
too rapid chilling. When
the candles are completely
set, the frame is removed
from the water, and the Fig. 99.
candles extricated by re-
moving the pegs and inverting the frame, when they mostly
fall out of themselves owing to the moulds being slightly conical;
if sticking occur, gently tapping the mould generally suffices to
dislodge the candle. Including "threading" — i.e., setting the wicks
.398
OILS, FATS, WAXES, ETC.
in position by hand (by passing it through the lower orifice and
pulling it upwards by means of a wire) — filling, and emptying,
hand frames can only be worked off about once in an hour, or
somewhat less frequently. In the later " continuous " candle
moulding machines, three times this speed is attained, much time
being saved by a device whereby the wick is passed continuously
at stated intervals through the mould, a candle being cast at each
period, and when set, lifted upwards so as to draw the wick into
position for the next moulding, so that a string of candles, one
after the other, is cast around each wick.
Fig. 99 represents Royan's form of continuous wick moulding
machine as used in Germany (Schadler) ; as each batch of candles
is cast and becomes sufficiently hard, they are lifted upwards out
Fig. 100.
of the moulds by means of a rack and pinion which elevates a
platform to the under side of which the wicks are fastened by a
series of clips ; in this way the wicks are always kept gently
stretched along the axes of the moulds ; several successive tiers
of candles are thus moulded without altering the attachments.
When the platform reaches its highest elevation the wicks are
severed below the lowest tier, and the strings of candles removed
from the clips that support them ; the platform is then lowered
and the wick ends affixed to the clips, and the operations com-
menced afresh.
Fig. 100 represents " Camp's moulding wheel," a combination of
the principle of the " Edinburgh wheel '' used for dipping candles
with this "continuous" moulding action; this arrangement has been
.somewhat extensively used in America (Christian!). A revolving
CONTINUOUS MOULDING MACHINES.
399
horizontal wheel, B, is supported by iron rods, O O O, and turns
on a pivot, C, attached to the roof. A series of moulding frames,
A A A, are supported by the wheel, regularly arranged radiating
from the centre; the troughs, b b, b b, surrounding these can be
filled with water heated to any required temperature by means
of steam pipes, or if need be cooled with ice. Just below the
tips of the moulds are the rows of bobbins of wick, the ends of
which, to begin with, are drawn upwards by hand and adjusted
in the axes of the moulds. When all the moulds are ready the
discharge valve, P, of a tank of melted candle material, M, is
opened so as to fill one of the mould frames in position under-
neath ; the wheel is then pushed round until the next mould
frame is in position under the spout, when this is similarly filled ;
and so on with all in turn. By the time the last frame is filled
the first will have cooled sufficiently to enable the candles to be
cautiously withdrawn and laid over in grooves cut for their
support in the ledges of the frame ; as this is done the wricks
are drawn upwards, so that the moulds are threaded ready for
the next filling. The mould frame thus emptied is refilled with
melted candle material ; and similarly with the next, so that the
wheel is revolved a second time, each mould frame being filled
in succession as before ; when all the frames are filled the candles-
lying over in the grooves (by this time perfectly
hard and solid) are cut off and removed, and these
now filling the moulds are pulled upwards and
made to take their place.
The moulding machines in use at the present
day in the larger factories are mostly constructed
on the "piston" principle, whereby the candles
when sufficiently set are mechanically expelled
from the moulds by means of a series of pistons
rising up therein and lifting the candles out. Fig.
101 represents the general mode of action, identical
in principle with that of an ordinary " lifting
pump " without the valve, excepting that the
piston-rod is below instead of above ; the piston is
hollowed conically so as to form the mould of the
candle tip ; the wick passes upwards through the
tubular piston-rod. A series of moulds is arranged
in a convenient frame or trough into which water
can be run heated by means of steam, or artificially
cooled as may be requisite according to the tem-
perature at which the moulds are to be kept, which Fig. 101.
varies with the nature of the candle material.
Fig. 102 represents a moulding machine containing two such
troughs arranged parallel, each containing a double row of
moulds set in a suitable frame with the piston-rods all depressed;
this is effected by connecting them all to a horizontal shelf
400
OILS, FATS, WAXES, ETC.
(driving plate) capable of being raised or lowered at will by
means of a handle working a pinion gearing into a rack ; as the
shelf is raised the four rows of candles are simultaneously lifted
upward by the ascent of the pistons. As they rise they pass
through four series of grooved jaws or ': nippers" slightly open ;
at the summit of the elevation these jaws close, gently grasping
iind supporting the candles, the grooves being lined with felt or
preferably india rubber. The handle is then turned the reverse
way so as to depress the pistons to the lower ends of the moulds ;
the wicks attached at the upper ends to the rows of candles
supported by the nippers are consequently stretched in the axes
of the moulds, having been unwound from the bobbins beneath
during the ascent of the candles.
Fig. 102.
To commence operations, each wick is hooked up by means of
a wire through the hollow piston-rod and fixed in the axis of the
mould, as in the hand frame ; melted candle material is then
poured into the moulds, and when set the candles are lifted out
(by raising the pistons) and held by the nippers, the wicks being
thus pulled upwards into position for the next casting ; the
MOULDED CANDLES. 401
pistons are then depressed, sliding over the wicks as they
descend ; the temperature of the water trough is adjusted if
requisite, and a new batch of candles cast by pouring in more
melted candle material. When this has set sufficiently to keep
the wick in its central position without extraneous aid, the upper
rows of candles held by the nippers are detached by cutting
through the wicks ; the nippers holding the candles are then
opened and the candles extracted, or, preferably, are lifted off
(being detachable) and emptied on to a table, &c. The nippers
are then replaced and the process repeated until the wick bobbins
are exhausted.
The lengths of the candles thus moulded in a given set of
cylinders can be regulated at will by simply raising the driving
plate by means of set screws, so as to shorten the distance
between each piston and the top of the corresponding mould, and
thus form a shorter candle ; or vice versd. When the butt ends
of the candles are required to be conical (so as to fit into any
sized stick), a special kind of cutting machine is employed to
shave down the ends. If the cone is to be of greater diameter at
its base than the rest of the candle, a special modification of the
mould is employed (infra}.
The chief skill required in working the candle moulding
machine lies in properly regulating the temperature, the modus
operandi varying in this respect with the material. With pure
stearine (i.e., solid fatty acids with just enough paraffin wax,
beeswax, or vegetable wax, or other similar material to u break
the grain," and prevent or diminish crystallinity), the moulds
are kept at a temperature slightly below the setting point of the
candle material, which is poured in on the point of congealing,
well stirred so as to form a gruel-like mass. The workman
generally judges the temperature by simply putting his hand into
the water trough surrounding the moulds, cooling it by running
in a little cold water if requisite, or vice versd. With paraffin
wax, on the other hand, the moulds must be heated by hot water
or steam well above the melting point of the wax (usually up to
80° to 85°, or about 170° F.), whilst the wax also should be hotter
than its fusing point; when the moulds are filled, the surrounding
hot water is run off and cold water run in instead, whereby the
material is quickly chilled, and the peculiar translucency and
lustre desired is attained. In certain cases this effect is
heightened by alternately admitting hot and cold water into
the water box, the precise mode of operating varying somewhat
according as paraffin scale of relatively low melting point is used,
or harder paraffin (cerasin, ozokerite, &c.) of higher melting point,
witli or without the addition of a few per cents, of stearic acid,
either for the purpose of serving as vehicle for colour (p. 405), or
to prevent the tendency to soften and bend often shown by pure
paraffin candles, even at temperatures considerably below the
26
402
OILS, FATS, WAXES, ETC.
fusing point. In some cases, where mixed materials are used
with stearine in larger quantity, intermediate temperatures are
employed for the water box. In Britain, paraffin candles have
largely driven fatty acid candles out of the market on account of
their greater cheapness, but this is not so much the case on the
Continent.
Moulded tallow candles were formerly somewhat largely
employed, but latterly have mostly gone out of use along with
dips on account of the objections to glycerides as combustible
matter (p. 394). The same remark also largely applies to
" composites," or mixtures of free fatty acids and glycerides,
except for night lights (p. 406).
Spermaceti candles are usually moulded in much the same
way as paraffin wax candles, the material being heated above its
melting point and run into hot moulds, which are then rapidly
chilled by means of cold water. During the latter part of the
last century and the earlier portion of the present one they were
in some considerable amount of use by the wealthier classes ;
but like wax candles, their use is but small nowadays as com-
pared with candles of "stearine" and paraffin wax. With
properly adjusted wicks they burn with considerable regularity
and brightness, and are accordingly selected as the practical
standard for photometric observations ; a " standard candle ;'
being one burning 120 grains of spermaceti per hour.
For certain special forms of candle particular modifications of
the moulding machine are requisite ; thus stearine
candles, especially on the Continent, are often cast
with longitudinal internal spaces or tubes, which
tend to prevent " guttering " whilst burning.
Spiral exteriors are also much in favour; formerly
these were made by lathing cylindrical candles
cast in the ordinary moulds ; but in the more
recent machines the pistons are made to ascend
by a screw motion, the moulds themselves being
correspondingly grooved, so that the candles are
screwed out of the moulds. For " self-fitting "
butt ends (Fig. 103), where the thickest portion
of the conical part is of greater diameter than the
rest of the candle, the frame above described
requires modification. Fig. 104 represents a
machine for moulding self-fitting butt end candles,
constructed by E. Cowles, of Hounslow, where the
butts are shaped by a separate series of moulds
fitting on the top of the cylindrical moulds, and ultimately lifted
off from the conical candle ends by means of the chain, the candles
being then raised by the piston and held in removable nipping
frames in the usual way. This arrangement does not permit of the
wick being run continuously ; after each batch of candles is cast
Fi<r. 103.
SELF-PITTING BUTT ENDS.
403
404
OILS, FATS, WAXES, ETC.
the wicks must bo severed, and after removal of the nipping
frames and candles the butt mould lowered into position ; each
wick is then hooked up through its appropriate butt mould and
clamped centrally in the axis of the mould so as to be ready for
the next casting. This involves much trouble and delay, besides
causing the waste of a short length of wick at each candle end.
These objections are obviated by making the butt end moulds
in two halves, separable from one another at will, so as to permit
of the candles rising upwards when the half-moulds are apart, but
tightly closing together and fitting accurately on the tops of the
piston moulds when required ; the opening and shutting is simply
effected by the motion to or fro of a separate handle. When the
moulds are closed, the melted candle material is poured in ; after
TINTED CANDLES.
405
setting, this handle is moved back so as to open the butt moulds ;
the main handle actuating the pistons is then moved so as to
raise the candles into the nipping frame ; the pistons are then
lowered, the butt moulds closed, and a new casting proceeded
with.
Fig. 105 represents a "turnover" machine, swinging on trun-
nions, so that when a hard candle material has been run into
the moulds and has partly solidified round the sides, the machine
can be tipped over so as to allow the still liquid portion of the
material in the centre of the moulds to run out, thus leaving
hollow candles which are then filled in with softer material;
candles of comparatively easily fusible substance can thus be
prepared with an outer casing of less fusible material which pre-
vents the guttering that would otherwise occur.
Stearine candles are comparatively seldom tinted, being gener-
Fig. 106.'
ally burnt uncoloured ; sometimes, however, they are tinted
yellowish with gamboge, &c. For tinted paraffin candles, how-
ever, a considerable demand exists. Formerly the candle
material was coloured by incorporating a small quantity of very
finely ground pigment ; but this is now never done if it can be
avoided, as the wick almost invariably becomes clogged after
burning a short time, so that a smoky less luminous flame
results. Coaltar dyestutf's are generally preferred, as far as pos-
sible free from fixed mineral constituents ; in many cases these
will not dissolve in pure paraffin wax; but by dissolving them
in fused stearic acid, and incorporating a little of the solution
with the melted paraffin, the latter can usually be readily tinted
any required depth of shade.
In the case of stearine and wax candles, and sometimes with
other varieties also, an extra degree of gloss and polish is some-
406 OILS, FATS, WAXES, ETC.
times given to the surface by rubbing and rolling them by hand
or between cloth-covered rollers, &c. ; several machines have
been constructed for this purpose. Fig. 106 indicates a simple
arrangement where the candles are gradually passed out of the
tray, A (by means of the grooved roller, B) on to the endless
cloth, E D E D, and rolled between the cloth-covered rollers,
G G G, and the cloth ; the latter moves in such a direction as to
carry the candles forward towards the tray, H, whilst the rollers,
G G G, revolve in a contrary direction so as to rub and polish
the surfaces of the candles. A small circular saw, G, trims the
bases of the candles as they emerge from the tray, A. Paraffin
candles as a rule are sufficiently smooth and glossy when properly
moulded without any additional polishing.
Nigh.tligh.ts. — The use of " mortars," or mortuary candles, for
burning in death chambers, etc., is very ancient, wTax tapers being
the form usually employed until comparatively recently, when
the use of short stumpy candles of peculiar composition and
construction became general for burning at night under such
circumstances that whilst only a feeble illumination is requisite,
the flame is required to burn steadily and constantly for a number
< >f hours together.
Two different forms of " iiightlights " are now chiefly employed,
one set in a case of paper, wood-shaving, or similar material,
sufficiently fluid-tight to prevent the melted combustible material
from running out ; the other cast into shape without any such
covering. The wick in each case is generally supported at the
base by a " sustainer," consisting either of a little metal disc with
;i small central perforation through which the wick passes, or a
similar small plaster of Paris plate, &c., the object being to
prevent the wick from falling over when the light has nearly
burnt out so that little or no solid grease is left to support the
wick. The nature of the materials burnt varies considerably ;
for encased nightlights substances are generally chosen the fusing
points of which are not extremely high, so that the cost is less ;
while for nightlights of the "pyramid" kind without cases,
substances of comparatively high melting points are preferable.
Different manufacturers vary considerably in the way in which
their nightlights are prepared. Tn some instances the pasteboard
or wooden case is simply filled up with melted candle material
from a can after the bit of wick and "sustainer" are fixed in
position by means of a drop of melted grease applied after the
wick has been passed upwards through a minute hole in the
bottom of the box : such nightlights are generally placed in a
saucer of water when burnt. Others are moulded round the
wicks in much the same fashion as ordinary longer candles ; whilst
others are cast as solid cylinders of fatty matter, through the
centre of which a hole is perforated; the wick previously threaded
on a little bit of tinfoil, is passed upwards through the perforation,
N1GHTLIGHTS. 407
and fixed in position sufficiently securely by a blow carefully given
with a peculiar kind of hammer : these are generally burnt in
glass dishes without water. Palmitic acid from palm oil, highly
pressed coker stearine, and pressed tallow are the materials most
frequently employed as combustible matter ; wicks of rush pith
peeled so that two small strips of peel are left adherent on oppo-
site sides are used for some, the effect of the strips being to turn
outwards in burning, giving a well-shaped flame.
Spills for lighting candles, &c., are generally drawn by much
the same process as that above described for thin wax tapers
(p. 389), the wicks being wound on a drum after passing through
the melted composition and a suitable sized drawplate. After
cutting to length the ends are "feathered'"' by dipping into hot
water so as to melt half an inch or so of composition and giving
n vigorous shake or jerk which dislodges most of the melted
materials, slightly separating the strands in so doing.
Medicated Candles. — For the purpose of impregnating the
air of sickrooms, &c., with disinfecting vapours, certain substances
are sometimes intermixed with the candle material — e.g., iodine
and eucalyptus oil. In the latter case the effect is produced by
the volatilisation of eucalyptol from the hot cup of melted grease
at the base of the wick, that portion which is burnt in the flame
being ineffective ; with iodine, the free element is evolved from
the flame itself, hydriodic acid, if formed, being largely decom-
posed again by the heat. Sulphur * has been used in similar
fashion, sulphur dioxide being formed on combustion.
":: A spirit lamp charged with a mixture of alcohol and carbon disulphide
affords a convenient means of producing sulphur dioxide for disinfecting
chambers, &c.
408 OILS, FATS, WAXES, ETC.
§ 7. The Soap Industry.
CHAPTER XVIII.
MATERIALS USED IN THE MANUFACTURE OF SOAP.
FATTY MATTERS AND ALKALIES.
THE raw fatty materials employed in any large quantities for
the manufacture of ordinary household soaps and those used for
technical purposes, such as wool - scouring, &c., are far less
numerous than the different varieties of oleaginous matters
used for culinary, edible, and miscellaneous purposes through-
out the world in different countries ; but almost every day
new sources of oily and fatty matters from abroad are brought
to light, many of which only require suitable development to
furnish excellent material for soapmaking as well as for more
superfine uses.
The leading substances of animal origin in largest use for soap-
making are the fats of the sheep and ox (tallow), horse grease,
damaged hog's lard, kitchen grease, and similar materials derived
from trade refuse of different kinds (such as tannery, bone-
boiling and gluemaking greases), together with seal and whale
oils, cod and shark liver oils, fish oils of various kinds, and
such like materials, including sewage grease, egg yolks, and
greases recovered from soapsuds, wool washing, engine waste
cleansing, &c. Amongst the more prominent materials of vege-
table origin may be mentioned the oils and butters derived from
olives ; cotton, sesame, sunflower, rape, and linseeds ; arachis
and cokernuts ; palm fruits and kernels ; niger and poppy seeds ;
castor beans and almonds ; and in lesser degree a large variety of
analogous substances, mostly either the " foots ;' formed during
refining (p. 261), or the interior qualities obtained as the last
hot pressings, or by treatment with carbon di sulphide and similar
solvents, of the partially exhausted mass from which oils of finer
quality, suitable for superior applications, have been previously
expressed or otherwise obtained ; it being a sort of general
ALKALIES. 409
axiom that any kind of greasy or oleaginous matter can be made
into soap of a more or less useful and valuable character, even
when fit for no other applications, the coarsest kind of cart grease
and such like rough lubricants alone excepted.
A certain amount of higher priced soaps (toilet and special
varieties) is also prepared from less coarse fatty matters, in some
instances from materials of the finest qualities ; but the quantity
of these superior grades made bears only a small proportion to
the total amount of ordinary coarser soaps manufactured for
scouring and laundry purposes (vide Chap, xx.)
Alkalies. — The term alkali is usually traced to the Arabic
Al kali, a name applied to a particular plant (a kind of " glass-
wort "), the ashes of which abound in potash, and have conse-
quently been used from the earliest ages, not only for the manu-
facture of glass (whence the English trivial name), but also for
laundry and detergent purposes generally. The term " potash,"
indeed, connotes much the same idea, being originally applied to
the soluble part of woodashes dissolved out by water and re-
covered by boiling down the solution in a pot ; pearlash being
the same material subjected to further purification so as to
whiten it. Even at the present d^y crude ashes from vegetable
combustibles are often used as a detergent without purification,
the earthy and calcareous insoluble matters present serving
rather to aid scouring purposes ] thus, cigar ash furnishes a
very effective dentifrice.*
The difference in character (from the soap boiler's point of
view) between the alkali contained in the ashes of inland vege-
tation (potash) and that present in marine plant ash (soda),
appears to have been known to a considerable extent to the
alchemists of the earlier and middle ages of the Christian era ;
although the essential chemical differences between the two, and
the practical identity of the latter with the mineral product
natron, were probably not so clearly understood. The effect of
treatment with quicklime so as to render " mild alkali " (car-
bonate) "quick" or "caustic," and the superior action of the
quickened product on oleaginous matters, so as to form soap,
were also more or less imperfectly known to them. At the pre-
sent day the alkalies used in soapmaking are generally (though
not invariably) used in the caustic condition because of this more
rapid action ; but saponification can be effected by carbonated
alkalies if sufficient time be allowed, or if the action be acceler-
ated by increased heat and pressure. In all probability the
action of an alkaline carbonate essentially consists in the forma-
* A few years ago an ancient tomb was duo; up in Rome ; a quantity of
what appeared to be ashes were found therein, which were appropriated
by one of the workmen for his wife to use in washing. It subsequently
transpired that the ashes were the remains of the Emperor Galba, who was
cremated some eighteen centuries ago (Time*).
410 OILS, FATS, WAXES, ETC.
tion of soap and bicarbonate ; thus with stearin and sodium
carbonate —
Stearin. Sodium Carbonate. Water. Glycerol.
C3H5(C18H3502)3 + 3NaaC03 + 3H,0 C3H5(OH)3
Sodium Stearate. Sodium Bicarbonate.
+ 3Na(C]8H35O2) + 3NaHCO3.
Under the influence of heat the bicarbonate breaks up into
carbon dioxide, water, and neutral carbonate, which last then
reacts as before —
Sodium Bicarbonate. Sodium Carbonate. Carbon Dioxide. Water.
2NaHC03 Na2C03 + C02 + H20.
Ammonia usually exerts a considerably less; energetic saponi-
fying action on most kinds of fatty matters than the fixed
.alkalies ; whilst lime, magnesia, zinc oxide, lead oxide, and
.similar materials, although useful in the preparation of earth}'
and metallic soaps for other purposes (candlemaking, preparation
of lead plasters, tfec.), are not used in the direct manufacture
of ordinary soaps ; excepting in so far as small quantities of lime,
iron, and other metallic soaps are often present therein as im-
purities derived from the water or the materials and utensils
used, &c.
Formerly the manufacture of alkali, especially soda, was very
frequently conjoined with that of soap ; but of late years it has
become more usual to dissever the two trades, the soapboiler
purchasing either caustic or carbonated alkali from the alkali
manufacturer instead of preparing it himself. At one time the
chief source of potash was the ashes of terrestrial vegetation
/whence the term " vegetable alkali ") ; but mineral potassium
chloride (chiefly from the Stassfurth deposits) is now largely
employed as raw material, being converted into potassium
carbonate by the Leblanc process.* Similarly, in the earliest
ages, soda (natron) was derived from saline efflorescences on the
soil, whence the term " mineral alkali ;" subsequently, the ashes
of seaweeds and marine plants furnished a cheaper source known
as "barilla;" whilst latterly, soda produced by the method of
Leblanc, or by the more recent "ammonia process" for converting
rocksalt into sodium carbonate, has mostly superseded all other
kinds. By either of these processes, "soda ash" (more or less
impure anhydrous sodium carbonate) and "caustic soda" (sodium
hydroxide) are prepared in the solid state, the latter being
usually put up in airtight iron drums for transport and preserva-
tion ; when caustic liquors of a given strength are requisite, they
* Conversion into sulphate by treatment with sulphuric acid, and subse-
quent heating of the sulphate with small coal and calcium carbonate, so as
to form alkaline carbonate and calcium sulphide (as "black ash"), separated
by dissolving out the former by means of water.
CAUSTICI8IN6 PROCESS. 411
are readily prepared by simply dissolving a known weight of the
solid caustic soda in a given volume of water, and are then ready
for use. When, however, sodium carbonate or potassium
carbonate is bought, before caustic leys suitable for soap boiling
can be obtained, the operation of " causticising " must be gone
through, consisting in dissolving the carbonated alkali in water,
adding lime, and boiling up with agitation so that the calcium
hydroxide and alkaline carbonate may react on one another in
accordance with the equations —
Sodium Carbonate. Slaked Lime. Caustic Soda. Calcium Carbonate.
+ CaHA = . 2NaOH + CaC0
Potassium Carbonate. Calcium Hydroxide. Potassium Hydroxide. Calcium Carbonate.
K._,CO, + CaFLO, 2KOH + CaC03
Causticising Process. — Tii the earlier days of soapmaking
the causticising of the alkalies employed was generally effected
in the cold ; a purer ley being thus obtained from crude " ashes "
(rough potashes and "black ash") than when the whole was
boiled up together, and then allowed to settle. At the present
<lay this method of treatment is but seldom employed in this
country, although still in use on the Continent. In order to
carry it out to the best advantage the bottom of the vat is
covered with lumps of quicklime, over which water is thrown to
slake it ; 5 parts of soda ash * for every 6 of quicklime originally
used are then shovelled in on the top as uniformly as possible.
Another layer of lime is then added, and a second of soda ash,
equal in weight to the lime ; then a third layer of lime, and a
third of soda ash, equal to the second layers. Water, or weak
runnings from a previous batch, is then gradually run on, and
the whole allowed to stand till next day, when the caustic soda
ley formed is run off through a cock at the base of the vat into
<i settling tank. More water is then added and allowed to stand
as before, and finally run off, giving a much weaker liquor either
mixed with the first, or used for lixiviating another batch. The
lime mud is then stirred up with more water, and the final weak
liquor thus obtained used to work a new batch. Conveniently
three (or even four) vats are worked in series, exactly like black
ash lixiviating tanks; the second liquor from No. 2 is passed
through No. 1, coming out of full strength, being itself obtained
as the third liquor from No. 3, which is then exhausted. No. 3,
being refilled, then becomes No. 1 of a new series ; the former
No. 1 becomes the second; and so on, methodically. Crude
Leblanc soda liquors are much less frequently used now than
* Theoretically, 106 parts of Na2C03 are equivalent to 56 parts of CaO ;
a considerable excess of lime, however, is requisite to ensure causticising
in the cold. For steam boiling in practice 200 parts of soda ash are used
per 100 of quicklime.
412
OILS, FATS, WAXES, ETC.
was the case before the ammonia soda process had made much
headway ; when carbonated alkali, free from sulphide, is treated
(as when ammonia soda ash is employed, or Leblanc soda ash
prepared from the " salts " that separate on evaporating the crude
liquors obtained on lixiviating black ash), the plant used consists
simply of some form of steam vessel, such as an old boiler, pro-
vided with an efficient agitator ; lumps of quicklime are added
(preferably placed on a grating or enclosed in a sort of cage to
keep back hard lumps and stones when the lime disintegrates by
slaking), and the whole boiled up for one or more hours until
the operation is complete, either under pressure in a closed vessel
(whereby a considerable saving of fuel and labour is effected),
or by means of wet steam in an open pan. If, on the other
hand, crude black ash liquors be used (impure sodium carbonate,
tfec., dissolved out from black ash by water, containing sulphide
owing to the reaction of sodium carbonate" solution on calcium
sulphide), or the " red liquors " obtained as mother liquors when
the crude black ash liquor is evaporated until " salts " (mostly
sodium carbonate) crystallise out during evaporation, the causti-
cising action of lime is conveniently conjoined with the oxidising
action of a current of air blown into the fluid for the purpose of
destroying sulphide by conversion into thiosulphate, sulphite,
and sulphate ; for which purpose a vessel is employed provided
at the base with a large rose jet or spiral tube pierced with
holes, or a perforated false bottom, through which the air and
steam are blown in together so as to keep the whole in agita-
tion and effect the causticising and oxidation simultaneously.
Finally, the whole is allowed to stand at rest awhile, so that
the " lime mud " (calcium carbonate, £c.) may settle, and the
clear caustic alkali solution run off or pumped into tanks for
storage. These are generally made of boiler plate rivetted
together (Fig. 107). When intended to hold ley for toilet soap,
Dussauce recommends that they
should be lined with sheet lead to
prevent possible discoloration of
soap through contact of the ley
with iron.
In order to causticise the car-
bonate thoroughly an excess of
lime is desirable ; the remaining
caustic lime in the lime mud, if
of sufficient quantity to be worth
saving, may be utilised by boiling
up again with a fresh batch of
carbonated liquors ; after allowing
Fig. 107.
to settle, the clear liquor is pumped off to another pan,
where the causticising is finished with another batch of fresh
lime, the mud from which operation is again boiled up with
CAUSTICISING PROCESS. 413
fresh carbonated liquor, and so on continuously alternately. The
lime mud resulting from the second treatment with carbonated
liquors usually contains too little caustic lime to be worth using
a third time ; but by boiling up with water the adhering soda
solution is mostly washed out, and a weak ley obtained, utilised
either to dissolve more carbonated alkali, or for other purposes
in the factory.*
To ciusticise sodium carbonate solution thoroughly, the liquor
must not be too strong, otherwise a considerable portion of the
alkaline carbonate escapes the causticising action of the lime ; on
the other hand, when the leys are made too weak, the quantity of
salt subsequently requisite for " salting out " the soap (Chap, xx.)
is increased. When the open pan system is adopted, a sufficiently
complete degree of causticising is generally effected by using
liquors of such strengths that the ley finally obtained has a
specific gravity not exceeding about 1-075 to I'lO (15° to 20° Tw.),
although slightly higher strengths, up to specific gravity I'll or
1'125 (22° to 25° Tw.), are sometimes made; by causticising
under pressure, considerably stronger leys may be effectively
prepared, provided that the subsidence of the lime mud and the
running off of the clear ley is still effected under the same
pressure ; thus, with a pressure of 50 Ibs. per square inch, caustic
leys up to specific gravity 1-16 to 1'20 (32° to 40° Tw.) may be
readily prepared, provided this precaution is adopted ; otherwise
the reverse action goes on, caustic soda reacting on calcium
carbonate so as to reproduce sodium carbonate (Parnell). When
more concentrated leys are required, they are obtained by
quickly boiling down with as little access of air as possible ;
weaker leys are got by diluting stronger ones with water, or
with the very weak liquors obtained by " washing " the lime
mud left after running off the caustic liquor — i.e., by adding
water to the mud, boiling up, allowing to settle, running off
the weak ley thus obtained, and repeating the operation so as to
obtain another batch of still weaker washings. The storage
tanks in which the caustic leys are kept should be well closed to
prevent absorption of carbonic acid from the air ; this is some-
times done by pouring a layer of paraffin oil or melted paraffin
wax on the ley, of course taking the requisite precautions to
avoid any hydrocarbon being drawn off with the ley used for
making soap ; when properly prepared, no visible disengagement
of bubbles of gas should be noticeable on adding sufficient hydro-
* The lime mud finally obtained from soda leys usually retains a notable
proportion of sodiiim carbonate in a form insoluble in water, chiefly as a
double carbonate of calcium and sodium. This may be regained in Leblanc
alkali works by drying and using the impure calcium carbonate obtained
over again in the black ash operation ; but in an ordinary soap work,
where the residual lime mud is little better than a waste product, the soda
thus retained in the lime mud is usually lost.
414 OILS, FATS, WAXES, ETC.
chloric or other mineral acid to supersaturate the alkali ; this
serves as a test of completion during the causticising process.
In order to know what quantity of alkali is used for a given
operation, the tanks are fitted with gauges ; so that if the level
is reduced by a given number of inches, for instance, it is known
that so many gallons of fluid have been run off ; the alkaline
strength of the fluid being known, the total weight of alkali
present in the fluid run off is then known. In general it is
more convenient to arrange the ley tanks at an elevation (in
the upper part of the factory) so as to run off the leys by
gravitation, than to have them in the basenient and pump
up the leys to the coppers, although this latter arrangement
economises space.
Valuation of Alkalinity of Leys. — In order to determine
the alkaline strength of soap leys with absolute accuracy, a
volumetric assay with a standard acid solution must be employed ;
but for general soapmaking purposes, the specific gravity of the
solution is a sufficiently near indication. It should be borne in
mind, however, that the specific gravity is only to be trusted as
an indication of alkalinity in cases where the character of the
liquor is always sensibly the same — i.e., where the proportion of
saline matters other than caustic alkali (sodium or potassium
chloride, sulphate, &c.) does not vary much. This is usually the
case when soda ash, <fec., of a tolerably uniform quality is always
employed ; but when different grades are used at different times,
leys may easily be obtained of considerably different alkaline
strengths although of the same specific gravity. Thus, if soda
ash be used, made by the ammonia process and containing say
56 per cent, of " anhydrous soda " (Na0O = 62), equivalent to-
about 96 per cent, of anhydrous sodium carbonate, Na2CO3, a ley
having a given specific gravity (say 1-075) at the ordinary
temperature will be notably stronger in alkali, bulk for bulk,
than a similar ley prepared from Leblanc soda of say 52 per cent.,
equivalent to about 89 per cent, of anhydrous carbonate, because
the latter contains a larger proportion of sodium salts (chloride,
sulphate, &c.), which increase the relative density of the liquor
without adding to its alkaline strength. A fortiori, if a "48 per
cent, soda ash " (i.e., an ash containing alkali equivalent to
only 48 per cent, of Na.,O, equivalent to about 82 per cent, of
Na2CO3) be used, the alkaline strength of the ley will be lower
still for the same specific gravity, since, in order to reduce the
alkalinity of the ash to "48 degrees" (48 per cent. Ka2O), an
extra amount of some diluting agent (usually salt) must be
added. Similar remarks obviously apply to potash leys made
from potash of different grades, and to caustic soda leys made
by directly dissolving solid caustic soda in water; the ley
from a " 70 per cent, caustic " (containing 70 per cent.
= about 90 per cent. NaOH) will usually be stronger,
ALKALINITY OP LEYS.
415
bulk for bulk, at a given specific gravity than that from a
" 60 per cent, caustic " (containing 60 per cent. Na2O = about
77 per cent. NaOH), except in so far as the difference in
strength between the two kinds of caustic is due simply to water,
and not to saline matters, such as sulphate and chloride.
The following tables exhibit the relationships between the
alkaline strengths of pure solutions of sodium and potassium
hydroxides and carbonates, and their respective specific gravities,
at the ordinary temperature (15° C.), or at more elevated tem-
peratures : —
*
SPECIFIC GRAVITV OF CAUSTIC SODA SOLUTION AT 15° (Tunnermanri).
Specific Gravity.
Per Cent, of Na2O
Specific Gravity.
Per Cent, of Na20.
1-42S5
30-22
1 -2392
15-11
1-4193
29-62
•2280
14-50
1-4101
29-01
•2178
13-90
1-4011
28-41
•2058
13-30
1-3923
27-80
•1948
12-69
1-383G
27-20
•1841
12-09
1-3751
26-59
•1734
11-48
1-3668
25-99
1-1630
10-88
1 -3580
25-39
1-1528
10-28 -
1 -3505
24-78
1-1428
9-67
1-3426
24-18
1-1330
9-07
1-3349
23-57
1-1233
8-46
1-3273
22-97
1-1137
7-86
1-3198
22-36
-1-1042
7-25
1 -3143
21-89
1-0948
6-65
1-3125
21-76
1-0855
6-04
1-3053
21-15
10764
5-44
1 -2982
20-55
1-0675
4-84
1 -2912
19-95
1-0587
4-23
1 -2843
19-34
1-0500
3-63
1 -2775
18-73
1-0414
3-02
1-2708
18-13
1 -0330
2-42
1-2642
17-53
1-0246
1-81
1-2578
16-92
1-0163
1-21
1-2515
16-38
1 -0081
1-60
1-2453
15-71
1 -0040
1 30
416
OILS, FATS, WAXES, ETC.
SPECIFIC GRAVITY OF CAUSTIC SODA SOLUTION AT 15°
(Lunge and Hurter).
Specific Gravity.
Grammes of Na20
per Litre.
Specific Gravity.
Grammes of Na20
per Litre.
1-005
3-7
1-260
228-9
1-010
7'5
1 270
240-0
1-020
15 1
1-280
251-0
1 -030
22-6
1 -290
252-1
1-040
30-2
•300
273-2
1 -050
377
•310
285-4
1-060
45-5
•320
297-7
1-070
53-2
•330
309-9
1-080
61-0
•340
322-2
1-090
68-8
•350
334-4
1-100
76-5
•360
347-2
1-110
84-3
•370
360-1
1-120
92 -1
•380 .
372-9
1-130
100-5
•390
385-7
1-140
109-6
•400
398-5
1-150
118-6
•410
411-8
1-1(50
1277
•420
4250
1-170
136-8
•430
438-2
1-180
145-8
•440
451-4
1-190
154-9
•450
464-6
1-200
l'J4-0
•460
479-9
1-210
174-7
•470
495-3
1-220
185-5
•480
510-6
1 -230
196-3
•490
525-9
1-240
207-0
•500
541-2
1-250
217-8
INFLUENCE OF TEMPERATURE ox THE SPECIFIC GRAVITY OF
CAUSTIC SODA SOLUTION.
Temperature.
Specific Gravity.
Degrees C.
0 1-015
1-030
1-060! 1-100
•150
1-200
1-250
1 -320
•370
10
1-012
1-027
1-057 1 1-097
•146
1-195
1-245
1315
•365
20
1-009
1-024
1 054' 1-093
•142
1-190
1-240
1 -310
•360
30
1 -007
1-022
1-052 1-091 -138
1-186
1-235
1 -305
•355
40
1 003
1-018
1-048 1-087 -136
1-181
1 -231
1-299
•350
50
0-999
1-014
1-044 1-082 -129
1-177
1-226
1-294
•345
60
•994
1-009
1-039 1-077 '124
1-173
1-221
1-288
•339
70
•988 ! 1 -003
1-033 1-071
•118
1-168
1-216
1 '283 1 1 -334
80
•982
•997
1-027 1-065
1-112
1-162
1-211
1-277
1-329
90
•977
•992
1-022 [ 1-059
1-107
1-156
1-206
1-271
1-324
100
•971
•986
1-016 1-053
1 101
1-151
1-200
1-265
1-319
ALKALINITY OF LEYS.
417
SPECIFIC GRAVITY OF CAUSTIC POTASH SOLUTION AT 15° (Tunnermann).
Percentage of
Percentage of
Specific
SpeciSc
Gravity.
KHO.
K30.
Gravity.
KHO.
K20.
1-3300
33-69
28-29
1-1437
16-85
14-15
1 -3131
32-35
27-16
1-1308
15-50
13-01
1-2966
31-00
26-03
1-1182
14-15
11-88
T2805
29-65
2490
1-1059
12-80
10-75
1-2648
28-30
2376
1-0938
11-46
9-62
1-2493
26-95
22-63
1-0819
10-11
8-49
1-2342
25-61
21-50
1-0703
8-76
7-36
1-2268
24-93
20-94
1-0589
7-41
6-22
1-2122
23-59
19-80
1 -0478
5-96
5-00
1-1979
22-24
18-67
1 -0369
4-72
3-96
1-1839
20-89
17-54
1 -0260
3-67
2-83
1-1702
19-54
16-41
1-0153
2-02
1-70
1-1568
18-20
15-28
1 -0050
0-674
0-566
SPECIFIC GRAVITY OF CAUSTIC POTASH SOLUTION AT 15°.
(Lunge and Hurter).
Grammes per Litre.
Grammes per Litre.
Specific
Gravity.
Specific
Gravity.
K20.
KOH.
K20.
KOH.
1-007
7
9
1-252
284
338
1-014
14
17
1 263
297
353
1-022
22
26
1-274
308
368
1-029
30
36
1-285
321
385
1-037
39
46
1-297
335
398
1-045
49
58
1-308
349
416
1-052
57
67
1-320
363
432
1-060
66
78
1-332
377
449
1-067
74
88
•345
394
469
1-075
83
99
•357
410
487
1-083
92
109
•370
425
506
•091
100
119
•383
440
522
•100
111
132
•397
457
543
•108
119
143
•410
472
563
•116
129
153
•424
490
582
•125
140
167
•438
509
605
•134
150
178
•453
530
631
•142
159
188
•468
549
655
•152
170
203
•483
571
679
1-162
181
216
•498
593
706
1-171
192
228
•514
615
731
1-180
203
242
•530
635
756
1-190
214
255
•546
655
779
1-200
226
269
•563
681
811
1-210
237
282
•580
706
840
1-220
248
295
1-597
731
870
1-231
260
309
1-615
759
902
1-241
272
324
1-634
789
940
418
OILS, FATS, WAXES, ETC.
SPECIFIC GRAVITY AT 15° C. or SODIUM CARBONATE SOLUTION
(Lunge and Hurter).
Specific
Gravity.
Percentage of
Specific
Gravity.
Percentage of
NacO.
Na2C03.
Na20.
Na2C03.
1-005
0-28
0-47
1-080
4-42
7-57
1-010
0-56
0-95
T085
4-70
8-04
1-015
0-84
1-42
1-090
4-97
8-51
1-020
1-11
1-90
1-095
5'24
8-97
1-025
1-39
2-38
1-100
5-52
9-43
i
1-030 1-67
2-85
1-105
5-79
9-90
1-035
1-95
3-33
1-110
6-06
10-37
1-040
2'22
3-80
1-115
6-33
10-83
1-045
2-50
4-28
1-120
6-61
11-30
1-050
2-78
4-76
1-125
6-88
11-76
1 -055
3-06
5-23
1-130
7-15
12-23
1-060
3-34
5-71
1-135
7-42
12-70
1-065
3-61
6-17
1-140
770
13-16
1-070
3-88
6-64
1-145
7-97
13-63
1-075
4-16
7-10
1-150
8-24
14-09
SPECIFIC GRAVITY AT 30° C. OF CONCENTRATED SODIUM CARBONATE
SOLUTION (Lunge and Hurter).
Specific
Gravity.
Percentage of
'Specific
Gravity.
Percentage of
Na20.
Na2C03.
Na20.
Na2C03.
1-140
7-97
13-62
1-230 12-48
21-33
1-150
8-46
14-47
1-240
12-98
22-20
1-160
8-96
15-32
1-250
13-49
23-07
1-170
9-46
16-18
1-260
14-00
23-93
1-180
9-96
17-04
1-270
14'49
24-77
1-190
10-46
17-89
1-280
14-98
25-61
1-200
10-97
18-75
1-290
15-47
26-45
1-210
11-47
19-61
1-300
15-96
27-29
1-220
11-97
20-47
1-310
16-45
28-13
CORRECTION FOR IMPURITIES.
419
POTASSIUM CARBONATE (Gerlach).
Percentage
of K2C03.
Specific
Gravity at 15°.
Percentage
of K2C03.
Specific
Gravity at 15°.
Percentage
of K2C03.
Specific
Gravity at 15°.
1
1-0091
19
1-1827
37
1-3828
2
1-0183
20
1-1929
38
1-3948
I
1-0274
21
1-2034
39
1-4067
4
1-0366
22
1-2140
40
1-4187
5
1-0457
23
1-2246
41
1-4310
6
1-0551
24
1-2352
42
1-4434
7
1-0645
25
1-2458
43
1-4557
8
1 -0740
26
1-2568
44
1-4681
9
1 -0834
27
1-2679
45
1 -4804
10
1-0928
28
1-2789
46
1-4931
11
1-1026
29
1-2900
47
1-5059
12
1-1124
30
•3011
48
1-5186
13
1-1222
31
•3126
49
1-5314
14
1-1320
32
•3242
50
1-5441
15
1-1418
33
•3357
51
1-5573
16
1-1520
34
•3473
52
1-5705
17
1-1622
35
•3589
52-024
1-57079
18
1-1724
36
1-3708
The above tables only apply to pure solutions of alkaline car-
bonates and hydroxides ; with commercial substances containing
other neutral saline matters (chloride, sulphate, &c.) a correction
is necessary to allow for the increment in specific gravity brought
about by the presence of these impurities without any corre-
sponding increase in alkaline strength : the amount of this cor-
rection necessarily varies with the proportion and nature of the
saline matter present, and consequently no very accurate allow-
ance on this score is practicable in most cases ; but an approxi-
mation sufficiently near for most practical purposes is obtained
by assuming that the effect of a given quantity of neutral saline
matter in increasing the specific gravity is the same as that of
the same quantity of actual alkali ; so that if it is known that a
given sample contains n per cent, of neutral saline matters,
together with 100 - n per cent, of actual alkali (reckoned on the
sum of alkali and salts as 100), the correction is obtained by
subtracting from the tabular number corresponding with the
particular specific gravity n per cent, of its value. Thus, for
example, if a solution of sodium carbonate be made from a soda
ash, &c., where the saline impurities (sulphate, chloride, &c.)
jointly represent 5 per cent, of the total solids dissolved (the
sodium carbonate consequently representing 95 per cent.), the
amount of sodium carbonate given in the table for a given
specific gravity is to be reduced by 5 per cent, of its value.
Similarly if the actual caustic soda, NaOH, in a sample of
commercial caustic be 90 per cent., and the saline impurities
420 OILS, FATS, WAXES, ETC.
10 per cent., of the total soluble solid matters present (exclusive
of moisture), the tabular number must be decreased by 10 per
cent, of its value. Where more exact valuations are requisite,
as is sometimes necessary in order to avoid using excess or
deficiency of alkali, specific gravity indications must be dis-
carded, and the results of alkalimetrical assays substituted
for them ; for this purpose a normal or seminormal solution of
hydrochloric or sulphuric acid is convenient, using an indicator
not affected by carbon dioxide (litmus employed in hot solution,
cochineal, methyl orange, &c.) *
English, French, and German Degrees. — A peculiar trade
custom obtains in Britain whereby the alkaline strength of
soda ash and caustic soda is represented as higher than the
truth to the extent of about 1'32 per cent, or 1 part in 76.
This is brought about by the incorrect assumption that the atomic
weight of sodium is 24 instead of 23 ; whence the percentage
of Na2O in pure sodium carbonate, Na2CO;], is reckoned as
^4 x 100 = 59-26, instead of ^ x 100 - 58:49. Hence 58-49
108 lOb
parts of soda are reckoned as 5 9 -2 6, thus giving an error in
excess of 0'77 in 58-49 = 1-32 in 100. A still more erroneous
mode of calculation was recently current in some districts, based
on the same assumption that Na = 24 ; only in this case the
molecular weight of Na2O was reckoned as 64 instead of 62,
thus giving an error in excess of 2 parts in 64 --= 3-23 parts in
100, more than twice the former error.
In Germany the alkaline strength is usually expressed in
"degrees" representing the percentage of pure Na2CO3 equi-
valent to the alkali present — i.e., pure sodium carbonate would
be a soda ash of 100°. In France " Descroizilles degrees " are in
use, representing the quantity of pure sulphuric acid, H2SO4,
neutralised by 100 parts of soda ash — i.e., pure sodium car-
bonate, Na.,CO.?, would represent a product of strength equal to
98
_ — x 100 = 92° -45 Descroizilles. The. relationships between
Descroizilles and German degrees and the true percentage of
anhydrous soda (Na9O = 31, not affected by the above named
errors in excess due to English trade customs) are consequently
given by the formula —
* When it is required to determine the amount of alkali present in the
caustic and in the carbonated state, two assays are requisite ; in one case
the total alkali is determined contained in a given volume of fluid ; in the
other the same volume of solution is boiled with barium chloride or nitrate,
and after cooling, made up to double the original bulk with water ; after
subsidence or filtration the caustic alkali in half the total fluid is determined,
and the amount found doubled and subtracted from that found in the first
assay. The difference represents the carbonated alkali present with more
or less accuracy according as access of carbonic acid from the air has been
avoided during the operations.
ENGLISH, FRENCH, AND GERMAN DEGREES.
421
I)
40
G
53
where S is the alkaline strength expressed as percentage of Na2O
(equivalent 31 — sometimes spoken of as the strength in "Gay
Lussac degrees ") ; D the same in Descroizilles degrees (equivalent
of H.2SO4 = 49) ; and G the same expressed in German degrees
(equivalent of Na,CO3 = 53).
From this formula result the equations —
S
D -
49 "
31
53 °
49
31S
G
G = .—
= 0-6327 D
= 0-5849 G
= 1-5806S
= 0-3245 G
- 1-7097 S
= £D = 1-0316D
The following table represents the same relationships —
S.
D.
G.
S.
D.
G.
2
3-16
342
42
66-39
71-81
4
6-32
9-84
44
69-55
75-23
6
9-48
10-26
46
72-71
78-66
8 12-64
13-68
48
76-87
82-07
10 15-81
17-10
50
79-03
85-48
12 18-97
20-52
>52
82-19
88-90
14 22-13
23-94
54
85-35
92-32
16 25-29
27-36
56
88-52
95-74
18 28-45
30-78
58
91-68
99-16
20
31-61
34-20
60
94-84
102-58
22
34-77
37-62
62
98-00
106-01
24 37-93 41-04
64
101-16
109-43
2<i
41-09 44-46
66
104-32
112-85
28 44-25 47-88
68
107-48
116-27
30
47-42
51-29
70
110-64
119-69
32
50-88
54-71
72
113-81
123-10
34
53-74 58-13
74
116-97
126-52
36
56-90 61-55
76
120-13
129-94
38
60-06 64-97
77 '5
122-50
132-50
40
63-22
68-39
Calculation of Quantity of Alkaline Ley requisite for
Saponiflcation. — When an alkaline solution of known strength
(either determined by titration, or inferred from the specific
422 OILS, FATS, WAXES, ETC.
gravity after correction of the tabular value for saline impurities)
is to be used for converting into soap a given kind of fatty matter
or mixture of fats, &c., the quantity requisite for exactly saponi-
fying a given weight of fat depends not only on the alkalinity
of the ley but also on the mean saponification equivalent of
the fatty matters (p. 158) ; the lower the value of this latter
quantity the more alkali will be required, the relationship being
indicated thus — Let E be the mean saponification equivalent of
the fats, etc., used ; then E units of weight of fat will be equivalent
to 31 units of Na2O (or to 40 of NaOH, 47-1 of K,O, or 56-1
of KOH). Let 1~000 parts by weight of alkaline ley be equi-
valent to 0J parts of Na2O (or to a.2 of NaOH, a3 of K20, or «4 of
KOH) — i.e., let a1 («„, as, or a4) be the permillage of alkali in
the ley. Then E units of weight of fat will obviously be equi-
valent to 31 x — units of weight of ley (or to 40 x — ,
al \ #2
1 000 1 000\
47-1 x -' , or 56 -1 x - ) ; whence one part of fat is equi-
1,000 I4 31,000 / 40,000
valent to 31 x - - x = = - — ^ parts of ley or to - — ^,
a1 E «1 x L A \ a.2 x Jjj
— , or — - — ., parts). Thus one part by weight of cokernut
«3 x E «4 x E r /
oil of mean saponification equivalent 215 wrill be exactly saponified
by — , r = 0'846 parts of caustic soda ley containing 220 per
mille of NaOH ; whilst one part of linseed oil of mean saponifi-
cation equivalent 291 '5 will correspond with •=- ?-= = 1*077
150 x 291-5
parts of a potash ley containing total active alkali (caustic +
carbonated) equivalent to 150 per mille of K2O ; and so
on.
When the alkalinity of the leys is expressed as parts ~by weight
per unit of volume (grammes per litre, pounds per gallon,* &c.)
the above calculation still applies in slightly modified form.
Let the alkaline ley contain bl grammes of Na^O per litre (b>2
grammes of NaOH, b3 of K0O, b± of KOH), then E grammes of
. . 31 ... . , / 40 47-1 56-1
fat are equivalent to - - litres of ley f or to — -, -y— , or —=-•
litres J ; whence 1 gramme of fat represents -.— ^ -^ for 7-^-^5
* A solution of anything containing n grammes per litre (n milligrammes
per c.c. or n kilogrammes per cubic metre), contains n pounds per hecto-
gallon (100 gallons), since 1 gallon of water weighs 10 Ibs. Hence when
laboratory estimations are made, as usual, on the metrical system, the
results can, if required, be referred to pounds and gallons for practical
British works' use in a "Very simple way.
QUANTITY OF LEY REQUISITE FOR SAPONIFICATION.
, or T -- ™ res o
56,100\
423
y =, v/x , — ™ ) litres of ley ; or 1 kilogramme represents
31,000 /40,000 47,100 56,100\
or j-l— ) litres. Thus, one kilo.
bt x E \b2 x E' bs x E'
of cokernut oil (E = 215) would be exactly saponified by
r.TTTT^ — JTT^- = 0-930 litres of caustic soda solution of such
200 x 21o
strength that 1 litre = 200 grammes NaOH; or 1 kilo, of lin-
seed oil (E = 291-5) would correspond with -^---7^- OQ, = 1'029
10/ "U X ZiV I'D
litres of potash ley of which 1 litre = 157'0 grammes K2O.
™ f n ' * w ' f 40'000 l 56'100 f
Ihe following table gives the values of — ^ — and — ^ — for
Talues of E between 190 and 400 ; by its means the number of
litres, x, of caustic soda (or potash) solution can be readily
calculated, requisite for the saponification of a kilogramme of any
fatty mixture the mean saponification equivalent of which is E,
by the simple formula —
n
X = TVf'
where n is the tabular number corresponding with E, and N the
number of grammes of NaOH (or of KOH) contained in a litre of
the ley used : —
E.
40,000.
Difference.
56,100.
E
Difference.
E
190
210-5
295-2
200
200-0
10 -5
280-5
14 7
210
190-5
9-5 -
267-2
13-3
220
181-8
8-7
255-0
12-2
230
173-9
7-9
243-9
11-1
240
166-7
7-2
233-7
10-2
250
160-0
6-7
224-4
9-3
260
153-8
6-2
215-8
8-6
270
148-1
5-7
207-8
8-0
280
142-8
5-3
200-4
7-4
290
137-9
4-9
193-5
6-9
300
133-3
4'6
187-0
6-5
310
129-0
4-3
181-0
6-0
320
125-0
4-0
175-3
5-7
330
121-2
3-8
170-0
5'3
340
117-6
3-6
165-0
5-0
350
114-3
3-3
160-3
4-7
360
111-1
3-2
155-8
4-5
370
108-1
3-0
151-6
4-2
380
105-3
2-8
147-6
4-0
390
102-6
2-7
143-8
3-8
400
100-0
2-6
140-25
3-55
424 OILS, FATS, WAXES, ETC.
Thus, suppose a mixture of tallow, palm oil, and cokernut oil to
have the mean saponification equivalent 250 ; then n = 160r
and the number of litres of caustic soda solution requisite to
saponify a kilogramme is — -^--> where N is the number of
grammes of NaOH contained in a litre of the ley; if N = 1GO
the quotient is, obviously, 1,000 — i.e., 1 litre exactly is re-
quired ; whilst for stronger and weaker solutions, where N is
respectively 320 and 80, the corresponding quotient values are
0-500 and 2 '000 — i.e., exactly 0*5 litre of the stronger fluid is
required, and 2*0 litres of the weaker one.
If the saponification equivalent is not exactly indicated by
the table, the value is readily obtained by interpolation by
means of the difference columns without introducing any material
error; thus a commercial "oleine" (impure oleic acid) of which
the saponification equivalent is 282*5 corresponds with a value
A-0 000
for ^— of 142-8 - 0-25 x 4'9 = 141-6; hence, if a soda ley
containing 293-6 grammes of NaOH per litre be used (N = 293*6),
-1 A~\ ./? . -'.
= 0-482 litre of ley will contain alkali exactly corre-
— • ' ' * *O
spending with 1 kilo, of fatty matter.
Obviously, the above formula x= --7 will also enable the
number of parts by weight of ley to be calculated, requisite to
saponify one part by weight of fatty matter of mean equivalent
E, if N denote the permillage of NaOH (or of KOH) in the
ley. Thus in one of the examples above quoted, one part of
cokernut oil of equivalent 215 represents a value for ' , - of
190'5 - 0-5 x 8-7= 186-1 ; whence the quantity of soda ley at
220 per mille of NaOH, equivalent thereto is — — = 0-846 part,
as before.
When it is required to use fatty matters and alkaline leys in
as nearly as possible equivalent quantities so as to avoid excess
of either constituent, calculations such as the foregoing afford
the simplest method of arriving at the relative quantities
requisite. In practice, when the same kind of operation is
to be repeated over and over again as a matter of routine,
the fatty matter employed being sensibly of the same quality
throughout, it usually suffices to gauge the tanks and vessels
employed once for all by means of calculations founded on
these principles, and preferably checked by careful analyses
of the resulting products ; the weight of fatty matters taken and
their mean saponification equivalent being practically constant
for each operation, the volume of alkaline ley used is slightly
QUANTITY OF LEY REQUISITE FOR SAPONIFICATIOX. 425
increased or diminished below that corresponding with the
original gaugings according as the alkalimetrical test of the
liquor (or the value deduced from its specific gravity) shows
that it is a little below or above its normal strength — i.e., that
pertaining to the original gaugings.
When it is required to calculate the amount of sodium or
potassium hydroxide or carbonate equivalent to a given amount
of anhydrous oxide, or vice versd, the following formulae may be
employed, based on the molecular weights —
Na = 23
Na20 = 6'2
NaOH = 40
Na2C03 = 106
K 39-1
KoO = 94 -2
KOH = 56' I
K2C03 = 138'2
Let a given weight A of .Na.,O be equivalent to B of
and C of Na.,CO3 ; and let a given weight D of K2O be equivalent
to E of KOH: and F of K2CO3 : then—
To reduce Formula.
NaOH to Na20 A ^^^ T> = °'""50 B
Na2C03 to Na20 A = ^ C = 0-5849 C
9 v 10
Na20 to NaOH B = ^— A = 1-2903 A
Na2C03 to NaOH B = '^T C = 0'7547 C
Na20 to Na2C03 C ^ A T7097 A
106
NaOH to Na2C03 C = ^ ™^ B = 1-3250 B
04-9
KOH to K20 D = g^P^l E = °'8396 E
94 '2
K2C03 to KaO D = -j^ F = 0-6816 F
K20 to KOH E - 2-^4^ D = 1 1911 D
9 v ^fi-1
K2C03 to KOH E - -Tooo F = '8119 F
lOo —t
1 ^8 *2
K20 to K2C03 F = j~ D = 1-4671 D
1 qq .o
KOH to K2C03 F - o-^^Y E = 1-2317 E
Thus a solution of sodium hydroxide of specific gravity 1-206
containing 13-3 per cent, of NaOH will contain 13-3 x 0-775 =
10-3 per cent, of Na2O ; one containing 21'5 per cent, of K2CO3
is equivalent to another containing 21*5 x 0*8119 — 17*46 per
cent, of KOH * and so on.
426 OILS, FATS, WAXES, ETC.
The following analogous formulae may be used to calculate the
quantity of soda equivalent to a given weight of potash or vice
versd. Let H be a given quantity of sodium carbonate and I
the potassium carbonate equivalent thereto ; similarly let J be
a given amount of sodium hydroxide and K the potassium
hydroxide corresponding therewith ; and let L be a given quantity
of Na^O, and M the K2O equivalent thereto. Then —
1^ l = °'767° I
Carbonates, . .
H - 1-3038 H
J = -Jf.- K = 0-7130 J
GO 1
Hydroxides, . . .
' K ^ J 1-4025 K
L -^r M 0-6582 L
Anhydrous oxides,
M *^i L = 1-5194 M
Thus 10 per cent, of K2O in a given soap is equivalent to
10 x 0-6582 = 6-582 per cent, of Na2O. A liquor containing
8 per cent, of NaOH is of the same alkaline strength as one
containing 8 x 1-4025 = 11-22 per cent, of KOH ; and so on.
CHAPTER XIX.
SOAPMAKING PLANT.
HEATING APPLIANCES.
THE plant and appliances requisite for the manufacture of soap
vary somewhat according to the nature of the process used and
the scale on which it is conducted. Formerly the vessels (usually
known as " pans," " coppers," or " kettles ") in which the boiling
operations were conducted were uniformly mounted over free
fires, so that the flame produced by the combustion of fuel in a
fireplace placed beneath the pan was made to play over the rest
of the bottom and part of the sides of the pan by means of a
suitably arranged circular flue provided with a damper for the
purpose of regulating the draught. Several coppers were usually
mounted side by side, so that the products of combustion of their
respective fires passed into the same common tunnel or flue lead-
FREE-FIRED SOAP PANS.
427
ing to the main chimney of the works. At the present day this
system of free firing is comparatively seldom applied in the
larger soap factories, the coppers being more frequently heated
by steam supplied from a special boiler, and in some cases super-
heated before use. Fig. 108 gives a general idea of the disposi-
Fig. 108.
tion of the arrangements adopted for a free-fired pan. The
pan, J, is mounted in masonry over the fireplace, B, placed
centrally beneath it, a nearly circular flue, E, carrying the flame
round the lower part of the pan to the chimney, F ; C is the
grate or range of firebars supporting the fuel, and D the ashpit.
The leys, &c., are drawn off
as required by the tube and
draw-off cock, K ; the level
of the flooring or staging
round the pan, A, A, is raised
so that the top of the pan
projects upwards some 3 feet.
Fig. 109 represents a cast
iron pan of slightly different
type, A, also mounted so as
to be heated by free firing ;
in this case the fireplace, B,
is not placed centrally be-
neath the pan, but somewhat Fig. 109.
in front of it, the heating
being chiefly effected by the hot air chamber, E, in which
the products of combustion circulate round and under the
428
OILS, FATS, WAXES, ETC.
base of the pan before passing away to the flue. C, firebars ;
D, ashpit.
In the case of modern steam heated pans, the steam is applied
in various ways. Heating by " wet " steam consists in blowing
steam at a sufficient pressure direct into the mass to be heated,
so that the water produced by the condensation of the steam
dilutes the whole until the temperature rises so high that the
steam simply blows through without becoming materially con-
densed ; for most general boiling purposes a wet steam coil is
thus used, consisting of an iron pipe descending to near the
bottom of the copper arid terminating in a ring perforated with
holes through which the steam issues, bubbling up through the
mass and producing a very effective agitation and intermixture
of the contents when the heat is sufficient to cause the steam to
blow through. In some districts this wet steam coil is accord-
ingly spoken of as the "blowpipe;" superheated steam is some-
Fig. 11U.
times employed instead of steam supplied direct from the boiler,
so as to diminish the amount of water condensation.
Heating by " dry " steam consists in causing steam (either
direct from a high pressure boiler, or preferably for many pur-
poses, superheated) to circulate through a sort of spiral tube or
coil arranged in the lower part of the copper ; the water con-
densed in the coil accordingly does not pass into the heated
mass, thereby diluting the leys, &c., but is blown off along with
the exit steam. Dry steam is also sometimes employed to heat
an external jacket usually only surrounding the lower part of
the pan; Fig. 110 indicates the kind of arrangement — C, steam
supply pipe ; D, pipe and cock for drawing off condensed water ;
A, copper; B, steam jacket at base of copper ; E, draw off pipe
from copper. A mechanical stirring arrangement to keep the
mass agitated is conveniently added.
In order to facilitate intermixture of materials in the pan
whilst heating up by dry steam an appliance known as " Morfit's
steam twirl " is much used. Fig. Ill represents one form of
arrangement applied to a comparatively shallow copper sup-
MORFIT'S STEAM TWIRL.
429
ported by a wooden frame work, A A, B B. The steam from the
steam pipe, G, passes into a hollow spindle, D D E, the central
part of which is
blocked, so that the
steam is obliged to
pass through the con-
voluted tubes, K K,
KK, braced together
by cross pieces,
HHH, which also
serve as stirring
vanes. By means
of the bevel wheels,
L L, worked from
the shaft and pulley,
M N, the twirl is set
in motion, so that
the contents of the
pan are thoroughly
agitated whilst being
heated up. The con-
densed water blows
off at E with the
surplus steam, whilst
C is the discharge
cock of the pan.
The same appliance
can also be used with
wet steam, the con-
voluted tubes being
pierced with holes
so as to allow part of the steam to escape directly into the mass
of material.
Soap Coppers. — Formerly the vessels in which soap and leys
were boiled together were made of various kinds of materials ;
sometimes of masonry, iron bottoms being provided for heating
by free fire ; sometimes of cast iron, like the pan represented in
Fig. 109, or of wrought iron plates ri vetted together subse-
quently, or of wooden staves strongly bound together like
enormous tubs, wet steam being the source of heat.
These forms, however, were mostly adapted only for use with
quantities of material small in comparison with those in use at
the present day, when charges of 30 to 40 tons and upwards of
fatty matters are not uncommon ; a more recent form of soap
kettle is a cylindrical or conical cauldron with somewhat rounded
apex, placed base upwards, constructed of boiler plates well
rivetted together, as indicated in Fig. 112; the degree of slope
of the sides (regulating the ratio between the top and bottom
430
OILS, FATS, WAXES, ETC.
diameters) and the relation between the depth and maximum
diameters vary somewhat in different countries — e.g., soap kettles
Fist. 113.
SOAP COPPERS.
431
of this pattern in America are generally from two to three times
as deep as they are wide, sometimes filling a building of two or
three stories; whilst in Britain the depth rarely exceeds once
and half times the diameter, still shallower pans being often used.
A copper 15 feet diameter and 15 feet deep will turn out 20 to
Fig. 114.
30 tons of soap, a usual rule being to allow 6 cubic feet capacity
(about 37-5 gallons) for each 100 Ibs. weight of fatty matters
treated, or about 135 cubic feet (nearly 850 gallons) per ton; so that
a copper holding some 2,500 cubic feet (upwards of 15,000 gallons)
will suffice for about 18 tons of fatty matters yielding 25 to 30
432
OILS, PATS, WAXES, ETC.
tons of soap according to the amount of water contained therein.
Fig. 113 represents " Morfit's Steam Series," a set of three coppers
supplied with both sets of steam coils (wet and dry). B B is the
steam main supplied from the boiler, A ; K is the wet steam
pipe ; and D F G the dry steam coil. The lowest part of the
Fig. 115.
copper is usually provided with a narrower basin or hat-shaped
downward prolongation for the more easy collection and separa-
tion of watery leys, &c. ; in the figure it is represented as con-
nected with a draw off tube, H, provided with a cock, J. F F F
represent " Curbs " (infra) of different shapes to prevent boiling
over.
CURB AND FAN. 433
Figs. 114 and 115 represent a modern form of pan for heat-
ing with either dry or wet steam as required, constructed by
Messrs. W. Neill & Son, of St. Helens, Lancashire. This is a
square tank made of steel plates rivetted together, with rounded
corners and dished bottom, the square form being preferably
employed as taking up less room than the circular shape requisite
in the case of free-fired coppers provided with flues running
round the lower part of the pan (Fig. 108). The pan is fitted
with wet and dry steam coils, and a cock at the bottom for run-
ning off spent leys. A "skimmer pipe" is provided, working
on a swivel joint, and capable of being adjusted at any required
height by a supporting chain ; as represented in the figure, the
fluid soap is run off by gravity through a down pipe; but if
required a pump can be connected at the elbow instead, a cock
being affixed to shut off connection when the pump is not at
work.
An airblast has been employed by Dunn for the purpose of
intermixing the ley and fatty matters during the preliminary
stage of " killing the goods," and the subsequent operations when
free-fired pans are employed, whereby tumultuous boiling is
largely avoided ; the air was introduced by a " blowpipe "
arranged in much the same way as the more modern wet
t steam coil. The process was said to answer well ; but has
nowadays fallen into disuse through the substitution of steam-
heate'oHpans for free-fired kettles.
Cui*9 and Fan. — With certain kinds of materials, and parti-
1/cularly at certain stages of the operation, tumultuous boiling up
or "bumping," and vigorous frothing are apt to occur, more
especially when oleine soap is made by the direct addition of hot
carbonated leys to free oleic acid (red oils, vide Chap, xx.), and
during the -"'graining " or "cutting" of boiled soaps — i.e., the
throwing them out of watery solutions by addition of salt (vide
Chap, xx.) Two appliances are of considerable utility in diminish-
ing the chance of loss by boiling over under such conditions. One,
known as the " curb," is simply a temporary expansion of the
upper part of the pan, consisting of a conical, circular, or barrel-
shaped addition bolted on so as virtually to amplify considerably
the dimensions of the copper at the top. Fig. 113 represents
a cone, F, of wooden staves, hooped together with iron, applied
to one kettle, and a barrel -shaped analogous curb applied to
another.
The other arrangement is termed a "fan," Fig. 116, and
consists of a sort of pair of paddle-wheels suspended in the pan
at such a depth below the surface as may be requisite, so that as
the paddles revolve the froth is broken by them and prevented
from rising up and boiling over. Motion is communicated to the
paddles by means of a vertical shaft with bevel wheels at top
and bottom, the shaft being telescopic so as to admit of being
28
434
OILS, FATS, WAXES, ETC.
drawn up and down to adjust the level of the paddles as re-
quired j it rotates within a tube carrying a Y-shaped frame at
each end, the whole
being suspended from
the upper horizontal
shaft, by means of
wrhich motion is com-
municated to the ver-
tical shaft through the
bevel wheels, whilst
the lower Y serves as
bearings for the axle of
the paddles.
Soap Fra-mes. —
When the operation of
soapmaking is finished,
and the spent leys
(when such are present)
removed by subsidence,
etc., the resulting soap
usually forms a hot
semifluid or pasty mass
which, on cooling, more
or less thoroughly
solidifies to a soft solid
substance. In order
to facilitate the opera-
tion of cutting up the
mass into bars and
tablets for sale without
waste, the hot soap is
run by gravitation, or
ladled, or pumped out
of the copper in which
it is made into "frames," in which it is allowed to solidify. The
pumps used for this purpose are generally of somewhat different
construction from the ordinary suction pump used for wells, &c.
Fig. 117 represents a rotary soap pump as constructed by Hersee
Brothers of Boston. Instead of pumping out the soap, it may
more conveniently be run off by gravity by means of the adjust-
able "skimmer pipe" shown in Fig. 114, the frames being
arranged so that their tops are at a level below the elbow joint
of the pipe.
A method sometimes used for emptying kettles and raising
their contents to a higher elevation was introduced by Gossage,
consisting of the application of a cover fitting airtight, and then
forcing in compressed air, so as to press the semifluid soap up a
pipe the lower end of which dips into the kettle to the required
Fig. 116.
SOAP FRAMES.
435
depth; the whole arrangement working on the principle of the
" acid egg " used in vitriol factories for elevating the acid without
employing ordinary pumps.
Fig. 119.
The size of the frames employed and the material of which
they are composed vary, wood being preferable when slow cooling
436
OILS, FAT?, WAXES, ETC.
I
Fig. 120.
SLABBING AND BARBING.
437
is essential, but iron being considerably more convenient in other
cases. For toilet soaps, frames holding 1 cwt. or less are often
Fig. 121.
employed ; for scouring soaps much larger ones, furnishing ulti-
mately a block of cooled soap weighing 8, 10, 15, or more cwts.*
Fig. 118 indicates the way in which a wooden frame may be
built up of a set of squares pegged together
and superposed on a bottom board. Fig. 119
represents a frame constructed of galvanised
iron plates where the ends fit into grooves
formed by turning round the corners of the
side plates, or fitting pieces of angle iron
thereto; the side and end plates are similarly
fitted to the iron bottom, and the whole kept
together by two transverse rods at the top
fitted with screws and nuts. Fig. 120 repre-
sents an improved form of steel soap frame,
mounted on four wheels, and held together
by cap fastenings.
When the block of soap has .completely
cooled down and set solid, the frame is taken
to pieces and the block cut into slabs, which
are then transversely cut up into bars.
When this is done by hand the block is cut
in a very simple fashion by simply pulling a
looped wire (Figs. 121 and 122) through it
horizontally so as to cut through the mass
along a series of parallel lines previously
Fig. 122.
marked 011 the outside by means of a scribe (Fig. 123). Slabbing
and barring machines of various patterns are frequently employed
for this purpose (Fig. 124). When it is requisite that the soap
* Formerly, the size of the soap frames was fixed by excise laws and regula
tions, and required to be 45 inches long by 15 wide, inside measurement,
and not less than 45 inches deep (usually made 50 to 60 inches deep) ; so as to
hold some 15 to 20 cubic feet, or about 9 to 11 cwts. of soap, Although no
longer compulsory, this size is still largely employed.
438 OILS, FATS, WAXES, ETC.
should cool very slowly in the frame (e.g., in. order to promote
saponification in making cold process soap — p. 457 ; or to
facilitate mottling — Chap, xx.) the sides of the frame
are sometimes padded to keep in the heat (Fig. 125).
The bars of soap into which a block is cut gener-
ally weigh about 3 Ibs. ; they are usually stacked in
a hollow pile to dry the outside slightly so as to case-
harden them, as it were, or else are stored on lattice
work shelves in an open rack allowing free access of
Fig ^123. a^r- With very moist soaps, this drying action is apt
to go too far, warping the bar out of shape, besides
causing it to lose weight largely ; accordingly such bars are
often "pickled" by immersion in brine, which slightly indurates
the outside. Of late years a considerable demand has sprung
up for 1 Ib. blocks instead of 3 Ib. bars ; such blocks are gener-
ally cut to size and shape and then stamped like toilet cakes in
similar machines but of larger size (p. 444). Often the block is
grooved in the centre, so that it can be readily broken into two ;
or three grooves are stamped at equidistant intervals enabling
four 4 oz. blocks to be obtained.
Crutching Machines. — Formerly, when it was requisite to
stir up soap containing excess of wrater in the cooling frames to
prevent its separating into two liquids, a peculiar hand worked
agitator termed a " crutch " was largely used, consisting of a
square piece of board with a handle attached to the centre of
the square perpendicular to its plane (Fig. 126) ; by plunging this
into the pasty mass, and working it up and down, a sufficiently
efficient mixing was brought about. Such implements are still
in use, especially for small-scale operations, but have been largely
superseded by mixing machines, the operation of agitation by
their means being still spoken of as " crutching." For inter-
mixing silicate or resinate of soda solution with boiled soaps in
large quantities at a time, or for otherwise working in saline
solutions to dilute and harden the soap or improve its detergent
qualities, or " filling " of various kinds, as well as for preventing
separation of watery fluid from the mass, such machines are
largely employed. Various forms are employed — Fig 127 repre-
sents a horizontal cylindrical form, with a rotating internal axle
provided with projecting vanes for stirring up the contents ; when
required for rapid cooling or heating an outer jacket is applied
into which water or steam can be admitted as required
(Fig. 128).
Figs. 129 and 130 represent a series of three crutching pans
arranged so as to be worked from the same shaft. By means
of the clutches indicated, any one of the three can be set in
motion or stopped as required : the stirring vanes are here
horizontal, projecting from a vertical axle, similar fixed vanes
being arranged internally so as to prevent the liquid mass from
CRUTCHING MACHINES.
439
simply swinging round and round without being broken up and
intermixed.
In another form of mixing machine two sets of vanes are
provided, moved in opposite directions by means of bevel
wheels, one axle being hollow and the other working inside it
like the axles carrying the two hands of a watch. The vanes
slope at an angle of 45°, so that the material is continually
440
OILS, FATS, WAXES, ETC.
lifted and the different layers intermixed, the general action
resembling that of an ordinary eggwhisk. Large steam driven
Fig. 127.
sizes are very effective ; but if worked too rapidly the mass is
apt to become frothy. For very stiff soap, an archimedean
screw, working inside a wider cylinder, answers very well.
TOILET SOAP MACHINERY.
441
Toilet Soap Machinery. — In the manufacture of various
kinds of toilet soaps, several special kinds of appliances are used
varying in their nature with the process adopted. When
" stock " soaps prepared on the large scale are " remelted,"
for the purpose of blending together different kinds, with the
addition of colouring or scenting materials, «fcc., a steam jacketted
pan is generally preferred, somewhat after the fashion of Fig. 110 ;
as the soap (previously cut up into small lumps) melts, it is
mixed together either by hand crutching (supra) or by means
Fig. 128.
of some form of agitator; too rapid a movement must not
be communicated to this, otherwise air bubbles are stirred
in and the soap becomes more or less frothy, forming a spongy
mass when solid.* Figs. 131 and 132 represent a very effec-
tive form of remelter constructed by W. Neill & Son, where
the heating action of the outer steam jacket is greatly amplified
by means of the internal cross steam pipes ; the pieces of
soap are continually brought in contact with these by the
motion of the agitating arms, and as a large heating surface
is thus brought into play the remelting proceeds rapidly.
When finished, after intermixture of the various ingredients
"Floating" soaps are purposely prepared in this way, enough air
bubbles bein^ worked in to enable the tablet to float in water, even after
compression in the stamping press.
442
OILS, FATS, WAXES, ETC.
REMELTINC PANS.
443
Fig. 132.
444
OILS, FATS, WAXES, ETC.
intended to render the soap emollient, to scent it, or otherwise
to improve its qualities, the fluid mass is cast in small frames so
as to form blocks of J cwt. or upwards, according to circum-
stances ; usually these are made of iron plates bolted together, as
indicated in Fig. 119, so as to cool quickly and avoid as far as
possible loss of volatile scenting materials, and the injurious
effect of heat thereon. The blocks when cold are then slabbed
and barred by hand or machine, and the bars cut into short
lengths, each of which is then stamped into tablet form by some
form of press acting on the principle of a coining press, where
Fig. 133.
both sides of the coin or medal are embossed at once, a ring or
collar being adjusted round the medal so as to prevent its swell-
ing out sideways under the pressure. A large variety of tablet
stamping machines are in use ; some are worked by hand, the
upper die and collar being attached to a rod or plunger worked
by a lever provided with a balance weight, so that by forcibly
pulling down the lever the die descends and stamps the tablet.
Fig. 133 represents a machine of this description, and Figs. 134
and 135 a steam stamping machine, where the impact of the die
is given by letting steam into the cylinder by means of the valve
STAMPING MACHINES.
445
handle, so that the piston suddenly rises, and consequently
depresses the plunger to which the die is attached on the
opposite side of the axis of motion. In another form of machine
Fig. 134.
Fig. 135.
the requisite impact is given by raising the upper die to which
a considerable weight is attached, and then letting it fall, pile-
driver fashion.
In the case of transparent toilet soaps made by the spirit
process (Chap. xx.\ the pan in which the solution of the soap in
446 OILS, FATS, WAXES, ETC.
spirit is effected is connected with a still head and worm, so that
the alcoholic vapours evolved are condensed and regained. With
soaps of this class, the liquid soap left when most of the spirit is
distilled off is run into frames, so as to gelatinise and solidify,
and is then cut up into tablet blanks, which are exposed to the
air for a considerable length of time (several weeks or even
months) in a warm room, so as to consolidate them by gradual
evaporation of remaining alcohol, etc., otherwise they would be
too soft to keep their shape properly. Moreover, when freshly
Fig. 136.
•prepared the mass is often "muddy;" but on keeping, it gradually
becomes transparent and clear.
Milled Soaps. — Much more elaborate machinery is requisite
for the manufacture of " milled " soaps. The bars of stock soap
are first " stripped " — i.e., cut into slices or chips by a slicing
machine, actuated like a rotary plane or vegetable cutter.
Fig. 136 represents Rutschmann's stripping machine. The chips
are dried in a warm air chamber until only a few per cents,
of moisture are retained, and are then ground between successive
MILLED SOAPS.
447
pairs of heavy horizontal rollers, so arranged that the soap first
passes between No. 1 and No. 2 rollers, then between No. 2 and
No. 3, and so on, somewhat as in the case of seed crushing for
oil extraction (p. 218). Each roller is made to revolve somewhat
faster than the previous one, so that the soap slices are not
merely crushed in passing through, but are also rubbed ; the
soap always adheres to the more quickly moving roller, so that it
passes onwards automatically. By means of " doctors " or
scrapers, it is detached from the last roller in strips or ribbons,
which are returned to the front of the machine and passed
Fig. 137.
through again and again. Fig. 137 represents a form of mill for
the purpose.
In order to facilitate the preliminary drying of the stock soapr
A. & E. des Cressonnieres* use a series of rollers arranged
vertically one above another in an enclosed space heated by
steam or hot air, &c. Soap in a just fluid state from the remelter,
&c., passes in a flat stream from a hopper on to the top roller, the
contact with which partly solidifies it; the resulting semisolid
sheet passes alternately from right to left, and vice versd, between
each successive pair of rollers, as in the mill itself, finally
emerging at the bottom in the form of a solid sheet, which is
separated by an automatic cutter into strips. The temperature
* English patent, No. 2,446, 1890.
448
OILS, FATS, WAXES, ETC.
of the chamber and the rate of soap supply are so adjusted that
the strips are sufficiently dried by the time they emerge.
When the various stock soaps used, colouring matters,
perfumes, unguents (lanolin, vaseline, spermaceti, tfec., as re-
quired in special cases), or medicinal agents, are thoroughly
incorporated together in the mill, the whole mass (if not over-
dried) becomes compara-
tively soft and plastic,
much as partially dried
putty is softened by roll-
ing and working it in the
hand. When thoroughly
intermixed, the ribbons
stripped off the last roller
are strongly compressed
together ; in one class of
machine by filling them
into a barrel or cylinder
provided with a conical
end terminating in a
nozzle, and forcing the
mass outwards by means
of a piston worked by a
screw or by hydraulic
power : the plastic rib-
bons are thus " squirted "
outwards through the
nozzle as a continuous bar, which is then cut into short lengths and
stamped into tablets. In another class of "plotting machine,"*
the ribbons are made to fall from a hopper into the grooves of a
large conical archimedean screw working in a funnel shaped
barrel, terminating in a nozzle of appropriate size ; as the screw
revolves the soap is gradually propelled onwards towards the
nozzle, and on account of the diminishing diameter of the worm,
becomes strongly compressed together, so as finally to issue from
the nozzle as a firm solid bar, which is then cut up and
stamped as before. Fig. 138 represents Beyer's plotting machine
working on this principle.
Cylindrical and spherical soap tablets and wash balls are some-
times prepared; these are usually stamped into approximately the
required shape by means of suitable presses, or by hand, and when
sufficiently dry, finished by turning and polishing in a kind of lathe.
In order to give a polished surface to soap tablets, a method
frequently employed is to expose them to wet steam for a few
seconds, which glazes the exterior. More expensive varieties
are sometimes polished by hand, using a cloth dipped in
alcohol, &c.
* From the French term, " pelotage," applied to this squirting process.
SOAPMAKING PROCESSES. 449
CHAPTER XX.
MANUFACTURE OF SOAP.
As compared with metallurgical and textile industries the art of
soapmaking is not possessed of any claims to great antiquity ;
the ancients were acquainted with the detergent power of wood
ashes (vegetable alkali) and probably also with that of mineral
soda or natron* but do not appear to have known anything of
the products of the action of these substances on oleaginous
materials, no mention of any such compounds being to be found
in Homer or other early Grecian authors ; whilst the Hebrew
term borith f used by the prophets Jeremiah and Malachi,
although translated " soap," appears to have simply meant ivood-
ash alkali.
Pliny the elder, however, in the first century A.D. described
a sort of imperfect soft soap made from goat's tallow and the
alkali from beech wood ash ; and also a harder variety (possibly
got by the action of salt on the former, producing soda soap) ;
and another writer in the second century in a work entitled
De Simplicitus Medicaminibus refers to a softer " German "
variety of soap (probably chiefly made from the ashes of land
plants) and a harder " Gallic " form (probably derived from sea-
weed ash). Later still, soapmaking appears to have been some-
what more extensively practised, as the remains of a soap factory
have been found at Pompeii.
Soapmaking Processes. — The variations in the different
methods by which soaps are prepared on the manufacturing
scale are somewhat numerous, but all may be conveniently
classified under one or other of the three following heads, so far
as the essential parts of the soap producing processes are concerned.
In many cases, however, various subsequent operations are gone
through before the goods are finally ready for the market, con-
sisting either of mechanical cutting and shaping operations, such
as casting into blocks, cutting these up into slabs, bars, and
tablets, and stamping the latter into shape in appropriate presses ;
or of the addition of other substances to the soap before cooling
* Proverbs xxv. 20.— "As vinegar upon nitre [or soda, marginal note,
Revised Version], so is he that singeth songs to an heavy heart." The
frothy uon-perinanent effervescence due to the action of the acid on natron
is doubtless what is here alluded to ; acetic acid and nitre (potassium
nitrate) having no mutual action whatever.
t Jeremiah ii. 22. — "Wash thee with lye, and take thee much soap."
Malachi iii. 2. — "Like a refiner's fire and like fuller's soap."
29
450 OILS, FATS, WAXES, ETC.
or solidifying, so as to increase its detergent properties ; or to
give it special qualities (e.g., disinfecting action); or to harden it,
so as to enable more water or other weight-giving "filling" to
be added without rendering it too soft for ordinary scouring
purposes, £c.
I. Direct Neutralisation Processes. — Where free fatty
acids and alkalies are brought together and converted into soaps
by directly neutralising one another, with or without evolution
of carbonic acid gas according as carbonated or caustic alkalies
are employed. Obviously no glycerol is produced in the formation
of soaps of this kind.
The free fatty acids thus employed are practically almost con-
fined to the "red oils'" of the candlemaker (p. 386)— i.e., the
liquid fatty acids expressed from the mixed products of saponi-
fication leaving behind the solid acids (commercial " stearine ").
Certain distilled and recovered greases (such as Yorkshire grease
from the suds of wool scouring, &c., Chap. XH.) are of similar
character, and are sometimes intermixed with red oils for the
purpose of soapmaking in this way ; but, as a rule, they are not
suitable alone for the preparation of soap of good quality.
Resinate of soda (rosin dissolved in soda ley) used in the manu-
facture of rosin soaps (infra) is a product of precisely similar
nature, excepting that the rosin acids do not belong to the
ordinary fatty acid families described in Chap. in.
II. Soapmaking Processes where Glycerol is set free
taut not separated from the resulting Soap. — In these pro-
cesses natural glycerides are employed, being acted upon by
alkalies (usually caustic) used in regulated quantity so as to
suffice to saponify the total fatty matters without introducing
any large excess of alkali ; the strength of the ley being made
such that the product becomes more or less solid after cooling
and standing, the glycerol consequently being contained in the
product.
To this class belong more particularly soft soaps made by
boiling together appropriate oils, &c., and potash ; marine soaps
and hydrated soaps prepared in similar fashion, mostly with
soda and largely from cokernut or palmnut oil ; socalled cold
process soaps of various kinds, more especially certain forms of
transparent soaps, perfumer's soaps, and analogous products ; and
certain kinds of soap prepared under pressure.
III. Soapmaking Processes where the Glycerol set free
and the resulting Soap are separated from one another.
— In these processes the essential feature is that glycerides are
more or less completely saponified by boiling up with compara-
tively weak alkaline leys, and the soap formed " salted out ;' by
addition of brine or solid salt so as to separate it as a pasty mass
from the watery fluid in which the glycerol remains dissolved.
The half made soap thus obtained is then finished by one or
DIRECT NEUTRALISATION PROCESSES. 451
other of various processes, leading to the production of some
variety of "curd," "mottled," or "fitted soap;" whilst the
watery liquors are either thrown away or utilised by boiling
down so as to recover more or less of the dissolved salt for use
over again, and ultimately obtain the glycerol in an impure form
(vide Chap, xxn.) As regards the magnitude of the scale on which
they are made, and the total quantity manufactured, boiled soaps
of this class are the most important of all. Additional materials
are frequently added to the soap thus prepared for special pur-
poses — e.g., silicate of soda, borax, and aluminate of soda, to
increase the detergent action of household and laundry scouring
soaps ; sulphate and carbonate of soda, to stiffen and harden the
soap, and prevent it from wasting too rapidly in use ; resinate of
soda, in the manufacture of yellow soaps ; carbolic acid, creosote
oils, and similar substances, in the manufacture of disinfecting
soaps ; and so on. When potassium carbonate is thus added to
molten soda soap in not too large a quantity double decomposi-
tion takes place between the sodium salts of the fatty acids and
the potassium carbonate ; thus in the case of stearate —
Sodium Potassium Potassium Sodium
Stearate. Carbonate. Stearate. Carbonate.
2Na.C18H3502 + K2C03 - 2K.C18H3502 + Na2CO3
The result of this is accordingly the formation of a certain pro-
portion of comparatively soft potash soap instead of the harder
soda soap, which alters the texture of the mass ; this operation
of " pearlashing " is consequently employed in the preparation of
certain kinds of toilet soaps (infra). On the other hand, if fatty
matters be saponified with boiling potash ley, and the resulting
soap salted out with ordinary salt, the opposite kind of change
takes place, soda soap and potassium chloride being formed —
e.g., in the case of palmitate —
Potassium Sodium Potassium Sodium
Pulmitate. Chloride. Chloride. Palinitate.
K.C16H3102 + NaCl - KC1 + Na.C16H3l02
In the earlier days of soapmaokingfwhen woodash was the most
available form of alkali, this reaction was of some technical
importance as enabling a hard soda soap to be obtained in lieu of
a soft greasy product ; but although the effect appears to have
been known and the operation practised to some considerable
extent, it is doubtful if the chemical nature of the change was
understood until recently (vide Chap, xxi.)
DIRECT NEUTRALISATION PROCESSES.
The preparation of soap by the direct combination of free fatty
acids and alkalies is an extremely simple operation, more especi-
ally when the alkali is caustic ; all that is required is a suitable
mixing pan provided with an agitator so that the fluid ingredients
452
OILS, FATS, WAXES, ETC.
can be intimately intermixed. Fig. 139 represents a steam
jacketted pan with steam pipes, ppp, projecting upwards into
the pan, whilst an agitator, <?, worked by bevel wheels, carries
a series of vertical vanes projecting downwards, so that clots are
broken up by the interlacing of the pipes and vanes. Another
form of agitator consists of two sets of rods or vanes made to
revolve in opposite directions by means of bevel wheels. The
red oils, &c., are run into the pan (steam jacketted for large
operations) and heated up ; the alkaline ley is gradually run in
Fig. 139.
with agitation, and finally the hot pasty mass transferred to a
"frame" in which it solidifies to a block of soap.
A slight surplus of alkali is practically imperative in order to
ensure complete conversion of the fatty acid into soap ; this
surplus mostly remains disseminated through the mass as it
solidifies, although a small quantity generally exudes as a watery
fluid ; by carefully regulating the quantities used the excess
may when requisite be diminished considerably below that indi-
cated in the example given below, where 5 parts of free alkali
are reckoned for 40 combined, representing a ratio of 1 to 8
RESINATE OF SODA. 453
or 12-5 to 100. On the other hand, for soaps intended to be
highly detergent a larger excess of alkali is intentionally used.
Carbonated alkali is sometimes used, instead of caustic, in the
preparation of " oleine soap " (Morfit's process) ; of late years,
however, the facilities for obtaining solid caustic soda as a com-
mercial product have increased so largely that the slight saving
in cost effected by the use of the former is generally considered
to be more than outweighed by the increased amount of trouble
involved in the process. When employed, the mixing pan is
fitted with a large movable " curb " (a funnel or barrel shaped
top — Fig. 113) in which the froth rises, due to the liberation of
carbonic acid, and the operation is carried out somewhat more
slowly to avoid frothing over.
With inferior soaps, largely made from recovered greases and
such like materials, silicate of soda is sometimes mixed or
" crutched " into the mass when the combination is complete,
just before running into the frames. For this purpose crutching
machines, such as those represented by Figs. 127 to 130, are con-
veniently used. Resinate of soda is also employed as an ingredient
to increase the detergent action. On the other hand, with soaps
required to contain as little free alkali as possible, not only is
great care taken to reduce the proportion of free alkali present
to the minimum consistent with proper combination of the fatty
acids, but in special cases — e.g., for wool-scouring soaps and
soaps used in the silk industries, further means are adopted to
render the small excess innocuous. One method, found in
practice to be very effective (patented by the author), consists
of the addition of a regulated quantity of an ammoniacal salt
(usually dissolved in a minimum of water) to the pasty mass,
and well incorporating by a crutching machine or otherwise
before running into the frame. Any free alkali is thus neutralised
by the acid contained in the ammoniacal salt, with the formation
of an equivalent amount of free ammonia. This latter mostly
escapes when the soap is cut into bars and stored, but the little
that remains is beneficial rather than injurious to wool and silk,
unlike the original free fixed alkali.
Resinate of soda is often prepared for intermixture with soaps
of various kinds by boiling up rosin with rather less than twice
its weight of soda ley of about 16° T. (specific gravity 1'08), con-
taining about 7 per cent, of NaOH * until completely dissolved.
The liquid sets to a sort of thin jelly when cold, containing the
soda salts of the rosin acids and more or less excess of alkali,
according to the quantity used. Any kind of pan will answer if
furnished with a wet steam coil, or with an agitator and some
other suitable means of heating. Morfit's steam twirl (Fig. Ill,
p. 429) answers well.
* The saponiti cation equivalent of rosin usually lies between 330 and 370,
so that 10U parts of rosin correspond with between 10'8 and 12*1 parts of
NaOH.
454 OILS, FATS, WAXES, ETC.
Calculation of Quantity and Strength of Ley required,
and of Composition of resulting Soap. — The quantity of ley
of a given strength employed depends partly on the mean equi-
valent of the oleine, £c., used, and partly on the amount of excess
of alkali intended to be added to ensure complete neutralisation
and communicate extra detergent properties to the soap ; whilst
the exact strength employed depends on the proportion of water
the finished soap is intended to contain. Assuming the oleine
to be pure oleic acid, its saponificatioii equivalent would be
282 — i.e., 282 parts of oleine would neutralise 40 of NaOH in
accordance with the reaction.
Gleic Acid. Caustic Soda. Sodium Oleite. Water.
C]SH34Oo + NaOH NaC18H33O2 + H20
Supposing the ley to be a pure solution of sodium hydroxide, if
such a quantity were used as would contain 45 parts of NaOH,
5 would consequently remain unneutralised, or the " free alkali ''
would bear to the " combined alkali " the ratio 5 to 40 = 1 to 8
= 12*5 per cent.; if, then, 140 parts of ley were used, containing
45 of NaOH (32-1 per cent), neglecting mechanical losses and
evaporation, the resulting mass would consist of 282 + 140 = 422
parts, made up thus —
Sodium oleate, . . 304 parts 72 '04 per cent.
Excess of caustic soda, . 5 ,, = 1'18 ,,
Water, . . . . 113 ,, = 26'78 „
422 100-00
The 113 parts of water are made up of 140 — 45 = 95 parts con-
tained in the ley used, arid 18 parts formed by the above
reaction.
If a proportionately larger amount of weaker ley were used
containing 45 parts of NaOH in 160 (28-1 per cent, of NaOH)
the resulting mass would consist of 282 + 160 = 442 parts,
made up thus —
Sodium oleate, . . . 304 parts = 68 '78 per cent.
Excess of caustic soda, . . 5 ,, 1'13 ,,
Water, 133 „ = 30'09
442 100-00
On the other hand, if a proportionately less amount of stronger
ley were used containing 45 parts of NaOH in 120 (37 '5 per
cent, of NaOH) the composition of the resulting 282 + 120
= 402 parts would be —
Sodium oleate, . . . 304 parts = 75 "62 per cent.
Excess of alkali, . . . 5 „ = 1'24
Water, 93 „= 23'14 „
402 100-00
CALCULATIONS. 455
In similar fashion the strength and quantity of ley requisite for
any other given mixtures of free fatty acids can be calculated ;
thus suppose the mean equivalent of the fatty acids to be E, and
that the surplus free alkali is to be n per cent, of that combined
as soap ; then for E parts of fatty acid a quantity of ley must be
used containing 40 x — ^— = CH x (100 + n) parts of NaOH
altogether. With a ley containing saline matters (chloride,
sulphate, &c.) representing m parts per 100 of NaOH, the
quantity of saline matter will be -^-= x 0*4 x (100 + n) =
0-004 x m x (100 + n); so that a weight, W, of ley will contain —
NaOH, 0'4 x (100 + n)
Saline matters, .... m x 0'004 x (100 + n)
Water, . . . . W - O'OOl x (100 + m) (100 + n)
Hence the total water present will be —
18 + W - 0-004 x (100 + m) (100 + »),
and the resulting soap will consist of —
Sodium oleate, E + 40 - 18 . . . . * ; ; = E + 22
Excess of NaOH, — - x 40 =0'4xn.
Saline matters, -™_ x 0'4 x (100 + n) . = 0'004 x m x (100 + n)
LOO
Water, W + 18 - 0-004 (100 + m) (100 + n)
Total, E + W.
Suppose that w parts of resinate of soda solution be added to
the soap, consisting of —
Resinate of soda, . . ..- . . a parts.
Excess of NaOH, b ,,
Water, w - (a + b) „
then the total mass, neglecting mechanical loss and evaporation,
will consist of —
Soap (sodium oleate + resinate), . . . E + a + 22
Excess of NaOH, 0'4 x n + b
Saline matters, .... 0'004 x m x (100 + »)
Water, W + w + 18 - {0'004 (100 + m) (100 + n) + a + b}
Total, E + W + w.
If, on the other hand, w parts of silicate of soda be added,
containing —
Silicate of soda and other saline matters, . . c parts.
Excess of NaOH, d ,,
Water, w' - (c + d) ,,
456 OILS, FATS, WAXES, ETC.
then the total mass will contain —
Sodium oleate, . . . . . . . . . E + 22
Excess of NaOH, 0'4 x n -f d
Sodium silicate and other saline matters, . 0'004 x m (100 + n) + c
Water, . W + w' + 18 - {0'OP4 (100 - m) (100 - n) + c + d]
Total, . E + W + «;'.
These various quantities are readily calculated into per-
centages when the values of E, m, n, a, b, c, c/, W, w, w' are
given for any particular case — e.g., suppose E = 280, n = 10,
m = 12, and W = 150 in the case of a soap not treated with
resinate or silicate, &c., then the composition is —
Sodium oleate, . . . 2SO + 22 = 302 "0 = 70 '23 per cent.
Excess of NaUH, . . . 0'4 x 10 = 4/0 = 0'93
Saline matters, . , 0'004 x 12 x 110 = 5'2S = 1-23 ,,
Water, . 150+ 18 - 0'004 x 112 x 110 = 11872 = 27 61
Total, 280 + 150 = 430 00 = 100 '00
and similarly in other cases.
SOAPMAKING PROCESSES WHERE THE GLYCEROL
IS SET FREE BUT NOT SEPARATED.
The methods of this character may be divided into three
classes according to the temperature and pressure employed. In
socalled "cold process" soaps the materials to be saponified and
the alkaline ley are intimately intermixed in open vessels at
temperatures usually considerably below the boiling point, and
allowed to stand until the action is complete, the leys used
being of sufficient strength to yield a product not too moist.
" Hydrated " soaps (including " marine " soap) and " soft " soaps
are prepared by boiling together the materials under the ordinary
pressure ; whilst soaps prepared under increased pressure are
treated in closed vessels so as to obtain a still higher temperature
for the purpose of shortening the operations and rendering them
more complete. In all cases the amount of alkali employed must
be carefully proportioned to the quantity of fatty matters used
and their mean saponification equivalent, otherwise either an
imperfect soap will result containing more or less unaltered
grease owing to the use of a deficiency of alkali, or a strongly
alkaline one through the use of too great an excess. Sometimes
these two faults occur simultaneously through the action not
having been completely carried through ; this is not unfrequently
the case with soaps made on the small scale with highly scented
materials (perfumer's soap), where avoidance of much rise of
temperature is indispensable, since otherwise the delicacy of the
odour would be deteriorated, so that the product is apt to contain
COLD PROCESS SOAPS.
457
simultaneously unaltered fatty glycerides and uncombined caustic
alkali. Soaps of this kind, however, have now been largely driven
out of the market by " milled " toilet soaps where the evil effect
of heat on delicate perfumes is avoided, and at the same time a
perfectly made soap ensured, by mixing a good kind of stock
soap with the scenting materials, &c., by machinery, grinding
them together in the cold (vide infra, also p. 446).
Cold Process Soaps. — For the preparation of cold process
soaps on the large scale a " Hawes' boiler " is convenient. The
fatty matters (tallow, either alone or mixed with palm oil or
lard, and preferably a small quantity of cokernut oil, the presence
of which facilitates the saponification; or other similar mixtures)
are introduced into a pan such as that indicated in Fig. 140, or into
a horizontal cylinder, Fig. 141 (5 to 6 feet diameter), provided
D
Fig. 140.
Fig. 141.
with a mechanical agitator and heated till sufficiently fluid, usually
to about 45° C. (about 113° F.) Strong soda ley of about specific
gravity 1-33 (66° Twaddell, containing about 24 per cent, of
NaOH) is then run in in sufficient quantity (approximately two
parts of fat to one of ley, the exact- proportion varying with the
mean saponification equivalent of the fatty matters), with con-
tinuous agitation until the whole becomes pasty and thoroughly
intermixed ; the paste is then run out into a wooden frame and
well covered up to keep in the heat ; as warmth is produced by
the saponification change, the mass doe^sjjiofr cool until the action
is completed ; at first the change takes place only languidly, but
after a while it becomes more rapid and the mass sensibly heats ;
by and bye as the action approaches completion the temperature
begins to fall again. If the materials are too highly heated at
first the paste is apt to be too fluid, so that unsaponified grease
and watery ley tend to separate partially during the period of
standing, thus yielding an imperfect product. Instead of soda
alone a mixture of soda and potash (the former largely predomi-
nating) is often employed with the object of obtaining a product
of superior texture.
458 OILS, FATS, WAXES, ETC.
Certain kinds of transparent soaps (often termed "glycerine
soaps") are frequently prepared by means of a modification of
the cold process ; the warm fatty materials employed (of which
castor oil is generally a considerable ingredient on account of
its ready saponifiability and its tendency to form translucent
soaps) are intimately intermixed with soda ley (and in certain
cases a small proportion of alcohol) ; soluble colouring matters
<and essential oils and other scents are then stirred in and
the whole allowed to stand until saponification is complete :
with suitably chosen ingredients and proportions the resulting
block of soap is more or less transparent, the presence of
the glycerol formed on saponification tending to cause the
soap to assume a "colloid" or gum-like structure instead of
the semicrystalliiie opaque condition usually developed in
ordinary hard soaps. When alcohol is not used as an ingre-
dient in the mass, the transparency is usually only imperfect,
but by incorporating extra glycerol instead a highly transparent
mass can be readily obtained. Cane sugar effects the same result,
and is generally employed instead of either alcohol or glycerol
on account of its cheapness ; but the effect on the nature of the
resulting product is by no means the same, inasmuch as saccharine
substances are apt to produce a very unpleasant irritating effect
when applied to highly sensitive skins (ladies', babies', invalids',
and so forth). This, moreover, is apt to be greatly aggravated
by the presence of a more or less considerable excess of alkali in
the soap mass, necessarily added to effect complete saponification,*
inasmuch as muddiness is apt to be produced if any of the fatty
glycerides remain unchanged, which is likely to be the case,
unless some excess of caustic alkali is present. It accordingly
results that many kinds of transparent socalled " glycerine soaps "
are of the worst possible quality from the point of view of liability
to excoriate and irritate extremely tender skins ; although their
appearance, when attractively tinted and agreeably scented, render
them apparently very elegant articles.
The cheaper kinds of transparent soap of this description are
often extensively " filled in " with liquid paraffin and petroleum
hydrocarbons which possess the property of blending with the
sugary soap mass without seriously interfering with either its
consistency or transparency ; taking into account some 20 to
25 per cent, of "loading" thus introduced, together with some
12 to 18 per cent, of sugar, and 20 to 25 per cent, at least of
water, it often results that the actual soap present does not
exceed 33 to 40 per cent, of the mass. On the other hand, a
well made soap where the minimum possible excess of alkali
only has been used, where the rate of saponification and ten-
transparent soaps made by the "spirit process" (infra) are generally
free f roui this defect, although as usually sent into the market they contain
considerable amounts of cane sugar. .
SOFT SOAPS. 459
dency to colloidal structure of the product have been intensified
by the use of an admixture of spirit in the original materials,
together with a little glycerol instead of sugar, and where no
loading has been added, not only contains a far larger proportion
of useful ingredients of much better quality, but also for that very
reason resists the wasting and solvent action of water (especially
when hot) much more completely, and is consequently much more
economical in use, as well as comparatively free from corrosive*
action, on delicate skins.
Soft Soaps. — Potash soaps appear to possess, on the whole, a
greater tendency to assume the colloid form than soda soaps, in
consequence of which, when prepared from suitable fatty matters,
they are more inclined to be jelly-like and transparent or trans-
lucent, than to form comparatively hard opaque semicrystalline
masses like ordinary soda soaps; moreover, they are generally
deliquescent, so that they do not readily dry up. The precise
texture of a given mass, however, largely depends on the tempera-
ture, as in cold weather crystalline grains often form, more especi-
ally when the fatty matters used contain palmitic or stearic acid :
soap exhibiting this peculiarity (known as " figging ") is gener-
ally supposed to be of superior quality for that reason, although
on what grounds it is difficult to say ; the granular appearance
is sometimes imitated by mixing in starch, clay, steatite, &c.
Linseed and other drying oils (poppy seed, hempseed, &c.) ; non-
drying and semidrying vegetable oils (such as rape, camelina,
and cotton seed) and similar animal oils (train, liver, arid fish
oils); together with the "red oils" of the candlemaker (crude
oleic acid), are those most largely employed in the manufacture
of soft soaps, a little tallow being added to furnish stearate for
"figging," and in many cases indigo in small quantity so as to
give a greenish shade (by conjunction with the yellow tinge of
the untinted soap) ; this tint being natural to hemp seed oil, and,
therefore, artificially imitated in other cases. When whale and fish
oils are employed an unpleasant smell is apt to be communicated
to linen, &c., washed with such soap. Considerable practice and
skill is requisite in boiling soft soap, although the actual opera-
tions are of the simplest character ; the " copper " or pan (usually
made of iron plates rivetted together boiler- fashion — Fig. 112)
in which the boiling takes place was formerly mounted over a
free fire, but is now generally heated by means of two steam
coils, one for " dry steam " (i.e., simply a coil through which
superheated steam circulates so as to heat up the contents of
the pan), the other for " wet steam " (i.e., a coil perforated with
holes, so that when steam is let in from the boiler it escapes into
the mass through the holes, heating it up and becoming itself
condensed, until the temperature is so high that the steam simply
blows through). Figs. 1 14, 1 ] 5 illustrate a pan fitted with the two
kinds of steam coils. The mixed fatty matters are run into the
460 OILS, FATS, WAXES, ETC.
copper so as to fill it to about one-fifth or one-fourth of its capacity ;
the whole is then heated up (by free fire when that is used, by
means of the dry steam coil if no free fire is employed), and whilst
heating potash ley (usually of specific gravity 1 -07 to 1 -08) is
slowly run in. This ley is found by experience to act better if
not completely causticised, a portion (some 15 to 25 per cent.) of
the alkali being still carbonated ;* the heat should be so applied,
and the rate of supply oc ley so adjusted, that by the time that a
volumn of liquor about equal to that of the oil has been run in,
the whole mass is beginning to boil ; to prevent frothing over a
"fan" (Fig. 116) is conveniently arranged over the pan. The
boiling is continued with wet or dry steam, usually the former,
with further additions of ley from time to time, until the proper
consistency and appearance are arrived at as judged by taking
out samples and quickly chilling them ; as long as an insufficient
quantity of ley has been used a visible appearance of unsaponified
fat is manifest, giving a peculiar border to the sample ; whilst if
excess has been added the sample more or less tends to separate
into two different portions, one of soap, the other of watery liquor;
in this case more oil (agitated and emulsified with a little weak
liquor to enable it to mix better with the boiling mass) is added,
and so on until the sample sets to a clear translucent mass.
Finally the wet steam is shut off and the mass boiled either by
dry steam or free fire until sufficiently concentrated by evapora-
tion, when the finished soap is barrelled or put up in canisters
or drums for sale.
Some makers prefer to use stronger leys in the first instance
(specific gravity 1-120 to 1-150 = 24° to 30° Tw.), whereby less
boiling down is requisite in the final stage. In some cases a
mixture of potash and soda leys is employed, the former, how-
ever, always constituting more than half of the total alkali (60 to
75 per cent.) Soft soap containing soda is apt to become muddy
in cold weather, and hence is preferably made only in summer.
The exact nature of the mixture of fatty matters employed is
generally regarded as a valuable trade secret ; the relative
proportions of the constituents are often varied somewhat
according to the season ; in winter the consistency of the product
is usually much greater than in summer, so that in the former
case, such a mixture is employed as would (for the same atmo-
spheric temperature) give a softer jelly, and vice versa. For
household soft soaps, silicate of soda (or potash) is sometimes
mixed in with the finished soap, whilst rosin is often added to
the fatty mixture employed as basis ; when the soap is intended
for silk and wool scouring, however, such admixtures are highly
* When the soft soap is required to be as nearly neutral as possible, car-
bonated alkali is undesirable as tending to give a product containing a
larger amount of "free alkali" than that obtainable by the judicious use
of caustic alkali free from carbonate.
MARINE SOAP. 401
injurious, partly because of the presence of silicated alkali in the
soap, which has a very bad effect on the fibre ; partly because
soaps thus treated usually contain a larger proportion of
uncornbined potash or soda, or both, than genuine well made soft
soap. It is generally supposed that because ordinary woolgrease
(suint) naturally contains much potash and but little soda, there-
fore soda has a more injurious action on wool fibre than potash.
Apart from the somewhat illogical character of this reasoning,
however, there does not seem to be any experimental evidence
extant to show that this is really the case ; on the contrary,
experience seems rather to indicate that, provided a soap is
sensibly neutral (i.e., devoid of alkali uncombined with fatty
acids), it is but of little consequence whether it be a potash soap
or a soda soap as regards injury to the fibre of wool during use
in scouring ; on the other hand, a highly alkaline potash soap,
otherwise pure, exerts more deleterious action than a compara-
tively neutral soda soap ; although, without doubt an alkaline
soda soap, especially if silicated, is extremely objectionable.
Probably the prejudice respecting the superiority of potash over
soda soaps for wool scouring is largely due to the inferiority of
the soda (silicated) soaps now manufactured in great quantity for
household scouring purposes, when compared with potash soft
soaps of good quality as regards the amount and nature of the
alkaline constituents present other than true soaps — i.e., com-
pounds with fatty acids ; for a well made soda (oleine) soap devoid
of silicate or other forms of " free alkali," such as the dealkalised
soap described on p. 453, appears to be in practice quite as well
suited for wool scouring purposes as the best potash soft soap
obtainable.
Hydrated Soaps. — The term " hydrated soap " is often
applied to soap manufactured in much the same way as soft soap,
but made with soda as alkali, and with fatty matters of such
nature as to furnish a comparatively hard opaque product rather
than a soft jellylike mass.* Cokernut or palm kernel oil is
generally an ingredient in the mixture of fatty matters used, its
presence facilitating the saponification of other fats less readily
attacked by alkalies ; when this substance constitutes the great
majority or the whole of the mass, the product is known as
marine soap, as the solubility in brine of the soda salts formed
from cokernut oil is sufficient to enable it to form a lather with
seawater.
Marine Soap. — This is readily prepared by boiling up together
with wet steam cokernut or palm kernel oil, and strong soda ley
of specific gravity about 1-15 to M75 (30° to 50° Tw.), the latter
* In Germany, soap of similar character is often designated eschweyer
seife; in America, the term "Swiss soap" is similarly applied. Soaps of
this kind are often intermixed with boiled soaps containing no glycerol, so
as to form products of mixed character.
4G2 OILS, FATS, WAXES, ETC.
being run in slowly. Saponification proceeds very rapidly when
once commenced, the mass frothing up largely, and requiring a
largo pan and curb to avoid loss by boiling over. A boiling
temperature, in fact, is not absolutely necessary, nor even
desirable to begin with, as the heat liberated by the action rapidly
raises the temperature, whence the copious frothing. Owing to
the low saponification equivalent of cokernut oil (about 210 to
215), a much larger quantity of alkali is requisite to bring about
complete saponification than is the case with most other kinds of
fatty matter ; 100 parts of cokernut oil correspond with about
19 of NaOH, whereas 100 parts of tallow represent only about
14 parts of NaOH (vide infra). A considerable quantity of
silicate of soda is generally run into the finished mass and well
" crutched in" (i.e., intermixed by agitation); the effect of this is
greatly to intensify the natural tendency of cokernut oil soap to
form a tolerably solid mass, even when incorporated with a con-
siderable amount of water ; so that silicated marine soap often
contains less than 20 per cent, of actual soap (sodium salts of
fatty acids), and upwards of 70 per cent, of water. Such a soap,
when heated alone, generally separates into two distinct sub-
stances, viz., a watery solution of silicate, etc., and a pasty mass
of actual soap. On account of this tendency to separation, the
crutching of the original mass must be prolonged until solidifica-
tion is tolerably far advanced, in order to ensure a uniform pro-
duct. Asa general rule, the price at which such highly watered
soap is sold is not reduced to anything like the extent that would
correspond with the amount of water added.
Hydrated soaps made from mixtures containing palm oil,
tallow, bone fat, horse grease, &c., are sometimes silicated, but
are more frequently hardened by crutching in a strong solution
of sodium carbonate (sometimes together with sodium sulphate),
whereby not only extra detergent quality is communicated, but
also a greater degree of firmness, enabling a larger proportion of
water to be present without rendering the soap too soft for
sale; the term "hydrated" (or "watered"), indeed, is originally
derived from the circumstance that the method of manufacture
enables a product to be obtained containing a much larger pro-
portion of water, and a correspondingly less quantity of actual
soap, than was formerly practicable with " boiled soaps " of the
third class. Even with these, however, it has been found
possible to produce an analogous result by somewhat similar
devices, more especially by cautiously crutching in saline solutions
(sodium silicate, carbonate, &c.) whilst cooling and solidifying
(vide infra}.
Hydrated Soaps prepared under Pressure. — A large
number of patents have been taken out from time to time for
various processes and modifications of plant, intended to shorten
and simplify the manufacture of hydrated soaps by causing the
HYDRATED SOAPS PREPARED UNDER PRESSURE.
463
reaction to occur at a more elevated temperature under increased
pressure. Thus Tilghmann proposed the use for soapmaking of
the same plant as used by him for hydrolysing glycerides by
water alone (p. 385). The apparatus that has been generally
found to answer best is some kind of autoclave where the
mutually adjusted quantities of fatty matter and lye are either
run in through a manhole or pumped in through a pipe, and
then heated up either by means of a free fire or by blowing in
high-pressure steam, much as in the manufacture of " steariiie }>
for candlemaking (p.
373). Fig. 142 illus-
trates Dunn's plant,
consisting of a ver-
tical boiler, B, with
manhole and safety
valve ; the fat and
ley are pumped in
through the safety
pipe, A, and the
finished mass ejected
through the empty-
ing tube and cock, C.
Heat is communi-
cated by means of
free firing, the tem-
perature attained be-
ing determined by
means of a long-
stemmed thermo-
Fig. 142.
meter, inserted in a tube filled with mercury or paraffin wax,.
projecting inwards into the boiler.*
In Bennett and Gibb's process a. horizontal boiler furnished
with an agitator is employed, somewhat similar to that used by
Hawe's (p. 457) ; into this are continuously pumped at one end
the fatty matters to be saponified and soda leys not causticised
(sodium carbonate solution), containing the appropriate quantity
of alkali (30 to 33 parts of soda ash at 48 per cent. Na2O
dissolved in 100 of water to 100 of fatty matter). At the other
end the finished soap mass emerges through a weighted exit
valve, the pressure 'being maintained at 220 to 280 Ibs. per
square inch (about 15 to 20 atmospheres, corresponding with a
* This boiler also serves for the preparation of silicate of soda (or potash)
solution. The boiler is charged with broken up flints or quartz pebbles and
soda ley of specific gravity 1*15 to 1*175 (30° to 35° Tw.), and is gradually
heated up until a pressure of 4 to 5 atmospheres is attained (corresponding-
with a temperature of about 150° C.), which is maintained for some hours.
At the end of this time the soda has dissolved silica to approximate satura-
tion ; the liquor is then blown off into a settling tank, and the clear portion
used for intermixture with soap.
464 OILS, FATS, WAXES, ETC.
temperature of 190° to 215° C.) At this higher temperature the
carbonated alkali is stated by the inventor to act as efficiently as
caustic alkali at lower pressures.
Calculation of Quantity and Strength of Ley required
and of Composition of resulting Soap. — Much the same
general principles apply in the case of the soaps at present
under discussion as in the case of those prepared by direct
neutralisation of fatty acids (p. 454), the chief difference being
that in the present instance no water is formed, whilst the
glycerol produced instead must be taken into account. If E
be the sapoiiification equivalent of a mixture of triglycerides,
E parts by weight of the mixture will require 40 parts of NaOH,
or 57 '1 parts of KOII, for sapoiiification, and will produce by
92
acting thereon ' ' parts of glycerol, in accordance with the
o
equation.
Trk'lyceride. Caustic Soda. G'ycerol. Soda Soup.
CH2 . OX CH2 . OH
i I
CH .OX + SNa.OH = CH . OH + 3Na . OX
CH2 . OX CH2 . OH
Suppose that a soda ley is used, containing m parts of neutral
saline matters (chloride, sulphate, £c.) per 100 of NaOH ;
and that the proportion of ley employed is such that for 100
parts of NaOH converted into soap n parts are employed in
excess. The total NaOH employed will, consequently, be
40 x 1" n = 0-4 (100 + n) parts for E parts of fatty matter
as before; whilst a given weight of ley, W, will contain, as
before —
NaOH, 0-4 x (100 + »»)
Saline matters, . . . -™^ x 0'4 x (100 + n) = m x 0'004 x (100 + w)
Water, W - 0'4 (100 + n) - 0'004 x m (100 + n) = W - 0'004 (100 -H m) (100 + n)
Total, W
Hence the resulting soap mass (neglecting mechanical losses
and|evaporation) will contain —
Soda soap, E + 40 - -* - . . . . E + 9'33
Glycerol, ~ ..... - 30'67
o
Excess of NaOH, T"7r x 40 . . . . = 0'4 x n
100
Saline matters, 0'004 x m (100 + n)
Water, W - 0'004 (100 + m) (100 + n)
Total, E + W
CALCULATIONS. 465
In the case of a potash soap, if m parts of neutral saline
matters be present per 100 of KOH, and if n parts of KOH in
excess be used per 100 converted into soap, the total KOH used
will be 57-1 x — 1Q* n = 0-571 x (100 + n) per E parts of tri-
glyceride mixture; whilst a given weight of ley, W, will contain —
KOH, 0-571 x (100 + n)
Saline matters, -^ x 0'571 x (100 + n) = 0'0057l x m x (ICO + n)
Water, j ^ ' 0-57,1(100^) - 0«B71 1 = w _ ^ (10D + m) (100 + n)
Total, W
Whence the entire soap mass produced will consist of —
no
Potash soap, E + 57'1 - .... E x 26'43
o
99
Glycerol, -^- = 30 "67
Excess of KOH, ^ x 57 '1 .... = 000571 x n
Saline matters, 0 '00571 x m x (100 + n)
Water, W-0'00571 (100 + m) (100 + n)
Total, E + W
Suppose that an admixture of silicate of soda, resinate of soda,
syrup, or loading of any kind be made to the extent of w parts
by weight, the composition of the total mass will be similarly
arrived at ; thus suppose a mixture of fatty matters of mean
saponification equivalent 290 (E = 290) be saponified with excess
of soda ley such that W = 160, n = 15, and m = 10, and that 150
parts of syrup be added per 290 of fatty matters, consisting of —
Sugar, . . 50 parts.
Water, . .100 ,,
150
i.e., let w = 150 ; then the composition of the resulting mass will
be —
Soap, . . . .290 + 9-33 = 299 '33 = 49 -89 percent.
Glycerol, ... - 30'67 - 5'11 „
Excess of NaOH, . 0'4 x 15 = 6'00 = I'OO „
Saline matters, . 0'004 x 10 x 115 = 4'60 = 0'77
Sugar, 50-00 = 8 '33
Water, . 160 + 100 - 0'004 x 110 x 115 = 209'40 = 34-90 „
Total, 290 + 160 + 150 = (300 '00 = 100 '00
30
466 OILS, FATS, WAXES, ETC.
In the preparation of soft soap, the quantity of ley and fatty
matter used are usually not adjusted to one another beforehand
in the way requisite for cold process soaps \ the ley is run in
gradually during the operation until the requisite consistency is
attained, more fatty matter being added in case of an excess of
alkali having been used, practical experience in carrying out the
manipulations being the guide to the quantities employed rather
than accurate weighing or measuring. Similar remarks apply to
most hydrated soaps prepared by boiling in open pans ; on the
other hand, for soaps made under pressure in autoclaves, tfec.,
the relative quantities of materials must be carefully adjusted at
the commencement of the operation, as the nature of the process
does not conveniently admit of more material being added after
the operation has been once commenced and the increased pressure
attained.
SOAPMAKING PROCESSES WHERE THE GLYCEROL
AND SOAP FORMED ARE SEPARATED
FROM ONE ANOTHER.
Methods of this class substantially depend upon the general
principle that whereas most alkali soaps are pretty freely soluble
in pure water, especially when hot, the presence of various kinds
of neutral saline matter — e.y., common salt — and even of a large
excess of caustic or carbonated alkali, renders them insoluble ;
so that the addition of salt or strong ley to an aqueous soap
solution causes the soap to separate or precipitate in more or less
solid flakes, the physical structure of which is more akin to that
of crystalloid substances than to the colloid gum-like form in
which transparent soap is obtained. The process of manufacture
may accordingly be broadly described as consisting o^f boiling up
the fatty matter to be saponified with comparatively weak alkaline
fluids not used in excess, but employed in such quantity that
when the alkali has been practically all neutralised by combina-
tion with the fatty acids the great majority of the fatty matter
is decomposed, the remaining portion being distributed through
the soap solution formed as a sort of emulsion. At this stage,
on adding solid salt or strong brine, the dissolved soap is thrown
out of solution and separates as a more or less granular curd,
carrying with it the unaltered fat ; the watery fluid containing
the liberated glycerol being run off, the pasty imperfect soap is
further treated with successive small quantities of stronger ley,
being boiled up therewith until the saponification is complete.
Finally, the soap is "finished" by one or other of various kinds of
operation, according to the nature of the intended product. For
"mottled" soaps, the curd resulting after complete saponification
is boiled down (by dry steam, or in the older w^ay of working, by
CURD SOAP. 467
free fire), together with excess of strong ley, until it acquires a
sufficient consistency — i.e., until it is so thick that on running
into the frames the coloured impurities present (iron soap, &c.,
formed during the process, or produced by adding green vitriol,
&c., to the curd) are unable to sink to the bottom by gravitation;
in which case, as the mass cools and solidifies, these coloured
matters segregate into veins producing " mottling " of the old
fashioned type.*
For "fitted" soaps, the curd produced after complete saponifi-
cation is effected is allowed to stand awhile so as to separate
from the leys ; these are run off, and the curd boiled up with
wet steam and weak leys or water until it is sufficiently thinned
in texture to permit of the coloured heavier metallic soaps falling
to the bottom by gravitation on standing ; with rosin soaps more
particularly, peculiar textures ("coarse fit," "fine fit") are thus
arrived at, respectively suitable for different purposes.
Curd Soap. — For "cleansed" curd soaps, the diluted curd
thus freed from coloured impurities is pumped off into another
copper, and theie boiled up with dry steam and a small quantity
of strong ley until again concentrated to the required extent
(i.e., until the curd, freed from ley by subsidence, has the desired
proportion of water associated with it) ; the water retained by
the curd being less the longer the boiling is continued, and the
stronger the ley (pp. 470, 4b6).
In boiling for curd soap,f the first saponification operation is
usually carried out by running into the copper caustic leys of
strength not exceeding specific gravity 1'05 to 1'075 (10° to
15°T.),J together with' the melted fatty matters, and boiling
them up together. The way in which this is done varies much
in different cases and in different districts ; sometimes *tKe wfrole
batch of " goods " (fatty matters) is. run in, and then, a fraction
of the ley, and the whole boiled up^more ley bfeing added from
* Totally distinct from the modern" mottled soaps of highly watered and
silicated character — vide p. 472.
t British curd soaps are almost invariably made from tallow as chief
basis, the hard difficultly lathering character of pure tallow soap being
modified by the addition of other oils and fats (small quantities of cokernut
oil, more or less cotton seed or groundnut oil, lard, and so on), according
to the object in view. On the Continent, and especially in France, vegeta-
ble oils are used in much larger proportion ; thus Marseilles (Castile) soap
is supposed to be made almost wholly from olive oil, and, in point of fact,
is chiefly prepared from the highly sophisticated mixtures sold under that
name ; and even in those cases where tallow is used, a pretty large propor-
tion of mixed vegetable oil is generally also added, rape oil being generally
one of the constituents added to give lathering qualities.
% Leys containing more than some 5 per cent, of JSa20 act much less
slowly on tallow and most other oils and fats than weaker solutions, at
any rate in the first instance. When, however, the action is once fairly
started, somewhat stronger leys may be run in (in small quantities at a
time).
468 OILS, FATS, WAXES, ETC.
time to time. Sometimes the majority of the ley is run in first,
and the goods added in successive portions, with continuous
boiling. More frequently the ley and goods are run in alter-
nately until the full complement of the latter is in the kettle,
with somewhat less than the corresponding quantity of ley, the
rest of which is subsequently added. When wet steam is used
to heat up the copper the leys initially employed may be a little
stronger than if dry steam be used on account of the dilution
with condensed water ; the later leys may also be stronger than
the first ones, as they become greatly diluted with the water
already present from the former leys. The effect of the action of
the hot ley on the melted fatty matter is to "kill the goods " —
i.e., to emulsify the whole, so that no distinct layer of melted fat
swims up on taking a sample.
When the saponification has gone on to such an extent that a
large fraction of the glycerides is acted upon and but little alkali
remains dissolved in the ley, the whole mass forms a homo-
geneous pasty mass, consisting of the half made soap with
portions of emulsified fatty matter not yet saponified distributed
throughout it.* In this state it is known as "close" soap (in
some districts, as being in a "hitch" or "glue"). If too much
ley has been added this peculiar texture is not attained, a sample
taken out on a trowel exhibiting more or less marked tendency
to separate into two fluids, one more watery than the other ;
whilst, if the boiling has not been continued long enough, or if
the ley be too concentrated, a large surplus of undecomposed fat
is visible, giving a greasy texture to the imperfectly made soap
that thus separates from the watery ley. With proper care,
* It is extremely probable that the saponifying action of the alkali is
exerted in three stages, forming successively one, two, and three molecules
of soda soap ; thus (in the case of stearin) — •
Tristearin. Caustic Soda. Distearin. Sodium Stearate.
(O.C18H3;0 (O.C18H8fiO
C3H5 O.C18H350 + NaOH = C3H5 \ 0. C18H330 + Na. 0. C18H350.
(O.C13H350 (OH
Distearin. Monostearin.
I O.C18H350 <O.CJ8H350
C8H5{O.C18H350 + NaOH - C3H5 \ OR + Na. 0. C18H350.
/OH (OH
Monostearin. Glycerol.
(O.C18H350 (OH
C3H5 I OH + NaOH - C3H5 \ OH + Na. 0. C18H,50.
(OH (OH
On this view "half made soap;' consists of a mixture of sodium stearate
with emulsified tristearin, distearin, and monostearin, uniformly dissemi-
nated through the water as a sort of jelly. A circumstance favouring
this view is that the quantity of glycerol obtainable from the first spent leys
is considerably less than the amount corresponding with the goods killed,
not much above one half as a rule.
GRAINING. 469
guided by indications only obtainable by practical experience,
the requisite physical condition is attained, representing a state
of matters where most but not quite all of the fatty matter is
saponified, whilst practically all the caustic soda in the leys has
been used up, furnishing an aqueous soap solution, or thin jelly,
with a little emulsified fat disseminated throughout.
Graining. — The next stage consists in "graining" or "cutting"
the soap by the addition of sufficient saline matter to render the
dissolved soap insoluble in the resulting weak brine. For this
purpose common salt is used, either solid fresh salt or that
regained from previous batches of liquor during boiling down to
recover glycerol (p. 514); or a strong brine is run in. The
quantity added depends on the proportion of water already
present in the copper relatively to the soap, which in turn
depends on the strength of the leys used and the quantity of
water condensed from " wet " steam ; moreover, soaps containing
much coker or palmnut oil require more salt than others, cceteris
paribus. When sufficient salt is present in the watery liquor,
a sample of the contents of the copper taken out on a trowel
shows a mass of grains of semisolid soap, whilst a clear watery
fluid runs away, which should not be markedly alkaline to the
taste, and should throw up no scum of fatty acids on acidulation ;
showing that practically all the soda used has been converted
into soap, and all the soap formed thrown out of solution by the
addition of sufficient salt. Explosive evolution of steam (violent
" bumping ;;) is very apt to occur during the graining process,
whence the use of a fan and curb (p. 433) in moderating the
frothing, whilst the kettle or copper used is only partly filled
with materials.
After standing for a few hours (steam being shut off) the
contents of the copper separate into watery " spent ley " which
is run off and utilised (for glycerol extraction, &c.), and pasty
" grain soap " consisting of about 3 parts actual soap to 2 of
adherent water : this is either finished at once (usually
pumped off into a smaller copper, or mixed with another batch
from another copper, there being less liability of violent frothing
over during the subsequent stages) ; or else more goods are
added with weak ley and the boiling recommenced as before
until the new batch of fatty matters is properly " killed," when
the whole mass is again salted out.
The grained soap, freed from spent ley, is then boiled up with
wet steam and an additional quantity of somewhat stronger ley
containing some 9 per cent, of NaOH (specific gravity about
1*09 to I'll) gradually run in so as to complete the saponification ;
the quantity finally added being sufficient to cause the mass to
separate into two (aqueous ley, and soap paste), the excess of
caustic soda throwing the soap out of solution just as salt does.
In some cases this operation is carried out in two stages, the
470 OILS, FATS, WAXES, ETC.
alkaline " half spent " ley run off in the first stage being utilised
for killing fresh goods ; this ley washes out entangled brine and
contains most of the remaining glycerol developed by the com-
pletion of the saponification. ] 11 the second stage sufficient water
is added (including that condensed from wet steam) to cause
the paste to again assume the " close " state by dilution of the
leys admixed with it, and the boiling continued long enough to
ensure the saponification of the last portions of glycerides, when
the soap is again grained or "made" by running in sufficient
stronger ley to throw it out of solution in grains. Finally the
half spent leys are partly, but not wholly, run off, and the soap
paste and remaining ley boiled up by means of the dry steam
coils, so that water is evaporated, whereby the residual ley
becomes more concentrated, and the soap paste less watery
(p. 467) : when the paste sets on cooling to the required con-
sistency and degree of hardness, the boiling is stopped and the
mass allowed to stand some hours so that the leys and curd may
thoroughly separate from one another : the. curd is then trans-
ferred to the cooling frames. Unless purposely watered or
boiled down to a less extent, curd soaps generally contain only
20 to 25 per cent, of water. When required to be as white as
possible, the curd is allowed to stand for some time before the
final boiling operation, so that coloured impurities may subside ;
the " cleansed ;' curd is then ladled or pumped off into another
copper in which the boiling down with close steam is effected.
The time occupied during these various operations varies with
the scale of operations and the skill of the workman : with batches
of 40 to 50 tons of goods (tallow and rosin for yellow soap) the
" killing " may be effected by an experienced hand in one day,
and the further process up to " making " the soap carried out on
the next day, the whole being furnished on the third day (Lant
Carpenter).
British curd soaps are usually made with tallow as chief in-
gredient with comparatively small admixtures of other oils and
fats ; they do not lather very freely, and " waste " in hot water
less rapidly than many other kinds of soap. The term " curd "
soap, however, does not necessarily denote a tallow soap, but
rather a soap boiled in a particular way.
Fitted Soaps. — In the manufacture of curd soaps more or less
of the alkaline ley on which the soap is finally boiled, is neces-
sarily left entangled in the interstices of the soap, incompletely
removed by gravitation whilst standing ; so that on analysis a
curd soap thus prepared always shows a considerable proportion
of " free alkali." In order to eliminate this an operation termed
" fitting " is carried out, more especially in the case of rosin
(yellow) soaps, whereby a peculiar texture is attained as the
result. The " made "" soap is allowed to stand some twelve
hours or more so as to bring about as complete separation of
FITTED AND MOTTLED SOAPS. 471
ley and curd as possible, and the half spent ley completely
pumped away. Wet steam is then turned on, the -condensation
of which dilutes the ley still entangled in the interstices of the
soap grains. With a particular stage of dilution (attained if
need be by adding water to dilute further, or a little stronger
ley if the dilution have gone too far) the mass of soap acquires
the property of allowing a watery soap solution to separate at
the bottom of the mass on standing (for some days with large
batches, for twenty-four hours with smaller ones), whilst the
rest of the soap forms a mass of jelly-like flakes, which solidify
on cooling to a yellow somewhat waxy and translucent solid,
usually containing a little under 30 per cent, of water. Before
this cools, it remains sufficiently soft to allow all dirt and solid
impurities, such as coloured metallic soaps (containing iron, &c.),
to subside by gravity, so that the lowest watery stratum is very
dirty and much discoloured, and in consequence is known as the
" negur " (sometimes spelt negre, nigre, nigger, &c.) The upper-
most layer of the " neat soap " resting on the negur generally
solidifies whilst standing to a solid frothy crust known as the
" fob." *
The character of the "fit" attained, whether "fine" or
"coarse," is judged by the indications observed on sampling
the mass from time to time with a trowel • when the physical
indications known by experience to denote the desired constitu-
tion of the mass are observed, the boiling is stopped, and the
copper covered over to keep in the heat, the whole being allowed
to stand at rest for from two to six days according to the size of
the batch. Finally the cover is removed, the fob carefully cut
away, and the still soft and semifluid neat soap pumped into the
frames. After cooling, fitted soaps generally contain notably
more water than curd soaps : from 28 to 33 per cent, is usually
present in nonsilicated genuine fitted soaps. The fob is gener-
ally worked up with the next batch"; the negur is either worked
up with coarse fats and darker rosin and made into a brown
rosin soap, or is utilised for making mottled soap.
Mottled Soaps. — In the earlier half and middle of the pre-
sent century the majority of soap manufactured was of the
curd class, and being made from leys directly prepared from
black ash without purification, generally contained more or less
sulphide of iron, or metallic soaps disseminated through it,
derived from the impure liquors, or in some cases purposely
added (in the form of raw or calcined green vitriol = ferrous
sulphate, &c.) The curd was boiled down until the proportion
of water therein was reduced to a quantity not exceeding about
* Society has been compared with a pot of porter, "dregs at foot, scum at
top, and good liquor in the middle ;" a copper of fitted soap with "negur "
and " fob " as the extremes and clean " neat soap " in the midst, would be
quite as apt a comparison.
472 OILS, FATS, WAXES, ETC.
20 to 23 per cent., and more frequently lying between 17 and 20
per cent. ; after standing and running off the leys, the whole was
well intermixed, and the greyish or otherwise coloured mass
run into the frames. During cooling and solidification the
colouring matters (chiefly iron soap) segregated from the rest of
the mass into veins ; so that when the solid soap was cut across a
peculiar characteristic marbling or mottling was evident. By
exposure to air the iron soap changed its colour from bluish grey
to red in consequence of oxidation, forming what was known in
the Marseilles district as the Manteau Isabelle. As this effect
could not be produced in the case of a curd soap insufficiently
boiled down (on account of the thinner texture permitting the
heavier metallic soaps, &c., to sink completely to the bottom,
like the negur of a fitted soap), the existence of a mottled appear-
ance came to be regarded as a criterion of good quality so far as
absence of an undue excess of water (say not above 20 per cent.)
was concerned. "Castile," "Marseilles," "Olive" and other
mottled soaps of this class, although still manufactured to some
considerable extent, are, however, but little made at the present
day for household use as compared with other varieties of
mottled soaps in which the one especial good point characterising
the old mottled soaps is wholly absent — viz., that only a limited
amount of water is present. A considerable degree of skill is
requisite in adjusting the proportions of materials used so that a
maximum of water can be incorporated without unduly inter-
fering with the veining of the mass. Usually silicate of soda
solution is used as stiffening agent, the fatty matters being
selected according to the judgment of the maker, and generally
containing a considerable proportion of palm kernel oil or coker-
nut oil, on account of the property of these oils to form soda
soaps possessing considerable stiffness even when largely watered
(p. 462). After admixture of the silicate the pigments intended
to give the mottle are added, and the mass thoroughly crutched
until sufficiently stiffened to run into the frames ; these are usually
made of wood so as to allow the mass to cool as slowly as possible
and cause the mottle to " strike " properly into veins. Soaps thus
made and " filled " with water and silicate often contain 50 per
cent, and upwards of water and not more than 40 to 45 per cent,
of actual soap.
Absolutely no good purpose whatever is fulfilled in com-
municating a mottle of this kind to household scouring soaps :
the only effect is that the public is induced to buy a greatly
inferior article on the strength of the reputation for quality
gained years ago by mottled soaps of the old style. Whatever
advantages may be gained by the addition of silicate as a cheap
detergent, these are wholly independent of the mottling.
A method of preparing hard soda soaps without employing
caustic soda (sometimes referred to as the "old German process'')
ROSIN SOAPS. 473
was formerly of considerable importance, although at the present
day the relative prices of potash and soda are such as to render
the process inapplicable, except in backwoods districts where
potashes are more readily obtainable than soda ash or caustic
soda. The tallow, or other mixture of fats and oils to be
saponified, is boiled up with potash ley (made by causticising
potashes with lime) much as in the process of soft soap making,
until a syrupy " close " soap is obtained ; this is then salted out
by the addition of common salt or brine, whereby a curd is
obtained mainly consisting of soda soap, the potash soap and
sodium chloride reacting on one another by double decomposition
(pp. 451, 489). The curd thus obtained is finished by repeating
the operations of boiling up with potash ley to complete saponifi-
cation, and salting out so as to transform the majority of the
potash soap still present into soda soap ; the curd ultimately
obtained after a sufficient number of such treatments being
finally boiled up with ley until any entangled salt is washed out,
whilst the ley becomes sufficiently concentrated for the curd to
separate properly.
In all probability, hard soda soaps were first prepared on a
comparatively large scale by this kind of process, rather than by
saponitication with caustic soda direct ; although the use of
" maritime alkali " (barilla) appears to have been practised in the
Marseilles district as long as the soap manufacture has existed
there. In inland districts, however, where seaweed ash was
practically unattainable, or at any rate costly as compared with
vegetable potashes, this "old German" process was the one
chiefly employed for making hard soaps until the discovery by
Leblanc of the method of preparing soda from common salt that
bears his name.
SPECIAL VARIETIES OF SOAP.
Rosin Soaps (Yellow Soaps). — In the manufacture of soaps
of this description ordinary rosin (colophony) is used as an
ingredient, the mixture of alkaline salts of rosin acids and of
fatty acids being peculiarly well adapted for certain purposes.
In one method of procedure (Meinecke's) crude turpentine is
added to the soap pan, which is fitted with a still-head, so that
the spirit of turpentine volatilised along with the steam is con-
densed and utilised. A much more frequently used process,
however, is to separate the spirit and rosin by the ordinary dis-
tillation process, and to mix the latter with the fats, &c., to be
saponified, so that a mixture of the alkali salts of fatty and resinous
acids results ; whilst a further improvement (sometimes termed
the " French process " for rosin soap) consists in dissolving the
rosin in hot alkaline ley separately (p. 453), adding the resulting
474 OILS, FATS, WAXES, ETC.
resinate of soda solution to the finished soap, well crutching the
two together ; or adding it to the soap in the pan and inter-
mixing by boiling up for a few minutes.
Rosin soaps of the better quality are generally " fitted "
(p. 470). When made from sound fatty matters and light
coloured rosin (" windowglass rosin") they possess a peculiar
odour not disagreeable, and are known in the south of England
as " Primrose " soap ;* such soaps usually contain about 30 to
33 per cent, of water and 66 to 69 per cent, of actual soap
(including resinate of soda). Coarser rosin soaps made from
dark brown rosin, damaged fats, horsegrease, and the like, have
generally a more or less marked unpleasant animal odour, partly
disguised by the rosin, or by the addition of nitrobenzene (arti-
ficial oil of almonds, or essence de mirbane) or other cheap scents.
Rosin soaps are generally preferred as stock soaps for trans-
parent soapmaking by the spirit process, as the presence of
alkaline resiiiates facilitates the acquisition and retention of the
colloid structure requisite for transparency ; moreover, a well
fitted rosin soap will dissolve practically completely in spirit,
not leaving behind any sodium carbonate or other insoluble
matters requiring separation by subsidence or filtration. A
similar product is also obtainable by dissolving in spirit an
ordinary curd soap (cut into shavings and dried) simultaneously
with rosin, whereby the free alkali contained in the stock soap
is neutralised, and an alcoholic solution of mixed fatty and
resinous soaps directly obtained.
The determination of the relative amount of resinous acids and
fatty acids present in a given sample of soap is in many such
cases a somewhat important matter ; this may be effected by the
methods described on p. 501, et seq.
Silicated Soaps. — Household soaps, properly socallecl, consist
of the alkaline (potash or soda) salts of certain organic acids,
either belonging to the various fatty acid series, being derived
from natural oils and fats, or to other series of more feebly,
marked acids derived from resins, more especially colophony.
The older soaps (of the first half of the present century) were
essentially of this character ; but a considerable proportion of
those now manufactured are cheapened by the admixture of
various ingredients possessing more or less marked detergent
power, the addition of which enables a given weight of socallecl
soap to be manufactured from a greatly decreased quantity of
fatty matters. Of these detergent substances, obviously the
most natural constituents are the alkalies themselves, either in
the form of hydroxides (caustic alkalies) or as carbonates ; in the
* In some districts in the north of England the term "primrose'' is
applied to greatly inferior articles, usually largely watered and treated
with silicate of soda to stiffen them, so that the actual soap present consti-
tutes notably less than one half the mass, like the inferior mottled soaps
described on p. 472.
SILICATED AND SULPHATED SOAPS. 475
manufacture of "oil" soaps (oleic acid soaps, p. 452) these con-
stituents are introduced by the simple process of using a larger
quantity of alkaline ley than is equivalent to the fatty acids ; in
other cases, the alkalies are dissolved in water and crutched into
the soap before framing. The introduction of silicate of soda
solution has various advantages as compared with that of caustic
alkalies, proper incorporation being more easy ; whilst for such
purposes as scouring floors, &c., the increased detergence thereby
gained is distinctly advantageous. For laundry soaps, on the
other hand, the utility of silicates is far less manifest ; so much
so, that various much advertised laundry soaps of the present day
are purposely prepared without that ingredient (sodium carbonate
being in some cases used instead) ; to which circumstances they
largely owe what superiority they may possess over other silicated
soaps.
One notable advantage gained by the admixture of silicate of
soda with soaps made from cheap soft fats, &c., is that the texture
of the bar of soap is considerably stiffened and hardened, so that
the soap does not waste so rapidly in hot water or when rubbed
against the clothing, tfec., to be washed, as it otherwise would
necessarily do.
Normandy Soaps (Sulphated Soaps). — In order to harden
and stiffen a comparatively soft soap mass various neutral salts
may also be employed, more especially sodium sulphate or thio-
sulphate. The use of these stiffening agents was originally
introduced by Dr. Normandy, not for purposes of adulteration
or "filling," but in order to enable useful household scouring
soaps to be made from materials that otherwise would give a
product too soft for economical use in scrubbing, especially with
hot water. When sodium sulphate (Glauber's salt) was used,
the crystallised salt (not salt cake) was heated so as to fuse in
its own water of crystallisation,* the liquid being immediately
crutched into the hot soap ; from one-fifth to one-third of the
weight of the soap being thus added. The soaps thus made
rapidly become unsightly through efflorescence ; so that their
use at the present day is not large, other stiffening agents (more
especially alkaline carbonates and sodium silicate) being pre-
ferred.
Aluminated Soaps. — Aluminate of soda has been proposed,
and to some extent used, as a substitute for silicate of soda in
the preparation of scouring soaps, for which purpose it does not
seem to have any special advantages or marked disadvantages.
Borax Soaps. — The addition of borax to laundry soaps is
sometimes made, that salt possessing considerable detergent
power without injurious action on textile fibres j it is usually
* If salt cake is used, it must be dissolved in the right quantity of water
and treated with a little soda ash, so as to neutralise the free acid present
and precipitate the ferric oxide contained as sulphate.
476 OILS, FATS, WAXES, ETC.
supposed, moreover, to have a special blanching action on linen.
Some socalled " borax soaps," however, are in the market that
contain only extremely minute amounts of borax, or none at all.
Phosphated Soaps. — In order to diminish the waste of soap
with hard water through double decomposition by the lime and
magnesia salts present, H. Grimshaw* adds an alkaline phosphate
to the soap, with the object of forming calcium and magnesium
phosphates instead of lime and magnesia soaps insoluble in water.
Paraffin Oil and Petroleum Soaps. — Hydrocarbons of the
paraffin series possess the physical property of forming jellies
when admixed with soap solutions under suitable circum-
stances ; a small quantity of soap will thus solidify a large
quantity of hydrocarbon, a circumstance taken advantage of in
manufacturing " solidified petroleum " for fuel. On the other
hand, 10 or 20 per cent, of such oil can be crutched into a hot
soap paste without materially interfering with its setting on
cooling, so that a large amount of "loading" may be thus effected.
With certain kinds of transparent soap (made by the cold process,
pp. 458, 482) this addition is frequently made.
For laundry purposes the diluting effect of the hydrocarbon
oils is more or less compensated by an increased detergent action :
greasy linen, &c., soaped with "paraffin soap" can often be cleansed
with less rubbing and friction than would otherwise be necessary
because the hydrocarbon tends to dissolve the grease and so to
facilitate the detergent action of the soap so far as other dirt is
concerned.
Sand, Puller's Earth, Pipeclay, Kaolin, and Brickdust
Soaps. — When soap is required for household or other cleansing
purposes to be used in conjunction with fuller's earth, powdered
brickdust or pumicestone, sand, emery, or such like materials so
as to brighten metallic surfaces, cleanse greasy paint (insides of
baths, &c.), and so on, it is often found convenient to prepare
blocks of mixed mineral powder and soap for sale ; these are
made by crutching the pulverised pumicestone, &c., into the
hot melted soap in as large a proportion as is consistent with its
sticking together in blocks when cold, and are then sold under
various proprietary names, chosen according to the fancy of the
maker. For general cleansing purposes such mixtures are often
very handy; but the price charged, although moderate enough as
regards the weight of the block as a whole, is generally high
with respect to the quantity of soap actually present therein.
Superior kinds of such soaps are sometimes sold as "tooth soaps,"
prepared by incorporating with a good kind of remelted toilet soap
some 10 to 20 per cent, of finely powdered marble or pumice-
stone, cuttlefish bone, prepared chalk, &c., &c.
Disinfectant Soaps. —A large variety of soaps are in the
market consisting of ordinary soaps of more or less good quality
* English Patent, No. 983, 1890.
COLDWATKR SOAPS. 477
into which have been crutched, before finally cooling and
solidifying, fluid or other disinfecting materials, more espe-
cially those derived from coaltar products — e.g., carbolic and
cresylic acids, naphthol, naphthalene and creosote oils, &c. ; or
the artificial camphoraceous products got by the oxidation of oil
of turpentine (Sanitas oil) ; or hydrocarbons, such as terebene ;
or various inorganic germicide materials. Of these different
products, a considerable number are highly valuable for the
particular purposes for which they are intended ; but the value
of others is, at the best, only small as antiseptic and disinfectant
agents.
To this category also belong a variety of " medicinal " soaps,
usually put up in tablet form like "toilet" soaps (p. 478); in
these a stock soap of more or less good quality forms the basis,
sulphur, iodine, ichthyol, mercurial preparations, or other medi-
caments, supposed to exert beneficial action in certain cases when
thus applied to the skin, being mixed in either by remelting or
milling, or in some cases being added to the mass formed by the
cold process before it finally solidities.
Coldwater Soaps. — Various soaps are sold under this name,
the alleged advantage of which is usually stated to be that they
will lather freely with cold water and therefore do not require
clothes, etc., to be boiled. In many cases a more accurate
description wrould be that they dissolve so freely in hot water as
to be highly wasteful when used therewith. They generally
consist of more or less watered soaps * containing cokernut or
palm kernel oil to give consistency, with a liberal intermixture of
potassium or sodium carbonate (less frequently of silicate) to
harden and give increased detergent action ; in practice they are
equivalent to a mixture of 'true soap and soda crystals, and like
sand and brickdust soaps they are accordingly very handy in
use ; but in general the price is high .as compared with the actual
amount of soap present.
Soap Powders. — The above remark applies a fortiori to these
substances which in general consist of ground-up soda crystals
(sometimes of ordinary soda ash) with more or less pulverised
dry soap intermixed ; they are usually highly efficacious as deter-
gents, but somewhat dear as compared with the value of the
alkali present and the soap, taken separately from the water of
crystallisation and other inert constituents.
Starch Soaps, Oatmeal Soap, &c. — More than one patent
has been taken out for the preparation of products where potato
jiour, starch, and similar materials are intermixed with ordinary
* Some few "cold water1' soaps do not contain more than 20 to 25 per
cent, of water, and are made with only comparatively small additions of
potassium or sodium carbonate, the former being preferably used to soften
the texture, a result also partly brought about by the use of semidrying oils
as ingredients — e.g., cotton seed oil.
478 OILS, FATS, WAXES, ETC.
soaps. The advantages of such mixtures are difficult to under-
stand. Oatmeal, however, well intermixed with some reasonably
good quality of stock soap, enjoys some degree of popularity as a
"skinsoap." Bran and gluten have been used for the same
purpose ; as also dextrine, Iceland moss and other lichen jellies,
sawdust, cornflour, and various analogous substances.
TOILET AND FANCY SOAPS.
The term " toilet soap " is generally supposed to denote a
superfine variety of soap specially prepared with the object not
only of effecting cleansing during ablution, but of doing this
in the most delicate way with regard to injurious action on the
skin, thus serving as a sort of cosmetic. Some of the socalled
toilet soaps in the market well fulfil this description ; but,
unfortunately, many others are largely advertised and sold which
are of a far less satisfactory character, either through imperfections
of manufacture (more especially presence of excess of alkali), or
because of their having an objectionable action on tender skins,
through admixture of other ingredients (particularly cane sugar).
Some varieties of socalled toilet soaps are simply household
soaps of the finer class, more especially curd and yellow soaps
made from first class materials, cut up into tablets, and stamped
into shape by one or other of the various kinds of stamping
press referred to on p. 444. As a rule these are scentless, but
sometimes a small proportion of cheap essential oil or other
perfume (such as citronella, mirbane, &c.) is crutched in before
framing.
More frequently stock soaps of good quality are prepared on
the large scale from choice, or at least sound, materials, and
are then cut up, intermixed or blended, remelted, and again
framed, working on a smaller scale : usually scenting materials
are introduced just before transferring to the frames, and in
some cases emollient ingredients or unguents — e.g., lanolin, vase-
line, beeswax, spermaceti, or various undecomposed glycerides,
such as the finest beef marrow, lard, the socalled " beef stearine "
separated from the more fusible fats in the manufacture of mar-
garine (p. 309), «kc. Of late years "superfatted" soaps of this
description (in some cases made by remelting, in others by
milling — vide infra) have been somewhat largely "boomed,"
the special advantage derived from their use being supposed to
be that an extremely thin greasy film adheres to the skin after
use, which more or less prevents the drying and chapping
action otherwise produced by ordinary soaps on tender skins.
Opinions differ widely as to how far this alleged advantage is
really gained or not, some regarding the presence of a few
per cents, of glycerides in the soap as actually furnishing a
TOILET AND FANCY SOAPS. 479
protective film of the kind, rendering the outer layer of the
skin soft and supple ; whilst others consider that inasmuch as
the action of water on perfectly neutral soap always liberates
more or less free alkali, which emulsifies grease and enables it
to be washed off, whilst any excess of alkali naturally contained
in the soap accelerates the action, the notion .of an adherent
protective grease film is a priori improbable ; the advantage of
such soaps lying rather in their freedom from excess of alkali
arid other objectionable skin roughening substances such as.
sugar. On the whole, the preponderance of opinion rather
seems to be in the direction of regarding nonglyceridic un-
guents (lanolin, spermaceti, etc.) as being more " emollient ;>
when thus admixed with soap than glyceridic materials such
as usually found in "superfatted" soaps — i.e., when all other
things are equal, especially absence of free alkali ; moreover,
the presence of unsaponified fatty matters seems sometimes to-
facilitate discoloration on keeping through the development of a,
kind of rancidity.
In some cases "pearlashing" (pp. 451, 489) is adopted to improve
the texture and lathering power ; when this is done the pearlash
liquor (solution of potassium carbonate) is simply crutched in
with the other ingredients before framing. Since an equivalent
of sodium carbonate is formed for one of potassium carbonate
introduced, obviously, a pearlashed soap is apt to be strongly
alkaline and objectionable for persons suffering from tender
skins, or a tendency to acne or eczema.
Milled Soaps. — "Perfumers' soaps," sometimes known as.
" little-pan soaps," were formerly largely made by perfumers by
means of the cold process. The fatty matters thus employed
were generally of excellent quality, being mainly the oils and
fatty cakes used to absorb flower perfume (odorous essential
oils) by packing the fat cakes and flower petals together, or by
passing air over the flowers and bringing it in contact with oil,
etc., to absorb the volatile odorous matter; after the oil or fat
was fully charged by numerous repetitions of the process it was
treated with alcohol, whereby a flower essence was obtained by
dissolving out the essential oils, leaving behind a delicately
scented fat, capable of furnishing a deliciously perfumed soap.
Owing, however, to the necessity for avoiding heat as much
as possible in the preparation of the soap, it often happened
that these soaps contained simultaneously much undecomposed
fat and a large amount of free alkali. Accordingly, of late years
they have been largely supplanted by "milled" soaps, where
stock soaps of good quality are " stripped " or reduced to chips
and dried until only a few per cents, of moisture are retained,
and then ground (together ^ with perfumes, colouring matters,
glycerine, or other emollient ingredients, etc., as required) be-
tween rollers until reduced to a stiff putty-like mass, which is
480 OILS, FATS, WAXES, ETC.
then squirted or screwed into bars and so formed into tablets
(p. 448). The advantages of this method are, firstly, that inas-
much as no artificial heat is applied, delicate flower perfumes, &c.,
can be readily incorporated with the soap mass, which it would
be impossible to use with a remelted soap because the heat
would dissipate or destroy the odorous matter; and secondly,
that as the resulting tablets usually contain only a small quantity
of water, a given weight of soap tablet generally contains a much
larger quantity of actual soap than another tablet of the same
weight prepared by remelting or by the cold process, whilst,
being harder and stiffer, it lasts longer, wasting less rapidly
during use. By suitably choosing the stock soaps used, em-
ploying only such as have been prepared from first class oils and
fats, etc., and refined or otherwise treated to remove " free "
alkaline matters, "fancy" and "toilet" soaps of the finest possible
qualities are thus readily obtainable. Frequently the stock soaps
are partly made with potash and partly with soda, so as to arrive
at a suitable texture through the softer nature of the potash soap,
as well as to produce a better lather.
In this connection it is worth noticing that there is some
reason for supposing that soap with which an extremely large
proportion of flower essences and essential oils is incorporated,
may thereby become less suitable for use by persons suffering
from tender skins than would be the case with a lessened amount
of odorous matter, inasmuch as many essential oils of the kind
possess more or less marked rubefacient (skin-reddening) action,
analogous in character to the stimulating and blistering action of
mustard, oil of turpentine, and similar substances. It is within
the author's own personal observation that when the same high-
class soap mass is used for preparing two differently priced fancy
soaps, only differing in that the more expensive one is impregnated
with a much larger proportion of scent than the other, persons
possessing exceptionally sensitive skins can sometimes use tablets
made from the less highly scented portion with impunity, whilst
the employment of tablets made from the more strongly per-
fumed portion speedily sets up a disagreeable amount of skin
irritation.
From the point of view of irritating skin action, however, the
presence of sugar appears to be much more objectionable than
that of most scenting materials, even in large quantity. Opaque
fancy soaps are rarely, if ever, admixed with this adulterant ;
but very little transparent soap is in the market that does not
contain more or less.
Brown Windsor Soap. — The term " Brown Windsor " has
long been applied to a peculiar brown soap highly esteemed for
toilet purposes. Originally this substance deserved its reputation ;
but as in the case of "mottled" soap, the perverted ingenuity of the
modern adulterator has completely altered the character of the
TRANSPARENT SOAPS. 481
great majority of toilet tablets sold under that name. The " Old
Brown. Windsor " of a generation or two back was simply a form
of soap (usually mostly curd) that had been kept in stock for a
great length of time, and occasionally remelted ; with the
result of acquiring a pretty deep brown tint through oxidation
of fatty acids, &c., and of becoming practically wholly devoid
of free alkali, any excess of alkali originally present being
neutralised by the weakly acid oxidation products formed
during keeping or " ageing," or whilst being remelted. Such a
soap, pleasantly scented at the last remelting before making into
tablets, and originally made from suitable materials, lathered
sufficiently freely to be conveniently used, and had as little
deleterious action on sensitive skins as is compatible with the
hydrolytic properties of soaps generally. The modern substitutes,
however, are frequently nothing but coarse soaps made from dis-
coloured fats, and further browned by coaltar dyes or admixture
of brown ochre : all sorts of scraps (including floor scrapings)
incapable of utilisation in any other way are worked into the
mass, which frequently is alkaline to a highly objectionable
extent. In short, advantage is taken of the reputation deservedly
gained in former years by an excellent article to sell under the
same name an eminently inferior product. Similarly, socalled
" White Windsor " soaps are sometimes to be met with, largely
made from cokernut oil, highly alkaline, and wholly different in
character from the genuine old fashioned brown article.
Transparent Soaps. — As already stated, soap can in many
cases assume two distinct physical conditions, one a more or less
distinctly crystalline form in which the "grains" retain associated
by a sort of physical attraction a considerable quantity of water,
the amount of which varies with circumstances — e.g., a curd soap,
when granulated from a dilute liquor with a minimum of salt or
alkali, will contain as much as 35 to 40 per cent, of such associated
water, which becomes gradually lessened down to 20 to 25 per
cent, or less by boiling down with dry steam or free fire so as to
concentrate the leys. The other is a structureless colloidal state,
constituting a mass which under suitable conditions is clear and
transparent like a strong jelly. Soft soaps (potash soaps) appear
to have a stronger tendency to retain this colloidal state than
hard (soda) soaps, so that it is only with comparative difficulty
that they become granular ; soda soaps, on the other hand,
although granular when separated from watery solutions by
means of salt, readily become colloidal when dissolved in alcohol,
so as to form transparent masses when the solvent evaporates.
This physical condition is facilitated in many cases by the presence
of various other substances, of which glycerol is one of the best
known ; so that fats saponified by the cold process, even in the
absence of alcohol, often yield transparent products owing to
the production of glycerol during the process. Castor oil, in
31
482 OILS, FATS, WAXES, ETC.
particular, readily yields a transparent product in this way.
Cane sugar possesses the same property ; and being cheaper and
easier to work with in some respects, is largely substituted for
glycerol, to the great disadvantage of the consumer, excepting in
one respect, viz., that whilst transparent soaps containing large
percentages of glycerol are apt to " sweat," by attracting moisture
from the air, sugared soaps do not deliquesce so markedly.
Resinates mixed with ordinary fatty acid soaps generally form
colloidal masses more readily than the latter alone ; accordingly,
rosin soaps are preferred as " stock " when granular soaps are to
be rendered transparent. This tendency to transparency is often
strongly marked even with water-made rosin soaps of good quality
("fitted" soaps), which generally become translucent and some-
times tolerably clear when spontaneously dried in not too thick
masses.
Accordingly, two principal methods are in use for the prepar-
ation of transparent soaps. In the "spirit" process the stock
soap is dissolved in spirit and treated as described (p. 445), rosin
being sometimes added to the mass for the double purpose of
aiding transparency and combining with free alkali so as to
neutralise it.* The mass left when the bulk of the spirit is
distilled off is usually turbid ; but on slow drying in a warm
storage room (temperature near 35° C. = 95° F.) it becomes clear,
especially when a liberal addition of sugar has been made to the
mass before finally casting in the frames. Usually the blocks
are cut up into tablets which are shaped by stamping in blank
dies, and then slowly dried, the final impression being given by
a later stamping. When glycerol is added instead of sugar, the
resulting transparent soap is as innocuous, even to the most
sensitive skin, as any kind of soap can possibly be ; but the same
can by no means be said of sugared soaps (which constitute the
large majority of those in the market), persons of unusually
tender skins being generally unable to use such compositions
long without suffering more or less severely in consequence.
Similar remarks apply to the transparent soaps made by the
other process (cold process, p. 458) ; when sound fatty and oily
matters are used, together with alkali not in excess, no sugar
being employed, an article results of superior kind ; but the
great bulk of socalled " glycerine " soap made in this way is
alkaline to an extent highly prejudicial to tender skins, besides
being largely admixed with sugar, f whilst in many cases the oils
used (chiefly castor oil, together with cokernut oil, &c.) are of
such quality as to leave an unpleasant odour on the skin, easily
* Some transparent soaps thus prepared when dissolved in water and
agitated with petroleum spirit, or when dried and percolated therewith in
a Soxhlet tube, will yield several per cents, of uncombined colophony to the
solvent.
t For a typical analysis of a soap of this kind (not loaded with hydro-
carbons) vide p. 511.
NEUTRALISED SOAPS. 483
perceptible when the scenting material has evaporated • and in
addition, large percentages of valueless " loading " (petroleum
hydrocarbons, £c.) are added to increase the weight. In short,
transparent toilet soaps, like artificially mottled scouring soaps,
are articles in the purchase of which caution is pre-eminently
desirable. For further details concerning transparent and other
toilet soaps and their manufacture, vide the author's " Cantor
Lectures on the Manufacture of Toilet Soaps " (Journal Society of
Arts, 1885).
Soap Leaves. — A very convenient form of soap for travellers
is obtained by melting a good quality of stock soap with a little
water, perfuming to taste, and passing sheets of tissue paper
through the fluid; the paper thus filmed with soap is dried and
cut up into leaves, one of which generally suffices for ordinary
washing of the hands, &c., thus avoiding the necessity of having
to carry about a wet cake of soap.
Marbled Soaps and Harlequin Soaps. — A peculiar marbled
appearance is sometimes given to soap balls, tablets, &c., by
remelting a more or less white stock soap, and running 'it into a
small frame ; a comb with wide teeth is then dipped into a
colouring composition (melted soap with pigments or dissolved
colouring matters), withdrawn, and passed through the semifluid
soap in the frame, so as to streak it according to fancy. The
same method is applicable to cold process compositions, before
they have completely solidified. By cutting up pieces of variously
tinted soaps into fragments, and scattering them through a cold
process transparent soap mass on the point of solidifying, a
mixture of transparent soap with variously tinted lumps inter-
spersed is ultimately obtained ; when cut up and stamped into
tablets, these are sometimes sold as " harlequin soaps." Tablets
are sometimes ornamented by stamping a device somewhat
deeply, and then filling the grooves with melted coloured trans-
parent soap, &c.
Shaving Creams. — Cold process soaps made from refined lard
or other superfine fatty matters and caustic potash, not used in
excess, are usually the basis of these preparations ; to facilitate
lathering, a small quantity of the finest cokernut oil is often
added. The resulting mass is ultimately ground in a marble
mortar, <fcc., with scenting materials (oil of bitter almonds for
almond cream, and so on), glycerol or other emollient ingredients
being added to taste, and sometimes tinting materials — e.g., a few
grains of vermilion per Ib. — to give a faint flesh colour, &c. A
perfumed concentrated alcoholic solution of soap forms a variety
sometimes known as " liquid soap."
Neutralised Soaps. — For certain special purposes it is highly
important that the soapr employed should be as devoid of free
alkali as possible. In order to effect this object a variety of
methods have been proposed and more or less largely employed,
484 OILS, FATS, WAXES, ETC.
according to circumstances. In the generality of cases soaps
that have been put through the operation of "fitting" (p. 470)
are almost absolutely neutral, any entangled alkaline ley present
in the curd before fitting having been washed out during the
process ; if, however, after " cleansing " in this way so as to
separate coloured impurities, the soap be again boiled down on a
fresh portion of ley, the resulting curd soap is always consider-
ably alkaline through entangled ley. A method used with some
degree of success consists in remelting (p. 441) the soap to be
treated with a small proportion of fatty matter which becomes
more or less saponified by the treatment ; inasmuch, however, as
the alkali present is generally carbonated, this method rarely
gets rid of all the free alkali, excepting in cases where the addi-
tional fatty matters used consist largely of free fatty acids like
some kinds of largely hydrolysed palm oil.* In the manufacture of
transparent toilet soaps by the spirit process, any carbonated
alkali present is left undissolved and is, consequently, separated
by subsidence or straining ; whilst if rosin be directly added, the
free alkali present is more or less converted into resinate and so
eliminated. When, however, resinous or fatty materials are
added to a soap mass in the milling process, no action ensues
between them and the free alkali ; so that " superfatted " soaps
thus prepared (without long continued fusion of the glycerides
with the soap by remelting) often contain simultaneously excess of
alkali and unsaponified glycerides, like imperfectly made cold pro-
cess soap (p. 457). The author's ammonium salt process, referred
to on p. 453, on the other hand, acts equally well in the way of
removing "free " alkali, whether applied to soap shavings during
the milling process, or to fused soap during remelting, or to soap
curd, &c., in the crutching pan; any alkaline carbonate or
hydroxide being converted into a neutral salt with simultaneous
evolution of ammonia which mostly escapes.
CHAPTER XXL
GENERAL CHEMISTRY OF SOAP— SOAP ANALYSIS.
IN addition to various points previously discussed in connection
with the general chemical and physical properties of oils, &c., a
variety of other matters are of some interest relating to the
properties of soaps of various kinds.
* According to A. Watts, the superiority of the madder purples for which
the firm of lloyle & Sons were long famous, was due to their practice of
remelting the best soaps procurable with an additional quantity of palm
oil.
CHEMISTRY OP SOAPS. 485
As already explained, what is ordinarily meant by the term
"soap" is simply the various substances obtainable consisting
of the alkaline (potash and soda) salts of the various fatty acids
contained as glycerides in oils and fats, and of the rosin acids
contained in colophony and allied resinous matters. Numerous
corresponding salts of the alkaline earths and heavy metals,
however, exist, all of which, strictly speaking, are also soaps —
e.g., the lime "rock" obtained in the manufacture of candle
stearine (pp. 365, 373), and the "lead plaster" obtained by mixing
together olive oil (or other analogous oil) and litharge. As a
general rule these earthy and metallic soaps are insoluble in
water, at any rate as compared with alkali soaps ; so that on
adding a metallic salt solution to an aqueous solution of alkali
soap, double decomposition occurs, and a precipitate is formed of
the metallic soap. Thus, for example, the applicability of Clark's
soap test for lime and magnesia in water depends on such
actions — e.g., in the case of stearates —
Sodium Stearate. Calcium Sulphate. Calcium Stearate. Sodium Sulphate.
2Na . 0 . C18H850 + CaS04 =
Similarly Gladding's test (p. 501) for rosin acids in soap depends
on the precipitation of silver stearate, oleate, &c., insoluble in
ether containing a little alcohol when silver nitrate acts on an
alcoholic solution of mixed alkali salts ; whereas silver resinate
is soluble in that medium.
Alkali soaps often possess in a high degree the peculiar
property of gelatin and other colloid bodies — viz., that whilst on
heating with hot water they apparently dissolve to an ordinary
solution, on cooling this does not allow crystals of material to
form through diminished solubility on account of lowered tem-
perature, but instead sets to a more or less firm jelly. This
property of "jellifying" is often used as a practical test of the
value of soap for certain purposes ; a known weight of soap is
dissolved in water (conveniently 1J ounce to a pint = 20 fluid
ounces, or 62 -5 grammes per litre) and the solution allowed to
cool ; the rate at which the fluid gelatinises, and the texture of
the resulting jelly are noted. Preferably the soap is dissolved
in about half the total quantity of water, boiling, and when all
is in solution the rest of the water is added cold.
Although alkali soaps are usually freely soluble in water,
especially when hot, yet the presence of certain other substances
in solution prevents their dissolving, whilst the addition of these
substances to aqueous soap solution causes the precipitation of
more or less of the dissolved soap ; thus the process of " salting
out" half made soap in the open pan boiling process (p. 469)
depends on the less degree of solubility of soap in brine than
in pure water. Similarly, when curd soap is boiled down on
486 OILS, FATS, WAXES, ETC.
an alkaline ley, the soap is rendered less and less soluble in
the watery liquor as the concentration proceeds, and at the end
of the operation is wholly insoluble therein, even if partially
soluble at first when the ley was weaker.
The proportion of salt relatively to water required to render
a given soap insoluble, obviously varies with the nature of the
fatty acids present ; thus whilst sodium stearate and palmitate
are precipitated from solution by comparatively small amounts
of salt, cokernut and palmnut oil soaps are sufficiently soluble
to remain dissolved in seawater, which usually contains 3 to
4 per cent, of dissolved solid matters, mostly sodium chloride.
In hot brine the solubility of soap is usually greater than in
cold : thus in the course of a variety of experiments on the
solubility of soaps in saline solutions Whitelaw found * that
tallow soap was completely soluble to a clear fluid in a boiling
solution containing not more than 3'0 per cent, of NaCl, the
whole setting to a firm jelly on cooling ; whilst palmnut oil
soap dissolved clear in a boiling solution containing not more
than 13*0 of NaCl, a large portion of the soap being thrown out
of solution on cooling.
The curd thrown out of solution by salting retains an amount of
associated water incapable of expression mechanically by moderate
pressure in a dry cloth, and hence not in quite the same condition
as ordinary mechanically entangled fluid ; the amount of this
water varies inversely with the concentration of the saline solu-
tion ; thus the longer a curd soap is boiled down on the ley so
as to concentrate this, the less is the proportion of moisture
retained by the soap after separation from the ley and framing
so as to solidify. In similar fashion, Whitelaw found that an
olive oil soap retained the following amounts of water after half
an hour's boiling with different brine solutions : —
Salt in Brine. Water in Curd.
8 per cent. 31 '6 per cent.
17 „ 25-7
27 (saturated). | 19'1 „
Hydrolysis of Soap Solutions. — When soaps are dissolved
in absolute alcohol, or in spirit containing but little admixture
of water, no visible decomposition ensues ; a neutral soap
gives a solution which has no action on suitable indicators
— e.g., phenolphthalein. If, however, water be substituted for
spirit, the soap is more or less broken up into caustic soda and
an acid soap — e.g., in the case of stearate —
Sodium Stearate. Water. Caustic Soda, Sodium Acid Stearate.
2Na . 0 . C18H350 + H20 NaOH + { H* ! O ! C^O
A pretty way of illustrating this action is to boil a piece of dried
* Journ. Soc. Chem. Ind., 1886, p. GO.
HYDROLYSIS OF SOAP SOLUTIONS.
487
soap with alcohol to which a little phenolphthalein has been
added, and filter the solution into a tall jar or large test tube ;
the solution should be strong enough to set to a firm jelly on
standing. When set, a little distilled water is poured on the
top of the jelly ; this hydrolyses the soap in the top layer so as
to turn it pink by the reaction on the phenolphthalein of the
liberated alkali. On standing, the water gradually dialyses
downward through the colloid soap mass, and the pink colour
descends with it.
By adding salt to an aqueous solution of soap so as to salt out
the curd completely, filtering off, and examining the filtrate
alkalimetrically, the amount of alkali set free under given condi-
tions can be determined ; or the same result can be got at (with
more trouble) by collecting the salted out curd, washing with
brine over the vacuum filter, dissolving the curd in absolute
alcohol, and titrating the acidity with phenolphthalein as indi-
cator. A long series of observations thus made led to the
following results : — *
Hydrolysis brought about by x Molecules
Mean
of Water.
Fatty Acids.
Molecular
Weight.
a; =150
33 = 250
x = 500
03 = 1000
x = 2000
Pure stearic acid,
284
07
i-o
1-7
2-6
3-55
Nearly pure palmitic acid,
250
1-45
1-9
2-6
3-15
3-75
Crude lauric acid (cokernut
oil), ....
195
3-75
4-5
5-4
6-45
7-1
Pure oleic acid,
2S2
1-85
2-6
3-8
5-2
6-65
Crude ricinoleic acid,
294
1-55
2-2
3-0
3-8
4-5
Chiefly stearic, palmitic,
and oleic acids (palm oil
tallow soap),
271
1-1
1-55
2-6
4-1
5-3
Chiefly tallow and rosin
*
(primrose),
280
1-5
2-2
3-1
4-2
5-3
Cotton seed,
250
2-25
3-0
5-0
7-5
9-5
Fig. 143 represents these results in the form of curves, from
which it would seem to result inter alia that amongst homologous
soaps (stearic acid, palmitic acid, cokernut oil acids) the higher
the molecular weight the less rapid the hydrolysis.
If extra alkali be added to the soap solution, the hydrolytic
effect is proportionately weakened, as suggested by the character
of these curves, concave downwards ; thus the following figures
were obtained with some of these same soaps : —
* Alder Wright and Thompson, Journ. Soc. Chem. Ind., 1885, p. 625;
Alder Wright, "Cantor Lectures," Society of Arts (Journal Soc. Arts,
xxxiii., 1885, p. 1124).
488
OILS, FATS, WAXKS, ETC.
Nature of Fatty Acids Used.
Extra Na2O
added to
Solution, per 100
Soap.
Hydrolysis brought about by
x Molecules of Water.
x= 50
a= 250
x = 2000
Crude lauric acid (cokernut),
Cotton seed oil soap,
Stearic and oleic (tallow),
Tallow rosin (primrose), .
11-0
15-0
20-0
150
1-1
nil.
nil.
nil.
1-6
nil.
nil.
o-i
2-0
6-5
nil.
1-3
The property of becoming hydrolysed by water has a great
deal to do with the cleansing and detergent action of soap ; the
Values of X.
Fig. 143.
minute amount of alkali set free helps to emulsify greasy matters,
and thus greatly facilitates their removal by washing out under
friction.
Heaction of Soap Solution or of Fused Soap on In-
organic and other Salts. — When a solution of sodium chloride
is added to one of a soda soap, or one of potassium carbonate to
a potash soap, there being but one base present, obviously, no
tendency can exist towards double decomposition and exchange
of bases ; but it is otherwise if sodium chloride be added to a
potash soap, or potassium chloride to a soda soap ; or if potassium
carbonate be added to a soda soap or sodium carbonate to a
potash soap. In certain of these cases it is well known that
double decomposition ensues ; thus, if a potash soap be made by
PEARLASHING. 489
boiling fatty matter and wood ash ley together, and sodium
chloride be then used to salt it out of solution, the resulting curd
is largely composed of soda soap formed by the reaction (in the
case of stearate).
Sodium Chloride. Potassium Stearate. Sodium Stearate. Potassium .Chloride.
NaCl + K.O.C18H350 = Na . 0 . Ci8H350 + KC1
In former days this reaction was utilised to prepare hard soaps in
places where wood ashes only were obtainable as alkali (p. 473).
Similarly, it has long been a practice to improve the softness
and texture of soda soaps intended for toilet soapmaking by
remelting and " pearlashing " — i.e., adding to the melted soap
potassium carbonate dissolved in a little water ; the rationale of
which has been shown to be * that double decomposition takes
place with formation • of potash soap and sodium carbonate,
thus —
Sodium Stearate. Potassium Carbonate. Potassium Stearate. Sodium Carbonate.
2Na.O.C18H350 + K2C03 2K.O.C18H35O + Na2C03
The presence of the potash soap makes the resulting mass less
liable to crack during stamping, and also gives it better lathering
qualities.
In these and all similar cases the general principle involved
seems to be this. Potassium and sodium are so related that when
both alkalies are simultaneously in presence of two acids, one
weaker than the other, the potash tends to unite with the
stronger acid and the soda with the other. Thus when stearic
and hydrochloric acids are in question, the prevailing tendency is
to form potassium chloride and sodium stearate, because hydro-
chloric acid is the stronger acid of the two; whilst when stearic
and carbonic acids are the two acids, the chief tendency is to
form potassium stearate and sodium carbonate, because stearic
acid is a stronger acid than carbonic acid. As in most analogous
cases, however, the question of relative masses is also concerned
in the result ; if these be suitably chosen the actions may to
some extent be reversed — e.g., if a large mass of potassium
chloride act on a relatively small quantity of sodium stearate, a.
notable amount of soft potassium stearate is formed with a
corresponding quantity of sodium chloride, in opposition to the
above described actions occurring when the masses of potassium
and sodium salts are not widely different. Similarly, if a
relatively large amount of sodium carbonate acts on a small
quantity of fused potash soap, a measurable amount of soda
soap and a corresponding quantity of potassium carbonate are
produced, notwithstanding the usual tendency to the opposite
* Alder Wright and Thompson, Journ. Soc. Chem. Ind., 1885, p. 625.
490
OILS, FATS, WAXES, ETC.
change. Thus the following figures were obtained by Alder
Wright and Thompson (loc. cit. supra) : —
(<j) Soda Soaps fused with
KoCO3. Percentage of total
Fatty Acids present
(b) Potash Soaps fused with
Na2CO3. Percentage of
totat Fatty Acids present
Fatty Acids Employed.
Equivalent to
the K2C03
Actually con-
verted into
Equivalent to
the Na2(J03
Actually con-
verted into
added.
Potash Soup.
added.
Soda Soap.
Stearic and oleic (tallow),
10-4
8-0
53
45-7
34-4 !
...
33 55
100-0
97-95
100-0
4-3
104-2
99-0
1000-0
15-0
Stearic, palmitic, and
oleic (palm oil and tal-
57-2
52-1
low), ....
5 5 3»
108-0
90-8
177-0
9-5
Crude Jauric acid (coker- \
nut oil), . . . J
52-8
464
55 55
114-8
87-9
197-0
6-2
Crude ricinoleic acid (cas-
50-0
48-4
tor oil),
53 33
100-0
93-8
2050
8-2
Obviously the proportion of potassium carbonate converted
into potash soap in the series (a) is uniformly much larger than
the fraction of sodium carbonate converted into sodium soap in
series (b) — i.e., not far from the maximum possible in the first case,
and only a few per cents, in the second ; showing the much
stronger tendency towards the first change than towards its
converse.
In similar fashion the following figures were obtained on
salting out potash soaps with sodium chloride, and soda soaps
with potassium chloride ; in series (a) m molecules of water were
used to dissolve 1 of potash soap, and n molecules of sodium
chloride added ; in series (b) m molecules of water were added for
1 of soda soap, and n molecules of potassium chloride added : —
Fatty Acid Used.
m.
n.
(a) Potash Soaps salted
out with NaCl. Per-
centage of Fatty Acid
in Curd.
(b) Soda Soaps salted
out with KC1. Per-
centage of Fatty Acid
in Curd.
As Potash
Soap.
As Soda
Soap.
As Potash
Soap.
As Soda
Soap.
Stearic and oleic acids
(tallow),
Stearic and oleic acids
(tallow),
Stearic, palmitic, and oleic
acids (palm oil & tallow) ,
Crude lauric acid (coker-
nut oil),
100
200
200
200
5
20
20
20
10-5
5-1
3-8
5-4
89-5
94-9
96-2
94-6
79-1
82-1
95-8
74-8
20-9
17-9
4-2
25-2
SALTING OUT.
491
Here the disproportion between the results in the (a] series and
those in the (b) series is much less than in the case of carbonates,
although it is still obvious that on the whole there is a greater
tendency for sodium chloride to form a soda soap by acting on a
potash soap, than for the converse reaction to occur.
The same result follows if a mixture of equivalent quantities
of potash and soda soaps (obtained by halving the fatty acid, and
neutralising one half with one alkali, and the other with the
other) be dissolved in water and salted out with a mixture of
equivalent quantities of potassium and sodium chlorides ; a much
larger proportion of soda soap is thus separated than is equiva-
lent to the potash soap simultaneously thrown out of solution,
the precise proportion varying with the nature of the fatty acids.
Thus the following figures were obtained, indicating from 1'6 to
5 '7 molecules of soda soap to 1 of potash soap: —
-
Percentage of Fatty Acid contained.
Molecular Ratio of
Soda Soap to
As Potash Soap.
As Soda Soap.
Potash soap.
Pure oleic acid, .
38-0
62-0
1-63 to 1
Crude ricinoleic acid (from
castor oil),
17-8
82-2
4-6 to 1
Stearic, oleic, and rosin acids
mixed (primrose soap), .
17-2
82-8
4-8 to 1
Crude lauric acid ( from
cokernut oil soap), .
15-1
85-9
5-7 to 1
It is remarkable that when only one acid is present, or a
mixture of organic acids not greatly differing in strength, the
proportion of soda and potash soaps formed by acting on a mixture
of the two bases is sensibly the same as the proportion of the
bases ; thus with equal molecular quantities of potash and soda,
and amounts of acid exactly equivalent to either of the alkalies
separately, or to one-half of the two jointly, the following figures
were obtained : —
Fatty Acids Employed.
Percentage of Total Fatty Acid
converted into
Soda Soap.
Potash Soap.
51-2
50-8
51-5
48-2
49-7
48-8
49-2
48-5
51-8
50-3
,, oleic acid, .....
Crude stearic and oleic acids (tallow), .
,, stearic, palmitic, and oleic acids )
(palm oil and tallow), . . f
,, lauric acid (cokernut oil), .
Mean,
50-3
49-7
492 OILS, FATS, WAXES, ETC.
In similar fashion, if a soda soap be melted and well inter-
mixed with just as much caustic potash as is chemically
equivalent to the soda present, or if a potash soap be similarly
treated with the equivalent amount of caustic soda, the result in
either case is the formation of a mixture of potash and soda soaps
in practically equivalent quantities.
ANALYSIS OF SOAPS.
The general composition and character of soaps of different
kinds being subject to considerable variation, the analytical
determinations most useful in certain cases are not always those
most valuable in other instances. Thus in the case of a fulling or
woolscouring soap, freedom from excess of alkali or from alkaline
salts (silicate, £c.) that might act injuriously on the wool fibre is
the most important point, together with the proper nature of the
fatty matters employed ; whilst in the case of a laundry soap,
freedom from excess of alkali is not at all an important condition,
the presence of certain kinds of alkaline material (more especially
alkaline carbonates) being generally beneficial rather than other-
wise, cceteris paribus. In all cases, however, a highly important
consideration is the proportion of actual soap present— i.e., the
proportion of the alkaline salts of fatty and resinous acids, apart
from other saline matters, uncombined alkalies, unsaponified
glycerides, water, glycerol, and substances added to give weight,
or to increase the stiffness, or the detergent action, or for other
reasons. An examination of the fatty acids set free on decom-
position with a mineral acid is often useful, as giving information
as to the nature and quality of the fatty matters originally
employed ; the first results being corrected, when necessary, by
determining the amount of unsaponified fat present, and also the
amount and general nature of unsaponifiable constituents, such
as cholesterol, hydrocarbons, &c. Moreover, with certain kinds
of medicated and disinfectant soaps the amount of active
ingredient incorporated therein requires determination.
When the amount of total alkaline matter present (soda,
or potash, or both) is known, expressed as anhydrous oxide
(Na.,O, or K2O) and also that portion which is " free " — i.e., not
combined with fatty and resinous acids, the difference obviously
represents the combined alkali contained as actual soap : i.e., if
the percentage of "total alkali" (expressed as Na20) be a, and
that of "free alkali = b, a - b is the percentage of "combined
alkali." Similarly if c be the percentage of crude fatty acids, &c.,
obtained on decomposition with a mineral acid, whilst d is the
percentage of unsaponified grease and unsaponifiable matters
present therein admixed with the pure fatty acids, c - d is the
percentage of fatty acids contained combined as soap. The
ANALYSIS OF SOAPS. 493
weight of actual soap present then is a - b + (c - d) - n per cent.,
where n is the amount to be subtracted in order to calculate
fatty acids into fatty anhydrides (the soap being viewed for
present purposes as made up of compounds of metallic oxides
and the anhydrides of acids, such as Na20, (C]8H35O).2O for
sodium stearate, and so on). Obviously, if the alkali be expressed
9
as Na.,O, n = ^ (a - b) ; whilst if it be expressed as K0O,
ol
Q
n = (a-b); so that in the first case the percentage of actual
soap is —
• -» + (c-d)- -Ji(a-b) = ~(o-6) + (c-d)
and in the second case —
Q 38 •!
a-b + (c-d)-~(a-b) = ^-(a-b) + (c-d)
For instance, suppose that a soda soap gave the following
results on analysis —
Crude mixture of fatty acids, &c., = c = 67 '05 per cent.
Unsaponifiable matters, &c., . = rf - 1*80 „
Fatty acids present in soap, . = c-d — 65 '24 „
Total alkali (expressed as Na20), = a = 8' 55
Free alkali ,, = b = 0'85 ,,
Combined alkali present in soap, = a-b = 7 '70 ,,
Hence— n = ~ - x 7 "70 = 2 -23
ol
Whence the fatty anhydrides are 65'25 - 2'23 = 03 -02
And the actual soap present = 63 '02 + 7 '70 = 70 '72
The analysis would then be stated thus —
Fatty anhydrides, . . 63 '02 per cent. "I Jointly = 7072 per cent, of
Combined alkali (Na20), . 7'70 ,, J actual soap.
Unsaponifiable matters, &c., 1*80 ,,
Water, free alkali, saline ) /Containing free alkali equi-
matters, &c. (by differ- > 27 '48 ,, I valent to °'85 Per cent-
ence)' • • • ) ) Na20, or ~| = about ? of
\
100-00 V the combined alkali.
In order, therefore, to determine the percentage of actual soap
present, the four quantities a, b, c, and d must be determined ;
during the course of which analysis, the separate percentages of
potash and soda may conveniently be also determined (when the
two alkalies are simultaneously present) ; moreover, whilst c and d
494 OILS, FATS, WAXES, ETC.
are being separated from one another, the respective amounts of
unsaponified glycerides and of unsaponifiable matters present in d
may be conveniently determined, and further examinations made
as to the characters of the separated and purified fatty acids, c — d,
and of the unsaponifiable matters ; in particular the proportion of
rosin acids in the former may be determined, as also the melting
point, &c., so as to obtain information as to the probable nature of
the fatty matters used. This last point, however, is one where
analytical data, as such, often fail to give satisfactory results — i.e.,
the inspection of the mixed fatty acids and the valuation of their
fusing points, &c., often leads to nothing definite ; in some cases,
however, the application of other tests (qualitative or quantita-
tive) leads to useful results — e.g., the elaidin test, &c.
The average molecular weight, E, of the fatty acids contained
in the soap is frequently a datum of considerable value ; this is
readily deduced when a, b, c, and d are known, as shown on
p. 172, being given by the equation —
E = x 31, when the alkali is expressed as Na<>0
a- 6
B=~-|-x47'l „ „ „ K20
Thus, in the above example, the value of E is —
^^> x 31 =263.
7'7u
"When required, the proportion of water present in the soap may
be directly determined, as also any other constituents present,
such, for example, as admixed weighting substances of mineral
or organic nature (china clay, steatite, starch, sand, bran, <fec.);
saline matters (sodium chloride, sulphate, <fec.) ; silica (from
sodium silicate) ; glycerol • sugar ; and so on.
In order to carry out a complete detailed analysis the follow-
ing methods of procedure have been found convenient by the
author,* the exact selection to be made varying with circum-
stances.
Water. — A convenient weight of an average sample of the
soap cut up into thin shavings is dried, first at a temperature
somewhat below 100° so as to avoid fusion, finally at 110°-120°.
The loss of weight may be taken as water, especially when other
volatile substances (carbolic acid, essential oils, <kc.) are absent
* Various more or less similar methods and processes have been pre-
viously put forward by other chemists — e.g., C. Hope, Chemical News,
xliii. (1881), p. 219; Filsinger, Chemiker Zeituny, April, 1884; Allen, Com-
mercial Organic Analysis, Second Edition, vol. ii., p. 251; Leeds, Chemical
News, xlviii. (1885), p. 166; Alder Wright & Thompson, Analyst (1886),
p. 44 ; &c.
WATER, UNSAPONIFIED FAT, ETC. 495
or only present in small quantities. For many purposes this
direct determination is one of the most important valuations,
especially in conjunction with an estimation of free alkali (e.g.,
in the case of soft soap). In other cases the direct determination
is quite unnecessary, more particularly when the amount of
actual soap present is determined, wTater and saline matters being
conveniently taken by difference. Instead of reducing the soap
to thin slices and drying without fusion, the amount of water may
be arrived at by heating 5 or 10 grammes in a large porcelain
crucible set in a sand bath, and stirring with a bit of glass rod
(weighed with the crucible) until no more dew is deposited on
a piece of glass placed over the crucible (the lamp being removed).
"When this stage is reached the water is practically all expelled,
and a nearly constant weight attained. Care must be taken not
to overheat and burn the soap ; the glass rod should have a
rough jagged end to facilitate the breaking up of clots.*
J. A. Wilson recommends t weighing out about 2 -5 grammes
of soap in a dish and dissolving in about 5 c.c. of absolute alcohol
by means of heat ; about 10 grammes of ignited sand are then
added and the whole evaporated to dryness ; the residue is again
treated with 5 c.c. of absolute alcohol and evaporated and finally
dried at 100° to 105° in an airbath. The addition of the sand
facilitates the expulsion of water along with the alcohol, and
renders it more easy to treat the dried soap in a Soxhlet
apparatus for dissolving out unsaponified fat, &c.
Un saponified. Fat, Hydrocarbons, Spermaceti, Wax, &c.—
5 (or preferably 10) grammes of soap are dried, first at 100° or
belowr, and finally at 120° ; or in a crucible, or with alcohol and
sand as above : the residue is exhausted in a Soxhlet tube (p. 238)
with light petroleum spirit ; or a little spirit is poured on, allowed
to digest, poured off (if necessary through a filter), and so on until
all fat, &c., is dissolved out. Ether may also be used, but is more
apt to dissolve out soap. The residue left on evaporation of the
solvent may be examined as to its physical properties, and the
saponifiable portion thereof determined by heating with excess,
of standard alcoholic potash, precisely as in determining the "total
acid number" of an oil or fat (p. 157, et seq.) When saponifica-
tion is complete (which may in some cases require an hour's
boiling with a reflex condenser, or more) the unneutralised
alkali is back-titrated : the exactly neutral fluid is then evapor-
ated and the residue again treated with light petroleum spirit
so as to dissolve out hydrocarbons, cholesterol or other alco-
holiform saponification products, &c., obtained by evaporating
the extract ; whilst the undissolved portion on acidulation and
shaking with ether enables the fatty acids, &c., produced by the
saponification to be isolated for examination. In cases where
* Watson Smith, Journ. Soc. Dyers and Colour ist*, vol. i., p. 31.
t Chemical News, October 21, 1892, p. 200.
496 OILS, FATS, WAXES, ETC.
a full examination of the unsaponified fat, &c., is requisite it is
preferable to employ a larger quantity (50 grammes or even
100) of soap, and not to combine this determination with that of
water, &c., lost by drying. As a rule little but unsaponified
glycerides are thus extracted; but " oleine " soaps often contain
a small percentage of hydrocarbons contained in the oleine
(distilled, p. 278), whilst if woolgrease have been used to adul-
terate tallow, notable amounts of cholesterol, ttc., may be present.
Spermaceti, vaseline, &c.,* may be present in special kinds of
toilet soap ; whilst certain laundry soaps are purposely inter-
mixed with paraffin oil and similar hydrocarbons.
The unsaponified fat, ttc., may also be isolated by dissolving
the soap (which need not be dried) in hot alcohol and somewhat
diluting with water ; before complete cooling a little ether is
dropped in (care being taken that no light is near to inflame
ether vapour), which will generally prevent the mass gelatin-
ising. More ether is added and the whole well agitated, and
if separation does not occur, more water is added, the ethereal
solution being finally drawn off by means of a separating funnel
or Chatta way's tube (p. 120). The ethereal extract thus obtained
usually contains soap, so that it should be evaporated and the
residue dissolved in petroleum spirit and filtered. Some little
.amount of "dodging" is sometimes requisite to get the alcohol,
•ether, and water in the right proportions to bring about a proper
separation into two fluids, one a watery alcoholic soap solution,
the other an ethereal solution of fat, &c.
Fatty Anhydrides and Total Alkali. — The residue de-
prived of fat, &c., by petroleum spirit left in the Soxhlet tube
as above, is dissolved in water f and decomposed by boiling with a
slight excess of standard acid. On standing and cooling the fatty
acids separate as a cake, which is washed, dried, and weighed, J
* When wax is present, toluene dissolves it out in the Soxhlet tube
better than petroleum spirit (Schuaible).
tlf mineral matters, &c., insoluble in alcohol are present, the soap
may be treated (conveniently still in the Soxhlet tube) with alcohol, so as
to dissolve out the soap, and leave the insoluble substances. In this case
drying without addition of sand, &c. , is preferable. The alcoholic extract
may be evaporated to dryness and the residue weighed, so as directly to
determine the "actual soap " present ; or it may be diluted with hot water
and treated with excess of standard acid, &c.
£0r the hot fluids may be washed into a separating funnel, the watery
part run off, and the fluid fatty acids washed out on to a wet filter as in
determining the Hehner number of an oil, &c. (p. 166). If particles of
fatty acid adhere to the vessels either in this mode of operating or with
the solid cake, they should be washed off with a little ether, &c., into a
small beaker or basin, and the solvent evaporated, the rest of the fatty
acids being subsequently added, and the whole weighed together after
drying. When the soap contains any considerable amount of soluble fatty
acids (e.g., when made from mixtures containing cokernut or palm kernel
oil) these partly remain in the aqueous liquor from which they may be
mostly extracted by shaking with ether.
FATTY ANHYDRIDES AND TOTAL ALKALI. 497
and then subjected to such further tests as may be deemed
necessary (melting point, elaidin test, &c.), more especially rosin
acid determination (infra). If the fatty acids are very soft, or
are derived from coker or palm kernel oil, a known weight (5 or
10 grammes) of beeswax or paraffin wax may be advantageously
added before cooling so as to form a more solid cake, and to
assist in dissolving out from the water the more soluble acids,
due correction being made for the weight of added substance :
this, however, obviously prevents any physical or other examina-
tion of the fatty acids after their being separated from the soap.
If such an examination is not requisite it often saves time to
weigh up a separate amount of average soap (10 grammes*) and
without drying or treating with petroleum spirit to dissolve this
in water, decompose with acid, and weigh the resulting mixture
of fatty acids, unsaponified fat, &c., correcting the result by
means of a separate determination of the latter quantity. The
corrected percentage of fatty acids is calculated to fatty anhy-
drides as above described (p. 493).
"When nitric acid is used as the standard acid, and the alkali
employed for back-titration f is free from chloride and sulphate,
the neutralised fluid may be divided into two halves for the
determination of sulphate and chloride respectively ; or, if
requisite, a portion may be reserved for glycerol determination
(infra).
From the amount of standard acid used, less that titrated in
the liquid after removal of fatty acids, the total quantity of
alkali present is known, including that present as soap, that
contained as hydroxide or carbonate, and that present as other
inorganic salts of alkaline reaction — e.g., silicate.
* Instead of using 10 grammes of soap, a smaller quantity, say 2 grammes,
may be dissolved in water, acidulated, shaken with ether in a well closed
vessel, and the ethereal solution separated and evaporated ; this method is
preferable with soaps made from cokeriiut and palm kernel oils on account
of the partial solubility of the fatty acids thence derived in water. In
order to avoid loss of volatile acids during drying, the ethereal solution
may be exactly neutralised with alcoholic solution of pure soda, evaporated
to complete dryness, and weighed. By subtracting the Na20 contained
in the alcoholic soda from the weight of the pure soap (together with
unsaponified grease and unsaponinable matters) thus obtained, the weight
of fatty anhydrides + unsaponified grease and imsaponifiable matters is
known. The soda thus neutralised is the "combined alkali" (vide infra,
" fatty acid titration test " for free alkali).
t Cochineal is a convenient indicator for the purpose. If any soluble
organic acids are present in the watery fluid, they may be approximately
estimated by first titrating with methyl orange as indicator, the colour
change occurring when all the mineral acid present is neutralised ; and
then g"ing on with addition of phenolphthalein, which is not reddened till
the organic acids are neutralised. The additional alkali thus consumed
may be calculated as valeric acid, C5H1002, in the case of soaps containing
whale oils ; or as heptoic acid, C7H1402, or octoic acid, CsHje^^, in the case
of cokernut oil soaps.
32
498 OILS, FATS, WAXES, ETC.
Free Alkali. — The term "free alkali" is generally understood
as including the alkalinity of all substances present in soap pos-
sessing an alkaline reaction— i.e., the sum of the alkalinity due
to hydroxide (caustic alkali), carbonate, and other salts such as
silicate ; so that the difference between the " total alkali " and
the "free alkali " exactly represents the alkali combined with
fatty and resinous acids as actual soap.
Excepting with freshly made soap, especially when preserved
in large sized blocks, but little caustic alkali is ever found in
commercial soap, because the absorption of carbon dioxide from
the air is tolerably rapid ; but the passage of that gas into the
interior of a large mass, and to a lesser extent into the centre of
an ordinary bar, is by no means instantaneous, so that the
interior portion of a comparatively freshly made curd or hydrated
soap (pp. 461, 470) often contains a notable amount of hydroxide.
In order to distinguish the free alkali present as hydroxide from
that contained in other forms, C. PI ope * dissolves a known
weight of an average sample in strong alcohol and filters ; car-
bonate, silicate, &c., are left on the filter ; 'whilst caustic alkali
(whether potash or soda) passes through, dissolved in the alcohol
along with the neutral soap. The operation may be conveniently
carried out thus, constituting the "alcohol test" for free alkali.
5 grammes of undried average sample of soap are dissolved in
hot alcohol (free from all acidity or alkalinity, and as strong as
possible) and the solution filtered through a hot water funnel :
after completely washing out with alcohol, the undissolved
residue is treated with water and the alkalinity determined.
As a general rule, the alcoholic filtrate is neutral, but sometimes
it is faintly acid to phenolphthalein ; apparently with a slightly
moist soap mass, absorption of carbonic acid from the air tends
to develop a trace of "acid soap" (pp. 23, 486) with a correspond-
ing quantity of alkaline carbonate; as this latter is undissolved
by the alcohol it does not react on the acid soap during solu-
tion so as to neutralise it again, f In such a case the acidity
(" negative alkalinity ") of the alcoholic solution is determined,
and the amount subtracted from the positive alkalinity of the
residue. Thus 5 grammes of soap gave an alcoholic solution
where the acidity represented 0'25 c.c. of seminormal alkali;
whilst the residue neutralised 0'6 c.c. of seminormal acid : hence
the "free alkali" is reckoned as O6 - O25 = 0-35 c.c. of semi-
normal acid corresponding with 0-0054 gramme of soda (Na2O)
or 0-108 per cent.
Sometimes, on the other hand, the alcoholic filtrate is more or
* Chemical News, xliii. (1881), p. 219.
t With some kinds of soap, if a stream of pure carbon dioxide be passed
through a hot clear filtered alcoholic solution of the soap, a slight visible
precipitation of alkaline carbonate results, together with the formation of an
equivalent amount of "acid soap."
FREE ALKALI. ,499
less alkaline (through the presence of hydroxide in the soap) ;
in which case the amount of alkali present in the nitrate is
determined (using phenolphthalein as indicator) and added to
that found in the residue, this method of operating being
" Hope's test " in its original form. It has been pointed out by
J. A. Wilson * that when caustic alkali is present in a soap
which also contains unsaponified glycerides, the alcoholic alkaline
solution is apt to act on these glycerides, diminishing the alka-
linity by saponifying them, and so causing the amount of free
alkali to be understated. The author has found that this
source of error is readily avoided by cutting the soap to be
examined into very thin slices or shavings, and exposing these
loosely piled together in a small dish or beaker to the action of
carbon dioxide, conveniently by placing the dish in a wide
mouthed bottle filled with the gas, loosely corking it, and leaving
the whole till next day. By that time all caustic alkali is car-
bonated, so that the alcohol test can be applied without any
error due to saponification of glycerides, due correction being
made, if requisite, for the " negative alkalinity " of the alcoholic
nitrate caused by the action of the carbon dioxide forming small
quantities of acid soap and alkaline carbonate. This mode of
operating, however, obviously does not enable the relative amount
of alkali to be distinguished present as hydroxide and carbonate,
&c., respectively.
In the case of strongly alkaline soaps where a slight
amount of error in determining the total amount of free alkali
is not material, two other tests are applicable, respectively desig-
nated the " fatty acid titration test " and the " salting out test/'f
The first of these consists in determining the total alkali as
above, separating the fatty acids, and titrating them, reckoning
the difference as free alkali. In practice the unavoidable experi-
mental error of this differential method is sometimes found to be
sufficiently great to render the determination of minute quantities
of free alkali decidedly uncertain, so that for nearly neutral soaps
the method is useless. Moreover, the fatty acids separated by
the action of dilute aqueous acid on soap are sometimes partly
soluble in water, so that although the insoluble acids largely
dissolve the soluble ones and bring them out of solution in water
into the supernatant layer of fused fatty acids (as ether would
dissolve out similar matters from watery solution), still a small
proportion of the soluble acids are apt to be retained by the
water and lost, thus tending to increase unduly the value of the
free alkali determination ; this is especially noticeable when
cokernut or palm kernel oil has been employed in making the
soap. When, however, the free alkali is large, so that a small
* Chemical News, lix. (1889), p. 280.
t Alder Wright and Thompson, Journ. Soc. Chem. Ind., 1885, p. 625.
500
OILS, FATS, WAXES, ETC.
degree of possible error in its determination is not of great
importance, this method is very convenient.
The " salting out test " is worked by dissolving a weighed
quantity of soap in hot water, adding salt so as to throw the curd
out of solution, filtering off, and titrating the alkali in the filtrate.
This may be conveniently done in two fractions, one titrated
directly so as to obtain the total alkali present (caustic -f- car-
bonated) ; the other treated with barium chloride in excess, and
the caustic alkali determined present in the filtrate from the
barium carbonate, &c., thus precipitated (vide p. 420, footnote).
Apart from error in deficiency of the caustic alkali value
thus deduced due to unavoidable absorption of carbon dioxide
from the air during the operations, a source of error in excess is
that hydrolysis of the soap examined necessarily takes place to
an extent variable with the temperature, the quantity of water
present relatively to the soap, the nature of the fatty acids
present, and the amount of free alkali. When, however, a
uniform mode of manipulating is adhered to, the results got
with a given kind of soap are comparable .amongst themselves,
so that the figures obtained are often of considerable practical
use, especially when corrected (by means of carefully made tests
using the alcohol process) so as to get an approximate valuation
of the excess of alkali due to the hydrolytic action. For instance,
the following figures represent the difference in amount of free
alkali found with a variety of soaps according as the alcohol
test (A.T.) or salting out test (S.O.T.) was used : the numbers
are reckoned per 100 parts of alkali combined with fatty acids as
soap — i.e., if the combined alkali = lO'O and the free alkali =
0-52 per 100 of soap, this would correspond with 5-2 parts of
free alkali per 100 of combined alkali : —
Nature of Soap Used.
A.T.
S.O.T.
Excess of S.O.T.
over A.T.
Pure cokernut oil soap, not strongly \
alkaline, . . . . . /
5-0
9-1
4-1
Another sample of ditto, .
2-8
58
3-0
A British toilet soap, largely made 1
from cokernut oil, . . . . /
1-3
5-8
4-5
A foreign toilet soap, largely madel
from cokernut oil (neutral), . . /
0
3-5
3 '5
A high-class American toilet soap,
1-8
54
3-6
A toilet soap largely made from lard \
(neutral), . . . . . /
0
3-2
3-2
A second-class ditto, chiefly made from )
i -q
4*8
0-0
tallow, i
J. *J
Tt O
— *7
A cotton seed oil soap,
7'2
9-8
2-6
A tallow rosin (primrose), .
1-1
3-0
19
A neutral castor oil soap, .
0
1-7
1-7
A bleached palm oil soap, .
50
6-4
1-4
A tolerably alkaline curd soap, . j
Pure stearic acid soda soap (neutral),
18-3
0
18-3
07
0
0-7
ROSIN ACIDS. 501
When the watery soap solution is tolerably concentrated (about
1 part by weight of actual anhydrous soap to 10 of water), and
the soap itself contains a good deal of free alkali, the error due
to hydrolysis becomes small enough to be quite negligible ; but
with a nearly neutral soap the hydrolytic error becomes several
times as large as the free alkali actually present.
Potash and Soda. — When both alkalies are present, and it
is required to determine their relative amount, several methods
of operating are available. One of the simplest is to decompose
a known quantity of soap with dilute hydrochloric acid, evaporate
down the watery nitrate, convert potassium chloride into platino-
ehloride, and weigh this. In the absence of more than minute
quantities of sulphate, silicate, &c., the mixed alkaline chloride
solution may be evaporated down and weighed, the chlorine
contained determined (volumetrically or otherwise), and the ratio
of potassium to sodium calculated from the indirect results.
The soap may also conveniently be charred and the alkalies
dissolved out from the ash for treatment. When much sulphate
is present the alkalies should be weighed as sulphates and the
indirect determination made by determining the barium sulphate
yielded by the mixture.
Rosin Acids. — It is often of considerable importance to deter-
mine with some degree of approximate accuracy the proportion
between the rosin acids and the ordinary fatty acids present in a
given sample of soap. Several older methods have been pro-
posed, none of which yield very accurate results j but more
recently two processes have been introduced of a somewhat more
satisfactory nature, although still leaving a good deal to be
desired. The earlier of these is that of Gladding * based upon
much the same principle as the ordinary separation of oleic and
stearic acids, viz., conversion into metallic salts, one soluble in
ether, the other insoluble. The soap- to be tested is freed from
unsaponified fat, &c., by treatment with petroleum spirit ; or if
glycerides only are present by heating with strong alcohol and a
few drops of alcoholic potash in excess of the neutralising amount
to effect complete saponification. The alcoholic soap solution is
then agitated with powdered neutral silver nitrate and ether in
a closed vessel for some time (0'5 grm. fatty acid, 1 grm. silver
nitrate, and 100 c.c. of ethereal fluid altogether, answer well) :
after some minutes shaking flocculent silver stearate, &c., sub-
sides, whilst silver resinate remains dissolved. A known fraction
of the ether is siphoned off or removed by a " Chattaway tube "
(p. 120) and agitated with dilute hydrochloric acid, whereby the
silver is removed and an ethereal solution of rosin acids produced,
by evaporating which the rosin acids are obtained in weighable
form. Finally, a correction is made for the solubility of silver
* Chemical Fews, xlv. (1882), p. 159.
502
OILS, FATS, WAXES, ETC.
oleate, &c., amounting to a subtraction from the weight of rosin
acids obtained of 23'5 milligrammes per 100 c.c. of ether.
A notable source of error in this method lies in the uncertainty
of this correction, inasmuch as somewhat widely different values
are found with different acids — e.g.*
Nature of Fatty Matters in Soap
Examined.
Fatty Matters Dissolved (as Silver Salt) in
100 c.c. of Alcoholic Ether.
Maximum.
Minimum.
General Average.
Milligrammes.
Milligrammes.
Milligrammes.
Pure stearic acid,
16-0
8-0
11-6
,, oleic ,, . 15'0
9-0
12-0
Nearly pure palmitic acid, 30 '0
2SO
29-1
Cotton seed oil, . . 34'0
20-0
26-9
Castor oil, ... 62 "0
49-0
53-9
Cokernut oil (fatty acids dried
on water bath), . . 17*5
12-0
14-8
Cokernut oil (fatty acids dried '
over H2S04), ... 23 '0
19-0
21-1
Stearic and oleic acids, in
nearly equal proportions, 22 '0
Stearic acid and cotton seed oil,
IS'O J9-1
in nearly equal proportions,
...
...
25-5
Oleic acid and cottonseed oil,
in nearly equal proportions,
...
24-5
Stearic acid and cokernut oil
(water bath), in nearly equal
proportions,
...
23-4
Oleic acid aud cokernut oil
(water bath), in nearly
equal proportions, .
...
...
25-6
According to the nature of the fatty acids, the correction may
thus vary between 8 and 62 milligrammes in the most extreme
cases, and between 11 '6 and 53*9 for average values, these
quantities representing on 500 milligrammes of fatty acids
respectively 2-3 and 10 -8 per cent. ; so that whilst 2 3 -5 milli-
grammes ( - 4*7 per cent.) is not far from a mean value, it is by
no means equally applicable in all cases, f
* Alder Wright and Thompson, Proceedings of the Chemical Society, 1886,
p. 175 ; also Chemical News, vol. liii. (1886), p. 165.
t Lewkowitsch has subsequently found still wider discrepancies between
the corrections necessary in the case of stearic and oleic acids — e.g.,
Correction per TOO c.c. of Alcoholic Ether.
Oleic acid, . . . 109*0 to 109 '4 milligrammes.
Stearic acid, . . . 5 "4 to 5 '8 ,,
(Journ. Soc. Chem. Ind., 1893, p. 503.)
Hubl and Stadler modify Gladding's process by precipitating the mixed
silver salts from the largely diluted soap solution by means of aqueous
silver nitrate, drying, and dissolving out silver resinate with ether in a
Soxhlet tube (p. 238). Grittner and Szilazi add alcoholic calcium nitrate
solution to the alcoholic soap solution to be tested, so as to remove most of
TWITCHELL'S METHOD. 503
E. Twitchell's method * depends on the property of ordinary
fatty acids to form compound ethers when dissolved in alcohol
and treated with hydrochloric acid gas ; if the alcohol be absolute
and the solution saturated with the gas, the conversion is stated
to be complete with fatty acids, whereas rosin acids are not acted
upon at all ; with alcohol of only 90 per cent., however, the
action is not complete, several per cents, of the fatty acids
escaping conversion. 2 or 3 grammes of mixed acids are dissolved
in 10 volumes of absolute alcohol, and dry hydrochloric acid
gas passed through for 45 minutes, the vessel being cooled
by immersion in water ; by and bye the fatty ethers separate,
floating on the surface. After standing half an hour the mixture
is diluted with five times its volume of water and boiled till clear,
the ethers and rosin acids floating on the top; the whole is shaken
with about 50 c.c. of light petroleum spirit; after separation, the
hydrocarbon solution is washed by shaking with water, and
finally shaken with 5 c.c. alcohol and 50 of water containing 0-5
gramme of caustic potash. The alkali dissolves out the rosin
acids from the hydrocarbon, leaving the fatty ether still dissolved
therein ; on separation of the aqueous solution of resinate, and
agitation with ether or petroleum spirit after acidulation, the
rosin acids are obtained in solution, and may either be weighed
(after evaporation to dryness) or titrated, assuming some par-
ticular value for their mean equivalent.! If glycerides are
the stearate, palmitate, and oleate present by precipitation ; the filtrate is
then treated with silver nitrate and ether as in Cladding's process.
According to Lewkowitsch (loc, cit. supra] neither modification gives satis-
factory results, the quantity of rosin found being generally below that
actually present when soap made from known mixtures of fatty matters
and rosin are examined as test samples. On the other hand, the figures
obtained by means of Gladding's original process are generally several per
cents, too high, even when the correction to be used has been separately
determined for the particular fatty acids, &c., used for the test samples
employed.
* Analyst, 1891, p. 169; also Journ. Soc. Chem. Industry, 1891, p. 804,
from Journ. Anal, and Applied CTiem., vol. v., p. 379.
t Test experiments made by E. Twitchell showed that when the value
346, found as the mean equivalent weight of a sample of colophony, was
used to calculate the result of titration of the rosin acids isolated from
known mixtures of that colophony and fatty acids, the titration values
always came out higher than those got by weighing ; thus —
Volumetric. Gravimetric.
21-40
20-36
19-91
Average 20 "56 18 '93
Hence apparently one or two per cents, of constituents were present,
not of acid nature, and, consequently, not dissolved by the caustic potash
and, therefore, not ultimately weighed along with the true rosin acids.
Such constituents would be weighed along with the rosin acids isolated
504 OILS, FATS, WAXES, ETC.
present in the fatty acid mixture, this does not in any way
invalidate the rosin determination, as the glycerides are not
dissolved out by the alkaline liquor along with the rosin acids.
Silicate of Soda. — The substance left undissolved by alcohol in
the determination of free alkali by the "alcohol test" (supra), after
treatment of water and nitration, may be titrated for alkalinity
and then evaporated to dryness with a slight excess of hydro-
chloric acid ; the silicon dioxide formed in the event of silicate
being present in the soap, is then left undissolved on treatment
of the residue with water. Or a known weight of soap may be
charred, and the ashes supersaturated with hydrochloric acid and
thoroughly dried, so that silica and carbon are left undissolved
by water, the latter being ultimately burnt off.
Starch, China Clay, Steatite, Pigments, &c.— Substances
of this description other than colouring matters are not often
found in soaps, but are occasionally added, especially to certain
varieties of fancy soap — e.g., "oatmeal" soap, certain socalled
"milk" soaps, and the like. The residue from the previous
examination for silicate and carbonate, &c., left undissolved by
water on treating the matters insoluble in alcohol therewith
consists of these substances. Ultramarine, chrome green, ver-
milion and similar pigments are sought after by the appropriate
tests suggested by the colour; starchy matters by means of
iodine ; mineral constituents generally by incineration ; and so on.
The presence of such substances as oatmeal, farina, &c., sometimes
renders it necessary to modify slightly the method for deter-
mining fatty acids above described, where the cake of fatty acids
obtained is weighed, as it may contain some of these matters
mechanically intermixed ; to separate them the cake is dissolved
in ether, benzene, &c., and filtered; the residue is well washed
and the nitrate evaporated to dryness.
Glycerol and Sugar.— When glycerol is contained (as in
the case of soft soaps, cold process soaps, hydrated soaps, &c.) it
may be determined, with a fair degree of accuracy, in a variety
by Gladding's process. Lewkowitsch finds (Journ. Soc. Chem. Ind., 1893,
p. 505) that the mean equivalent* of different samples of commercial rosin
varies within somewhat wide limits ; thus, with six samples of American
rosin values were found varying between 340 '8 and 364, with an average of
348 "3. Hence, the percentage of rosin found by titration can only be
regarded as a somewhat rough approximation. On the other hand,
Twitchell's process, applied to pure stearic acid and other fatty acids and
mixtures free from rosin, indicated from 1'07 to 3'67 per cent, of that
substance, the products obtained being weighed ; whence it would seem that
the quantity of rosin apparently found in a given sample of soap by Twitchell's
process would be too high, and that a correction should be made to allow
for this source of error (probably incomplete conversion of fatty acids-
into compound ethers, or subsequent decomposition of compound ethers)
In practice, however, the quantity of rosin actually found is generally
somewhat beloiv that known to be present when test samples of known
composition are examined.
GLYCEROL AND SUGAR. 505
of ways in the absence of sugar ; but in presence of sugar its
accurate determination is not easy. If sugar be not present, one
of the simplest methods of procedure is to decompose the soap
with a slight excess of sulphuric acid, and after separating the
fatty acids to render neutral or slightly alkaline with sodium
carbonate, evaporate to dryness, and dissolve out the glycerol
from the sodium sulphate, &c., by absolute alcohol : the residue
left on evaporating off the alcohol may be weighed, and any
inorganic matters present determined by incineration and sub-
tracted. The crude glycerol may, preferably, be purified as
described on p. 523; or it may be converted into acetin by
acetic anhydride (pp. 186, 516); or if sufficiently free from other
organic substances it may be determined by the dichromate
process (p. 522), or oxidised to oxalate (p. 519). A little gly-
cerol is volatilised during the latter part of the evaporation ;
hence when either of these two latter methods is employed,
instead of evaporating the aqueous solution to complete dryness,
it may preferably be only partially concentrated. Muter's method
consists in treating with copper sulphate and caustic soda, the
copper kept in solution being determined colorimetrically or by
potassium cyanide (p. 523), parallel observations being made
with liquids treated in just the same way after addition of known
quantities of glycerol solution from a burette, so as to afford the
means of calculating the glycerol present from the amount of
copper kept in solution. In general the glycerol may be thus
estimated conveniently in the watery fluid left after determining
total alkali and fatty acids (supra). When sugar is present this
is inverted by heating with dilute hydrochloric or sulphuric
acid ; the liquid is then rendered alkaline and copper sulphate
added in excess, and the sugar deduced from the amount of pre-
cipitated cuprous oxide ; the alkaline liquid containing glycerol
and the products of the oxidation of the sugar may be tested for
glycerol by determining the amount of dissolved copper as before,
checking the results by means of similar tests with liquids con-
taining known quantities of sugar + glycerol; the results,
however, are apt to be only approximate even with the greatest
care. Instead of determining sugar by the copper reduction pro-
cess the polariscope may be employed. Knowing the amount of
sugar present and the specific gravity, the proportion of glycerol
present may be approximately calculated in the case of a liquid
containing no other substances in solution.
Volatile Substances other than Water. — Sometimes a
transparent soap contains alcohol, the proportion of which is
desired to be known ; other volatile constituents are sometimes
present in other kinds of soap — e.g., carbolic acid, thymol,
camphor, &c. In such cases special methods must usually be
resorted to to determine the volatile substance, dependent on its
nature. Alcohol, if in quantities above inconsiderable traces, may
506 OILS, FATS, WAXES, ETC.
be determined by dissolving in water a sufficient quantity of
soap, adding salt, filtering off say one half of the total fluid, and
distilling until about half has passed over; this distillate is simi-
larly redistilled, and ultimately the quantity of alcohol inferred
either from the specific gravity of the final distillate, or by
oxidising with chromic acid, ifec. The following method of
determining phenoloids is recommended by A. H. Allen * : —
5 grammes of soap are dissolved in hot water, 20 to 30 c.c. of a
10 per cent, solution of caustic soda added, and the whole cooled
and agitated with ether to dissolve hydrocarbons. The alkaline
liquor is separated and treated with excess of strong brine ;
fatty acid soaps are precipitated, but sodium phenolate and
cresylate, etc., remain in solution ; the liquid is filtered and
the precipitate washed with brine, and the nitrate and washings
diluted to a litre. 100 c.c. of the solution (representing 0'5
gramme of soap) are acidulated with sulphuric acid, and the
solution (clear if fatty acids have been thoroughly removed)
titrated with bromine water standardised by means of carbolic
iicid (or cresylic, &c. ), operating in the same way ; when enough
bromine has been added to cause all the phenoloids to become
converted into tribromo derivatives, the yellow tint due to excess
of bromine becomes visible. By treating the other 900 c.c. of
solution with sulphuric acid and excess of bromine, and agitating
with successive small quantities of carbon disulphide, the tri-
bromo derivatives may be dissolved out and examined after
evaporation of the solvent. Pure phenol (crystallised " carbolic
acid") gives nearly colourless long needles of tribromophenol,
whereas cresylic acids give deep yellow, orange, or red difficultly
crystallisable or non-crystalline products ; so that the character of
the phenoloids present may be ascertained, as well as the amount.
The following general scheme represents a selection from the
-above processes applicable in most cases : —
Dry 10 grammes of average sample, finally at 120°, and reckon
the loss of weight as water.
Exhaust the residue with light petroleum spirit, and examine
the extract for unsaponified glycerides, hydrocarbons, spermaceti,
wax, cholesterol, &c.
Treat the exhausted residue with water and excess of standard
^nitric) acid ; separate and weigh the fatty acids, and subject
them to such further examination as may be required, more
especially as regards the presence of rosin acids. Back-titrate
the aqueous liquor so as to determine the total alkali, using
alkaline solution free from sulphate and chloride. Determine
sulphate and chloride in the neutralised liquid ; also glycerol and
sugar if present ; and potassium if required.
Treat 5 grammes of average sample with hot strong alcohol, and
titrate acidity or alkalinity of filtered solution : dissolve the
* Commercial Organic Analysis, 2nd edition, vol. ii., p. 255.
CAILLETET'S METHOD. 507
undissolved part in water and titrate for carbonated alkali, &c.,
so as ultimately to deduce the free alkali. Examine the sub-
stances not dissolved by alcohol for silica, clay, starch, pigments,
and similar substances.* If unsaponified glycerides and caustic
alkali be simultaneously present, the latter should be carbonated
before dissolving the soap in alcohol, otherwise a deficiency in
the total " free alkali " will result (supra, p. 499).
An objection to this mode of operation is that if any caustic
alkali be contained in the soap, it becomes more or less carbonated
during the drying, so that an incorrect valuation of caustic alkali
results. When much caustic alkali is present, it may be deter-
mined by the salting out test (supra), adding barium chloride
to convert alkaline carbonate into chloride, and filtering before
titrating (compare p. 500).
Instead of decomposing the soap dissolved with alcohol with
excess of standard acid, and back-titrating after separation of
fatty acids, the alcoholic solution may be rendered neutral to
phenolphthalein, and then directly titrated with a standard
mineral acid solution, using methyl orange as an indicator,
organic fatty acids having no reaction on this substance: per-
fectly sharp results are thus obtainable (Allen).
Cailletet's method of Analysis. t — For determinations where
speed is indispensable but minute accuracy unnecessary, a con-
venient process has been proposed by Cailletet for the determin-
ation of fatty acids and alkali. A tube holding 50 c.c. and
divided into 100 parts is provided, into which are introduced 10 c.c.
of diluted sulphuric acid of known strength (about four times
normal), 20 c.c. of oil of turpentine, and 10 grammes of the soap
in shavings. The tube is closed with a stopper or cork and well
shaken up ; when all the soap is decomposed it is allowed to
stand, and the volume of the turpentine solution of fatty acids
read off. Subtracting the 20 c.c. of turpentine used, the differ-
ence gives the volume of the fatty acids : thus, if the turpentine
solution occupied 50 divisions = 25 c.c., the fatty acids would
represent 25 — 20 = 5 c.c. per 10 grammes of soap. Assuming
the specific gravity of the fatty acids to be n, their weight would
be 5 x n grammes = 50 x n per cent, by weight. The alkali
is obtainable by back-titrating the excess of acid.
Cailletet gives the following values for n in the case of soaps
of different kinds, experimentally determined by noting the
* Instead of weighing up two portions of soap, one portion (preferably of
10 grammes) may be employed for all the determinations, being first dried,
then exhausted with petroleum ether to extract fat, and then treated
(still in the Soxhlet tube) with alcohol to dissolve out soap, glycerol, &c.
The alcoholic extract thus obtained is titrated for acidity or alkalinity,
then largely diluted with hot water and decomposed with standard acid so
as to obtain fatty acids and total alkali ; whilst the residue undissolved by
alcohol is tested for alkali, silicate, sulphate, chloride, starch, pigments, &c.
f Bulletin Soc. Ind., Mulhouse, xxix., p. 8.
508
OILS, FATS, WAXES, ETC.
increment in volume of turpentine oil as above indicated, and
directly determining the percentage by weight of fatty acids in
another portion of the same soap : —
Specific Gravity of Fatty Acids.
Olive oil (Marseilles) soap 0'9188
Cokernut oil soap, ....... 0'9400
Palm oil soap, 0'9220
Tallow soap 0'9714
Oleic acid soap, 0'9003
In the case of rosin soaps, the rosin acids do not readily dis-
solve in the turpentine, 20 c.c. only increasing 0-15 c.c. in volume
by virtue of the rosin acids dissolved, whilst a bulky layer of
undissolved rosin collects below the turpentine.
Calcium Salt Test. — A rough method of arriving at the value
of a given soap is to dissolve in dilute alcohol and determine the
quantity of the solution requisite to be added to a known volume
of a solution of calcium chloride, sulphate, &c., so as to produce
a permanent lather, as in Clark's test for the hardness of water ;
a parallel determination being made with a standard sample of
similar soap of known composition, the ratio between the volumes
of the two soap solutions used gives approximately their relative
detergent value. The soap solutions may be conveniently made
of the strength of 10 grammes per litre ; the lime salt solution
maybe made by dissolving 0'2 gramme of pure calcium carbonate
in dilute hydrochloric acid, evaporating to dry ness on the water
bath to expel excess of acid, dissolving the residue in distilled
water and diluting to a litre ; the solution consequently repre-
sents 20 milligrammes of CaCO3 per 100 c.c. or 14 grains per
gallon (14° of hardness on Clark's scale).
The folio wing analyses represent the composition of a consider-
Best Tal-
low Curd,
London
make.
Bleached
Palm Oil,
London
make.
Marine
Soap, non-
siiicated.
Marine
Soap,
silicated.
Imitation
Castile
Soap,
English.
Fatty anhydrides, .
Combined alkali (Na20),
66-60
7-51
66-20
7-83
32-00
5-20
13-50
2-27
61-45
8-46
Freealkali(includingthat }
present as silicate), . J
•50
•40
2-25
8'36
1-16
Silica (Si02), .
...
10-50
Sodium chloride, .
1-35
2-05
765
5-05
1-17
Sodium sulphate, .
•20
traces
1-45
•35
1-23
Water, carbonic acid, and j
insoluble matters, pig- >
23-84
23-52
51-45
59-97
26-53*
ments, &c., . . . )
100-00
100-00
100-00
100-00
100-00
Percentage of true soap,
74-11
74-03
37-20
15-77
69-91
Mean molecular weight!
of fatty acids, . . /
284
271
200
197
234
Including '74 per cent, of insoluble pigments.
MANUFACTURERS', HOUSEHOLD, AND LAUNDRY SOAPS. 509
able variety of British and colonial manufacturers' and other
scouring and laundry soaps. Where no analyst's name is men-
tioned, the analyses were made by the author.
"Prim-
"Cold
"Cold
Oleic Acid
London
make.
"Ivory,"
Canadian.*
Water,"
English.
Water,"
Canadian.*
Soap,
London
make.
Fatty anhydrides, .
Resinous anhydrides,
| 46-88
\ 15 -40
43-33
25-00
43-70
22-00
45-85
24-00
62-71
Combined alkali (Na20),
7-12
7-72
9-28
8-00
7-36
Sodium carbonate, .
•14
2-64
•58
2-22
•68
,, chloride. .
•14
,, sulphate, .
Water with minute quan-
•07
21-31
24-44
1993
29-25
tities of insoluble mat-
on n-
ters, lime, ferric oxide,
&r>
100-00
100-00
100-00
100-00
100-00
Percentage of true soap,
69-40
76-05
7498
72-07
70-07
Free alkali (NTa20),
•08
1-54
•34
1-30
•40
Mean molecular weight \
of fatty acids, &c. , . /
280
283
230
280
273
MANUFACTURERS' SOAPS (C. Hope).
§
;_r~
;_.
|
*..s
, i
ti &Tii
c'O
o"
d -to
^3^'--> 0!
so
•jjsjOd
fr
^o «
•2 § S «
§S
^^"c°
^0
O
•e— 2
s ^ofe £
f^ 2
•e -ei'S
*s s*»
-^ Cl^*
2^ fifc^^
3 .
3 C? fl 02
£^d
Q
•— pq ^
?"3
g
?
S«i5
^ld
?!
Fatty anhydrides and rosin,
71-30
62-66
59-28
38-89
19-42
60-90
Soda (Na20), combined as soap,
Free alkali (Na2O), including
7-98
7-27
6-65
5-76
3-11
7-22 i
carbonate and silicate,
1-23
•80
•40
2-91
698
•10
Sodium chloride, .
•36
•76
•47
1-78
513
•46
Sodium sulphate,
•30
•30
•13
•72
•35
•12
Silica, .....
1-07
•06
•42
640
900
•04
Lime, oxide of iron, &c. ,
•16
•16
•16
03
•16
•02
Water, ....
17-44
28-20
32-35
38-70
5332
3122
Total,
99-84
100-21
99-86
95-1 9t
97-47t
100 08
Actual soap present,
79-28
69-93
65-93
4465
22-53
68-12
* Exhibited in the "Colonial and Indian Exhibition," London, 1886.
For analyses of various of the Colonial soaps, made by the author, vide
"Colonial and Indian Exhibition Reports — Oils and Fats" (Leopold Field).
fOlycerol present, but not determined.
510
OILS, FATS, WAXES, ETC.
MANUFACTURERS' SOAPS (Lant Carpenter}.
"Primrose" Soap.
"Cold
Water"
Soap.
" Neutral
Curd."
"Oil"
Soap,
"Oleic
Acid."
Genuine
Rosin Soap
(South of
Watered
& Silicated
(North of
England).
England).
Fatty acids,* . . . 62 -3
42-66
70-2
67-9
68-6
Combined soda (Na,0), 6 '7
5-4]
7-3
7-0
7-88
" Free alkali " (Na20),
1-21
1-8
nil.
1-0
Silica, ....
•94
1-6
...
...
Neutral salts, . . '2
•55
•4
•2
i-o
Water, . . . . 32 '8
50-40
22-0
28-0
21-0
Total, . . . 102-0
101-17
103-3
103-1
99-48
PHARMACEUTICAL SOAPS (M. Dechan).
Sapo
S. Castil.
8. Ani-
durus,
albus,
Mottled
malis,
S. Mollis,
Hard
White
Castile.
Tallow
Soft Soap.
Soap.
Castile.
Soap.
Fatty acids,*.
81-50
76-70
68-10
78-30
48-50
Combined alkali, .
9-92
9 14
8-90
9-57
12-60
Free alkali,
•08
•09
•19
•28
•30
Silica, ....
•15
•17
Sulphates and chlorides,
Matters insoluble in alcohol,
•28
•50
•36
•60
•63
1-30
•47
1-10
•93
1-60
Other insoluble matter, .
•20
•90
•80
•40
1-00
Water, ....
10-65
13-25
21-70
12-50
39-50
103-13
101-04
101-77
102-62
104-68
SOFT SOAPS (Ure).
London
Soft
Soap.
Belgian
Green
Soap.
Scotch.
Rape Oil
Soft
Soap.
Olive Oil
Soft
Soap.
Fatty acids, .
Dry potash (K20),
Water, salts, glycerol, &c.,
45-0
8-5
46-5
36-0
7-0
57 0
47-0
8-0
450
51-7
10-0
38-3
480
10-0
42-0
100-0
100-0
100-0
100-0
100-0
In general, similar partial analyses of soft soaps meet the
objects in view, inasmuch as such soaps are generally purchased
in quantity under contract either to contain a given percentage
(40, 50, &c.) of fatty acids producible on decomposition by a
mineral acid, or to lose not more than a given percentage in
weight (water) on drying completely ; the degree of alkalinity is
usually judged by the u touch " or taste of the sample, the tongue
being regarded as a sufficiently delicate indicator for such pur-
poses. When more definite information is required the methods
* Not calculated to fatty anhydrides.
ANALYSES OF TOILET SOAPS.
511
above described are applicable ; thus the water is directly deter-
mined by drying in a sand bath (p. 494) ; the total fatty acids,
free alkali, combined alkali, unsaponitied oil, and matters insol-
uble in water (such as starch added to simulate "figging," &c.)
by the respective processes above detailed ; the rosin acids by
Gladding's process (p. 501) or Twitchell's method (p. 503); silicate
by incineration and analysis of the mineral constituents of the
ash ; and so on.
In the case of household and laundry soaps it is to be noticed
that the physical consistence of the substance is in many cases
of as much importance as its chemical constitution. From the
consumer's point of view what is required in the case of a hard
soda soap is an article from which, during use, no more is dis-
solved or abraded than is just requisite for the object in view.
If the soap be of too soft a consistency (either through over
watering, or bad selection of materials), a much larger amount
is rubbed on the clothes, <fcc., to be washed or scoured than is
absolutely necessary, leading to much waste. On the other
hand, pure tallow curd soaps largely boiled down are so hard as
only to rub off and lather with difficulty. With manufacturers'
soaps intended to be dissolved in water before use (e.g., soft soap
for wool scouring, &c.), the rate of solution must be sufficient
for the purpose ; whilst hydrocarbons and other insoluble
impurities which might spot and stain goods must be absent
from soaps intended for treatment during dyeing and subsequent
operations.
TOILET SOAPS.
High-class
Milled
Soap of
Conti-
nental
make.
High-class
Opaque
Soap,
English.
Inferior
Ouaque
Soap,
English.
Transparent Soaps.
Made by
Cold
Process.
Made hy Spirit
Process.
Sugared.
Genuine,
not
Sugared.
Fatty anhydrides, .
Uncombined rosin and
unsaponified fats,
Combined alkali, .
Sodium carbonate,
Sugar, .
Glycerol,
Water and minute
quantities of salts,
Percentage of true
soap, .
Free alkali (Na20),
Mean molecular
•\veight of fatty acids,
83-60
1-00
9-80
•24
5-36
GO -20
G-9S
•17
3-00
29-65
6500
8-91
1-73
6-00
18-36
38-90
•40
5-57
3-80
28-00
3-00
20-33
65-60
3'00
7-73
nil.
14-00
9-67
68-10
3-20
7-62
•20
nil.
7-00
13-88
100-00
100-00
100-00
100-00
100-00 100-00
93-40
•14
274
67'18
•10
276
73-91
1-01
228
44-47
2-22
225
73-33
nil.
272
75-72
nil.
286
512 OILS, FATS, WAXES, ETC.
In the case of " toilet " soaps, the most important quality is
that of furnishing a sufficient lather without at the same time
causing the application of too alkaline a substance to the skin ;
the small amount of free alkali developed by hydrolysis when a
tablet of soap is rubbed on the skin or between the hands is
practically insensible, excepting to extremely sensitively skinned
persons who, in consequence, are rarely able to use soap in any
form without suffering more or less irritating effects. Such
individuals are comparatively rare; but a much larger portion
of the population, especially ladies and young children, are prone
to suffer inconvenience (particularly in windy and wintry weather)
through the use of soap containing more than traces of free
alkali ; to some extent this inconvenience may be mitigated by
introducing into the soap such substances as vaseline, spermaceti,
or even purified lard, &c., whereby a film of greasy or unguent-
like substance is left adherent to the skin, or at least pressed
into its pores (vide p. 478) ; but a far safer plan is so to prepare
or refine the soap as to ensure that it shall not contain any
material amount of free alkali. The author has proposed* to
classify toilet soaps into three grades from this point of view,
viz. : —
First grade. — Soaps containing a total amount of " free alkali "
not exceeding JQ- (2*5 per 100) of the alkali present combined with
fatty anhydrides as soap ; so that if the soap contained 8*0 per
cent, of combined alkali, the free alkali would not exceed 0*2 per
cent.
Second grade. — Soaps where the "free alkali" ranges between
•Jg- and -£Q (2-5 to 7 '5 per 100) of that present as actual soap —
i.e., for a soap containing S'O per cent, of combined alkali the
free alkali would be between 0'2 and 0*6 per cent.
Third grade. — Soaps where the "free alkali" exceeds -£§ (7*5
per 100) of that present as actual soap.
It is to be borne in mind, however, that other possible ingre-
dients besides alkali are apt to be detrimental to sensitive skins:
of these sugar (almost invariably present in transparent soaps) is
the one most certainly known to be noxious (pp. 478, 480, 482);
but there is also reason for supposing that some extremely
highly perfumed soaps may exert a more or less marked irri-
tating action of the same kind in virtue of the comparatively high
proportion of essential oils, etc., present (p. 480), even though
entirely destitute of free alkali, and containing no sugar.
When a soap (toilet, household, or manufacturer's) contains
an amount of glycerol approximately corresponding with that
equivalent to the fatty acids found (92 parts glycerol for 3 x n
parts of fatty acids of mean molecular weight n), the probability
*" Cantor Lectures," Society of Arts, Jo-urn. Sor. Arts, vol. xxxiii.,
p. 112i (18S5), where also various other analyses of toilet soaps are given.
MANUFACTURE OF GLYCERINE. 513
is that the soap has been prepared by a cold process : such a soap,
for instance, might yield fatty acids of mean molecular weight
270, in which case 100 parts of fatty acids would correspond with
~Q — o7n = 11*3 parts of glycerol, if triglycerides were employed,
o x 2i i U
Larger proportions of glycerol can only be contained in cases
where extra glycerol has been added. On the other hand, as
soaps prepared by boiling and salting out contain no glycerol at
all, the presence of smaller proportions of glycerol suggests
either that the soap mass is a mixture of hydrated soaps or cold
process soaps (Chap, xx.) and boiled soaps, or that free oleic acid,
&c., has been employed along with glycerides in its manufacture.
CHAPTER XXII.
GLYCEROL EXTRACTION— MANUFACTURE OF
GLYCERINE.
IN the manufacture of soaps and " stearine" for candlemaking,
large quantities of glycerol * are produced as product comple-
mentary to the fatty acids formed by saponification of the oils
and fats employed. Until comparatively recently, much of the
glycerol thus formed was wasted, being run away along with
other watery fluids into the drains, <fcc. ; but since the introduc-
tion of various applications for which glycerol is suited, more
especially the manufacture of dynamite and other explosives,
much of the substance formerly thrown away as worthless, is
now extracted and utilised by processes which substantially
consist of evaporation so as to remove saline matters by
crystallisation, and distillation with superheated steam of the
final mother liquors.
The " sweet water " obtained in the saponification of glycerides
by lime in the autoclave or open pan processes (pp. 365, 373), is
one of the most eligible sources of commercial glycerine when re-
quired of high purity ; the distillation of fatty matters by means of
superheated steam, so as to hydrolyse them and form fatty acids
and glycerol (p. 385), furnishes a still purer raw product ; if the
temperature of distillation be too high (above 310° to 320° C.),
more or less decomposition of glycerol into water and acrolein
(acrylic aldehyde) results.
The watery glycerol solutions thus obtained are concentrated
* As already stated (p. 110) the word "glycerol" is employed in the
present work to denote the chemical substance C3H5(OH)3, and the term
" glycerine " to indicate commercial products more or less largely consisting
of glycerol in varying states of purity.
33
514 OILS, FATS, WAXES, ETC.
by evaporation, preferably not in ordinary pans, but by special
devices analogous to those used in the sugar industry, where a
series of convoluted tubes or hollow plates heated by the
internal admission of steam, are made to revolve, so that the
tubes or plates partly dip into the fluid to be evaporated and
carry upwards an adherent film thereof as they revolve, which
film rapidly loses water by evaporation whilst the part of the
tube or plate to which it adheres is exposed to the air after
emerging from the liquid, especially if the whole arrangement is
placed inside an exhausted vessel or " vacuum pan."
When the glycerol solution is sufficiently concentrated, it
is decolorised by treatment with animal charcoal, and again
distilled by means of superheated steam,* the processes being
repeated several times for products of high purity, such as the
glycerine required for the manufacture of nitroglycerine for
dynamite arid similar explosives. Glycerines of the highest
degree of purity are best obtained by crystallising, draining
off the unsolidified portion by a centrifugal machine, and melt-
ing the residual crystals.
The extraction and purification of glycerol from soap leys is a
much more troublesome matter, not so much because of the dis-
solved salt, &c., which requires to be fished out as the evapora-
tion proceeds, as because various organic impurities derived
from the fats, &c., are also present. C. T. Kingzett f found the
following compositions in the case of the salts deposited on
evaporation, and of the evaporated mother liquor of specific
gravity 1-236:—
SALTS.
Sodium chloride, . . . . 78 '12
Sodium sulphate, . . . . 8 '61
Sodium carbonate, . . . . . 2-61
Insoluble organic matter, . . . . 0'22
Glycerol and other organic soluble matters, . 3 '55
Water, ...... 7'50
100-61
CRUDE GLYCERINE.
Water, . . . 7 '53 pounds per gallon.
Glycerol, . . .2-04 „
Salts, . .2-78
12-35
The removal of the inorganic salts and the saponaceous,
resinous, and albuminous organic matters contained in the crude
leys may be more or less completely effected in a variety of
ways the subject of a number of patents. Thus, by acidulating
the liquor any soap is decomposed, and fatty and resinous acids
* An improved form of glycerine rectifying apparatus has been patented
by R. O. Unglaub (Eng. Pat., 8,196, 1889).
t Journ. Soc. Chem. Ind., 1882, p. 77.
COMMERCIAL GLYCERINES. 515
set Jfree, separable by filtration. By treating with carbon dioxide
any caustic alkali is carbonated, and its removal by salting out
on evaporation rendered more easy (Versmann). By adding
tannin in some form or other, albuminous matters may be
coagulated and precipitated (Payne). The substitution of
sodium sulphate for common salt in the salting out process is
said to facilitate the separation of saline matters on evaporation,
and the remaining sodium sulphate finally remaining to interfere
less with the purification by distillation, ultimately necessary to
render the glycerol suitable for most of the purposes for which it
is employed (Benno, Jappe, & Co.) Spent leys produced when
black ash liquors are directly used for soapmaking, contain a
variety of impurities not present when purer caustic soda is used,
especially that made by the ammonia process ; such liquors may
be considerably purified by the addition of soluble copper salts,
whereby sulphocyanides and organic matters, <fec., are precipi-
tated (Allen, and Nickels).
A few years ago the Michaud-Freres process for saponifying
glycerides with zinc oxide (p. 379) instead of lime, attracted
considerable attention, it being expected that fatty acids and
glycerol would be so readily obtained that the older soap boiling
processes would be superseded, and direct neutralisation processes
(p. 451) substituted for them, whilst almost pure glycerol would
result, as in the candlemaking lime autoclave process. As yet,
however, this result has not been brought about to such an
extent as seriously to interfere with the older soapmaking
processes. A similar remark applies to methods based on
sapouification with ammonia solution under pressure (p. 379).
Commercial glycerines often contain impurities of various
descriptions best estimated by direct determination. Lime, lead,
magnesia, saline matters, and similar nonvolatile substances are
left behind on evaporation and incineration, and may be examined
in the ordinary ways ; distilled glycerines only contain minute
amounts of inorganic matter, rarely exceeding 0*1 to 0'2 per cent.
Silver nitrate forms no precipitate or darkening in colour after
standing 24 hours when added to glycerines free from acrolein,
formic acid, or other substances capable of reducing silver salts,
but blackens considerably in their presence.* Traces of chlorides
will not precipitate silver nitrate, silver chloride being slightly
soluble in glycerol ; glycerines from soap leys, however, give
copious precipitates, as they usually contain several per cents, of
sodium chloride. Such leys often contain resinous matters, albu-
minoids, fatty acids, and other substances precipitable by basic
lead acetate. Cane sugar and glucose are sometimes added as
adulterations, easily detected by the cuprous oxide (Fehling's)
* According to Ritsert, pure glycerol gives neither deposit of metallic
silver, nor formation of yellow colour, when mixed with its own volume of
ammonia solution, heated to boiling, and treated with silver nitrate.
516 OILS, FATS, WAXES, ETC.
test. Glycerol intended for dynamite manufacture should be
wholly free from organic impurities, because the action of nitric
acid thereon during nitration might seriously endanger the suc-
cess of the process and the stability of the product. Chlorides,
except in the merest traces, should similarly be absent ; whilst
other inorganic matters (lime, &c.) should only be present in traces.
Estimation of Glycerol in Watery Solutions. — For the
qualitative detection of glycerol in aqueous solution a variety of
tests have been proposed, one of which (Reichl's) is described 011
p. 8. Kohn * recommends the following method : — The liquid
to be examined is evaporated with acid potassium sulphate and
the residue heated in a retort ; if glycerol is present, acrolein is
formed, so that the distillate gives a red coloration on treatment
with a solution of rosaniline that has been just decolorised by
sulphurous acid.
Several processes have also been proposed for the quantitative
determination of glycerol, some of which are only suitable under
particular conditions: thus in the case of distilled glycerines of
considerable or tolerable purity where organic matters are absent
and inorganic constituents and water are the only impurities (no
adulteration with glucose or other sugar, &c., being present), the
amount of glycerol may be conveniently ascertained by oxidation
with potassium dichromate and sulphuric acid, either collecting
the carbon dioxide formed, or determining the dichromate reduced
by using a known quantity and back-titrating with a standard
iron solution.! Another method applicable under such condi-
tions is the "acetin process" of Benedikt (p. 186), where the
substance is heated with excess of acetic anhydride and anhy-
drous sodium acetate, and the weight of potash (KOH = 56'1)
determined, neutralised by the acetic acid formed on saponiti-
cation of the triacetin produced (after destroying the excess
of acetic anhydride by boiling with water). J 92 parts of glycerol
correspond with 3 x 56*1 = 168'3 parts of KOH thus neutralised.
Weak glycerol solutions must be evaporated down until at least
50 per cent, of glycerol is present in the fluid.
Two physical methods are applicable in the case of glycerol
solutions where no appreciable amount of interfering impurity
is present, so that practically only glycerol and water are con-
tained ; these are based respectively on the determination of
the specific gravity at 15°, and of the refractive index at the
same temperature.
Skalweit gives the following table § for the purpose of exam-
ining glycerol solutions in these ways : older tables have also
* Journ. Soc. Chem. Ind., 1890, p. 148.
tFor comparative results of various modes of testing commercial gly-
cerines, vide 0. Hehner, Journ. Soc. Clvm. Ind., 1889, p. 4.
J According to Hehner (loc. cit. ) the liquid must vot be boiled, as the tri-
acetin rapidly hydrolyses. § Repert. Analyt. Chemie, v., 18.
SPECIFIC GRAVITY OF GLYCEROL SOLUTIONS.
517
been given by Strohmer* and Lenz, f reproduced by Benedikt. J
Hehner (loc. cit. supra} considers Lsnz's table accurate, and
Richmond has recalculated it to 15°-50.
SPECIFIC GRAVITY AT 15°"5 (Lenz, recalculated by Richmond').
Percentage of
Glycerul.
Specific Gravity at
15° -5. '
Percentage of
Glycerol.
Specific Gravity at
15°-5.
100
1-2674
87
1-2327
99
1-2647
86
1 -2301
98
1-2620
85
1-2274
97
1-2594
84
1-2248
98
1-2567
83
1-2222
95
1-2540]
82
1-2196
94
1-2513
81
1-2169
93
1-2486
80
1-2143
92
1 -2460
79
1-2117
91
1 -2433 ]
78
1-2090
90
1-2406
77
1-2064
89
1-2380
76
1-2037
88
1-2353
75
1-2011
SPECIFIC GRAVITY AND REFRACTIVE INDEX OF GLYCEROL
SOLUTIONS (Skalweit).
Percentage
of
Glycerol.
Specific
Gravity at
15° 0.
Refractive
Index for D at
16° 0.
Percentage
of
Glycerol
Specific
Gravity at
15° 0.
Refractive
Index for D at
15° 0.
100
1 -2650
1-4742
50
•1290
•3996
98
1 -2600
1-4712
48
•1236
•3966
96
1 -2550
1-4684
46
•1182
•3938
94
1 -2499
1 -4655
44
•1128
•3910
92
•2447
1 -4625
42
•1074
•3882
90
•2395
1 -4595
40
•1020
•3854
88
-2341
1-4565
38
•0966
•3827
86
•2287
1 -4535
36
1-0912
•3799
84
•2233
1 -4505
34
1-0858
•3771
82
•2179
1-4475
32
1-0804
•3743
80
•2125
1-4444
30
1-0750
•3715
78
•2071
1-4414
28
1-0698
•3687
76
•2017
1-4384
26
1-0646
•3660
74
•1963
1-4354
24
1-0594
•3633
72
•1909
1-4324
22
1-0542
•3607
70
•1855
1 -4295
20
1 -0490
•3581
68
1-1799
1-4265
18
1 -0440
•3555
66
1-1743
1-4235
16
1-0390
•3529
64
M686
1-4205
14
1 -0340
•3503
62
1-1628
1-4175
12
1-0290
•3477
60
1-1570
1-4144
10
1-0240
•3452
58
1-1514
1-4104
8
1-0192
•3426
56
1-1458
1-4084
6
1-0144
•3402
54
1-1402
1 -4054
4
1-0096
•3378
52
1-1346
1-4024
2
1-0048
•3354
* Monatsh. ,/iir Chemie, v., 61. t Zeitsch. f. Analyt. Chemie, xix., 302
J Analyse der Fette, 2nd edition, p. 256, et seq.
518
OILS, FATS, WAXES, ETC.
Another physical process is also available for such fluids as
the comparatively pure solutions of glycerol obtained kin the
Fig. 144.
course of preparing candle materials (autoclave " sweet waters "),
or for distilled glycerines retaining only small quantities of
519
impurities ; this is based on the differences in the tension of
the vapour emitted by glycerol solutions of various degrees of
concentration. Gerlach's vaporimeter for this purpose is repre-
sented by Fig. 144. A B is a hollow metal cylinder with dished
bottom for heating ; G a glass cylinder fitting therein and made
watertight by the indiarubber ring, H. To use the instrument,
G is disconnected and the whole turned upside-down ; the reser-
voir, F, filled with mercury and a little of the fluid to be examined,
is then connected by a bit of rubber tubing to the end of the
pressure tube, D D, passing inwards through the tubulus, C. The
instrument is then erected, and filled with hot water after fixing
G in position, the temperature being then raised to boiling by
heating B. The expansion of the mercury on heating and the
further expulsion thereof by the vapour emitted from the glycerol
solution fill the pressure tube, D D, with mercury up to a given
level : the length in millimetres of the level-difference between
the mercury in the reservoir and that in the open limb of the
pressure tube (known by means of the attached scales) repre-
sents the difference between the tension of aqueous vapour
emitted from pure water (equal to the existing barometric
pressure) and that of the vapour emitted by the glycerol solution:
from this the percentage of glycerol is reckoned by means of the
table on next page.
When organic substances are absent capable of forming oxalic
acid under the influence of alkaline permanganate, moderately
sharp valuations may be obtained by converting the glycerol
into oxalate (Wanklyn and Fox ; Benedikt and Zsigmondy ;
A. H. Allen). The liquid is rendered strongly alkaline and
boiled with excess of permanganate ; this is destroyed by sodium
sulphite or sulphur dioxide and the liquid filtered and precipi-
tated as calcium oxalate.
When this process is applied to the determination of the
amount of glycerol furnished on saponification by a given oil or
fat, the preliminary saponification should be effected by means
of caustic potash and pure methylic alcohol ; the solution
obtained by treating 2 to 3 grammes of oil is evaporated and
the residue treated with hot water and dilute hydrochloric acid :
a little solid paraffin wax may conveniently be added to help the
solidification of liquid fatty acids on cooling. The whole is
filtered and washed, neutralised with potash and about 10
grammes more potash added ; enough 5 per cent, potassium
permanganate solution (or the powdered salt) is then added to
render the fluid no longer green, but blue or blackish : the whole
is then heated to boiling whereby hydrated manganese dioxide
separates, the liquid becoming red ; aqueous sulphurous acid is
then added till decolorisation is produced, and the whole filtered :
the filtrate is acidulated with acetic acid (whereby any turbidity
due to passage of manganese dioxide through the filter is removed
520
OILS, FATS, WAXES, ETC.
by the action of the sulphurous acid set free) and the oxalic acid
present precipitated by calcium chloride or acetate ; the calcium
oxalate is ignited, dissolved in excess of seminormal acid and
back-titrated with seminormal alkali, using methyl orange as
indicator. 1 c.c. of normal acid (2 c.c. of seminormal) corresponds
with 46 milligrammes of glycerine.
Percentage o
Glycerol.
Specific Gravity of Solution.
Boiling Poin
of Solution.
Tension of
Vapour
emitted
at 100°.
Diminution in
Tensiou
Compared wit
Water giving
760 Millimetres.
At 15°.
Water at
15° = 1.
At 20°.
Water at
20° = 1.
Degrees C.
100
1-2653
1-2620
290
64
696
99
1 -2628
1-2594
239
87
673
98
1 -2602
1 -2568
208
107
653
97
1-2577
1 -2542
188
126
634
96
1 -2552
1 -2516
175
144
616
95
1 -2526
1-2490
164
162
698
94
1-2501
1-2464
156
180
580
93
1 -2476
1-2438
150
198
562
92
1 -2451
1-2412
145
215
545
91
1 -2425
1-2386
141
231
529
90
1 -2400
1 -2360
138
247
513
89
1 -2373
1 -2333
135
263
497
88
1 -2346
1-2306
132-5
279
481
87
1-2319
1-2279
130-5
295
465
86
1-2292
1 2252
129
311
449
85
1-2265
1-2225
127-5
326
434
84
1-2238
1-2198
126
340
420
83
1-2211
1-2171
124-5
355
405
82
1-2184
1-2144
123
370
390
81
1-2157
1-2117
122
384
376
80
1 2130
1-2090
121
396
364
79
1-2102
1 -2063
120
408
352
78
1 -2074
1-2036
119-0
419
341
77
1 -2046
1-2009
118-2
430
330
76
1-2018
1-1982
117-4
440
320
75
1-1990
1-1955
116-7
450
310
74
1-1962
1-1928
116
460
300
73
1-1934
1-1901
1154
470
290
72
M906
T1874
114-8
480
280
71
1-1878
1-1847
114-2
489
271
70
1-1850
1-1820
113-6
496
264
65
1-1710
1-1685
111-3
533
227
60
1-1570
1-1550
109
565
195
55
1-1430
1-1415
107-5
593
167
50
1-1290
1-1280
106
618
142
45
1-1155
1-1145
105
639
121
40
1-1020
1-1010
104
657
103
35
1 -0885
1 -0875
103-4
675
85
30
1 -0750
1-0740
102-8
690
70
25
1-0620
1-0610
1023
704
56
20
1 -0490
1-0480
101-8
717
43
10
1 -0245
1-0235
100-9
740
20
0
1-0000
1-0000
100-0
760
0
OXALATE PROCESS FOR VALUATION OF GLYCERINES.
521
The quantity of glycerol thus found is close to, but generally
a little below, that deduced from the saponification equivalent
of the substance on the assumption that only triglycerides are
present.* In the case of oxidised drying oils, however, a notable
excess is observed, doubtless on account of the formation of other
products yielding oxalic acid by oxidation. Thus Benedikt and
Zsigmondy obtained the following values : —
Name of Oil, &c.
Glycerol ca^ulated from
the Saponification
Equivalent.
Glycerol found by Oxalic
Acid Process.
Olive oil, ....
10-49 to 11-10
10-15 to 10-38
Coker butter, .
Tallow
Cows' butter fat,
Linseed oil,
Skins from boiled linseed oil,
14-76 to 14-83
10-72
12-51
10-24 to 10-66
13-3 to 14-5
9-94 to 10 21
11-59
9-45 to 9-97
15-5 (Allen)
The following table exhibits the amounts of glycerol theo-
retically obtainable from 100 parts of the triglycerides of the
respective acids named ; the last column indicates the amount
of fatty acid simultaneously produced : —
Glyceride of
Formula of Acid.
Percentage of
Glycerol.
Percentage of
Fatty Acid.
Butyric acid,
^14^8^2
30-5
87-41
Laurie
CifHgjOa
14-4
94-04
Myristic
Ci4H28O2
127
94-47
Palmitic
Ci6H3202
11-42
95-28
Steario
Ci8H3602
10-34
95-73
Oleic
V\$HS402
10-41
95-70
Ricinoleic
CisHsjOs
9-98
95-92
Lmolic
Ci8H32O2
10-48
95-67
In the case of the higher acids the sum of the glycerol and
fatty acids is approximately constant — viz., 106 to 107 per 100 of
glyceride used.
C. Mangold f modifies the oxalic acid process by dissolving
0'4 gramme of the glycerine to be tested in 300 c.c. of water
containing 10 grammes caustic potash, and adding 55 c.c. of a
5 per cent, solution of potassium permanganate. After standing
half an hour hydrogen peroxide solution is added until all
manganese is precipitated. A known fraction of the total fluid
* If E is the mean saponification equivalent of a mixture of triglycerides,
3E milligrammes of the mixture theoretically yield 92 of glycerol =
x 100, or
per cent.
t Zeits. angew. Chem., 1891, p. 400.
522 OILS, FATS, WAXES, ETC.
is filtered off, boiled for half an hour to destroy excess of
hydrogen peroxide, acidulated with sulphuric acid after cooling,
and titrated with permanganate so as to determine the oxalic
.acid produced.
David recommends the following process for determining the
amount of glycerol formed on saponifi cation. 100 grammes of
fat are heated with 65 of crystallised barium hydrate, and 80 c.c.
of 95 per cent, alcohol added with agitation. The nearly solid
mass is boiled with 500 c.c. of water and allowed to settle ; the
residue left on pouring off the supernatant fluid is washed twice
by decantatioii, and the total fluid evaporated to half its bulk
with sulphuric acid, the surplus being removed by barium car-
bonate. Finally the filtered fluid is evaporated to 50 c.c. and
examined either as to its refractive power or as to its specific
gravity, the amount of glycerol being deducible by means of the
table given on p. 517.
According to Hehner (loc. cit. supra) the bichromate process
(p. 516) gives sufficiently accurate results for practical purposes
with fats and soaps when thus carried out ; the fat is saponified
with alcoholic potash (about 3 grammes being used) and diluted
to about 200 c.c. ; the fatty acids are separated by means of
dilute sulphuric acid and filtered oft'; the filtrate is boiled down
to half its bulk and treated with sulphuric acid and dichromate;
Obviously if any traces of alcohol are left in the fluid, or if
soluble acids or other organic matters capable of reducing di-
chromate are present, the results will come out too high. Oper-
ating in this way Hehner obtained the following percentages of
glycerol : —
Olive oil, .... 10-20 per cent.
Cod liver oil, . . . 9'87 ,,
Linseed oil, . . . 10 '24 ,,
Margarine, . . . 10 '01 ,,
Butter fat, . . 11 -96 to 12 -4
When chlorides or aldehydic matters are present (e.g., acrolein
in distilled glycerines) the glycerol solution is first treated with
silver oxide, being slightly diluted and warmed therewith in a
flask ; basic lead acetate is then added in slight excess, the fluid
made up to a known bulk, and an aliquot part filtered off through
a dry filter and treated with dichromate.
Glycerol in Soap Leys. — On account of the organic im-
purities present in soap leys along with large amounts of in-
organic salts, the above methods, as a rule, are not directly
available for the estimation of glycerol in such liquors. By
evaporation these may be concentrated without material loss
of glycerol at first, although subsequently a perceptible amount
is carried away with the escaping water vapour as the liquors
become highly concentrated. When the evaporation is carried
GLYCEROL IN SOAP LEYS. 523
nearly to dryness a residue is obtained from which nearly
absolute alcohol dissolves out glycerol along with more or less
inorganic matter ; a rough estimate of the glycerol present is
obtainable by evaporating the alcoholic solution to dryness
and weighing, and then gently incinerating so as to burn off
organic matter, the weight of ash left being deducted from that
of the total residue. If, however, other organic matters soluble
in alcohol be present, obviously they would thus be reckoned
as glycerol ; in some cases a partial purification of the glycerol
may be brought about by again evaporating the alcoholic extract,
treating the residue with a small quantity of absolute alcohol,
and then adding one and a-half times the volume of ether ;
glycerol is kept in solution, but some of the other organic matters
are usually precipitated, so that a partial purification is brought
about. In other cases the crude glycerol may be purified by
treatment with neutral or basic lead acetate to precipitate
colouring matters, &c. When rosin is present in the liquors
they may be conveniently purified by evaporating down after
neutralising with dilute sulphuric and adding a little milk of
lime (whereby most of the rosin is converted into insoluble
lime salt) and filtering ; the residue is treated with a mixture of
three volumes absolute alcohol and one of pure ether, the dis-
solved matter weighed (after expulsion of the solvent) and
corrected for ash left on incineration (Fleming").
Another process (Muter's)* consists in heating the crude
glycerol liquors with basic lead acetate to remove certain kinds
of organic matters that would interfere with the subsequent
part of the test, filtering and removing the lead by sulphuretted
hydrogen, and then treating with caustic soda or potash, and
dropping in copper sulphate solution with continuous agitation
until copper hydroxide remains permanently undissolved ; the
quantity of copper contained in the blue solution is about pro-
portionate to the amount of glycerol present (under certain con-
ditions— vide infra), so that by determining the dissolved copper
the glycerol is known. For this purpose Muter employs a
standard solution of potassium cyanide, for which the author
has substituted a colorimetric process based 011 comparison of
the hue of the tinted fluid (filtered) with that of a known relative
thickness of copper solution containing a known amount of
copper also dissolved in glycerol solution under the same con-
ditions.!
Unless the proportion of caustic alkali present is uniform, a
measurable difference in the solvent power of glycerol for copper
hydroxide is noticeable, as the amount of alkali varies (Puls) ;
so that when a cyanide solution is used it should be standardised
* Analyst, 1881, p. 41.
t Alder Wright, "Cantor Lectures," Society of Arts Journal, 1885,
xxxiii., p. 1123.
524 OILS, FATS, WAXES, ETC.
by means of a known glycerol copper solution prepared side by
side with the substance examined in exactly the same way.
Crude glycerol solution, purified by basic lead acetate, usually
retains but little of any organic matters of an alcoholiform or
liydroxylated character, so that the acetin method (supra] can
generally be applied without serious error to the residue left on
evaporation and extraction with alcohol. This, however, is not
so certainly the case as regards the oxalate method, there being
a possibility of obtaining oxalate by the oxidation of organic
matters other than glycerol ; whilst the dichromate process is
usually inapplicable, organic impurities being generally still left
which readily reduce dichromate.
A method sometimes employed is to heat a quantity of crude
glycerine, representing about 2 grammes of glycerol, with 40
grammes of litharge to about 130°, taking care that no carbonic
acid gets access to the mass ; when the weight becomes constant
the whole is similarly heated to 160°, at which temperature the
glycerol is volatilised excepting that a molecule of water remains
behind combined with the lead oxide, so that the loss of weight
74
is — times the glycerol present; hence the loss of weight at
92
160° multiplied by — = 1*243 represents the glycerol present.
"With glycerol containing resinous matter it is impracticable to
expel all the glycerol at 160°; whilst if chlorides or sulphates of
alkali metals are present these react on the lead oxide forming
hydroxides which readily absorb carbonic acid (Hehner).
525
INDEX.
ABB£, refractive index, 51.
Abel, flashing point apparatus,
126.
Absolute measure, determination of
viscosity in, 107.
Absorption of oxygen by fatty acids,
by oils, 42, 125, 129-
137, 318, 341.
,, ,, during cod liver oil
extraction, preven-
tion of, 248.
,, quickened by boil-
ing, 129, 313.
,, ,, test for lubricating
oils, 134, 330.
See also Oils
(blown), Oils (dry-
ing), Gumming.
,, spectrum, 50.
Acajou — see Oil (cashewnut).
Accumulators — see Hydraulic presses.
Acetic anhydride, action on acids
from Turkey red oils,
335.
,, action on alcohols, glycerol,
&c., 8, 13, 186, 191.
,, action on cholesterol and
allied bodies, 17, 191.
,, action on hydroxylated
acids, 35, 37, 41, 186-191.
„ action on non- hydroxy-
lated acids, 189-191.
,, action on cenanthol, 25.
Acetyl acid number (acetyl saponiti-
cation number), 187.
Acetyl number, titration ; acetyl
number, distillation, 198.
Acetylation test (acetyl test, acetyl
number), 17, 43,
121, 129, 157, 341.
,, ,, process of working,
186-191.
,, ,, process of working,
Lewkowitsch's dis-
tillation modifica-
tion, 190, 198.
Acetylation test, use of, in analysis of
glycerine, 8, 186,
516.
,, „ ,, in analysis of
lubricants, 329.
„ ,, „ in analysis of
Turkey red oils,
335.
„ „ ,, in analysis of
Yor ks hire
grease, 273.
Acid, acetic, 20, 288.
,, as solvent (Valenta's
test), 55-57, 347, 349.
„ formed from oleic acid
24, 28, 30, 387.
acetyl oxyoleic, 189.
,, oxystearic, 186.
acrylic, 25, 27.
aldepalmitic, 24, 25.
angelic, 25.
anhydrodioxystearic, 42, 46.
,, possibly formed in
blown oils, 319.
,, arachic (arachidic, butic), 21.
,, ,, separation from other
fatty acids, 112.
,, azelaic, 34, 35, 36.
,, benic (behenic, benistearic),21.
,, benolic (behenolic), 31, 32, 45.
,, benomargaric, 21, 22.
,, benoxylic, 45.
,, benzole, 19, 32.
,, bcnzoleic, 32.
,, benzoyl oxymyristic, 37.
„ brassic (brassaidic), 28, 29, 44,
129.
,, bromohypogseic, 42.
,, bromoleic, 28, 41.
,, bromomyristic, 38.
,, bromostearic, 30.
,, butic — see Acid (arachic).
,, butyric, 20, 288.
,, camphic, 32.
,, campholenic, 32.
,, caproic— see Acid (hexoic).
„ capric— see Acid (decoic).
,, caprylic — see Acid (octoic).
carbolic — see Phenol.
526
INDEX.
Acid, carnaubic, 21.
,, cerotic, 21, 190, 358.
„ ,, formation, test of adulter-
ation of beeswax, 359.
,, cetic, 21, 22.
,, chloriodostearic, 177.
,, chlorocrotonic, 31, 32.
,, chloropropiolic, 32.
,, cimioic, 25.
,, cimiamic, 19.
„ cocinic, 20, 22.
,, crotonic, 25, 288.
,, crotonoleic, 288.
,, damaluric, 24, 25.
,, daturic, 21.
,, decenoic, 25.
,, decoic (capric), 20, 190.
,, diacetyloxysteario, 190.
,, diallyl acetic, 32.
,, dibromopropionic, 27.
,, dibromostearic, 31, 41, 176.
,, dibromoxystearic, 176.
,, dichloracylic, 32.
,, diiodostearic, 26.
,, dioxybenic, 28, 29, 44, 129.
,, dioxybenolic, 45.
,, dioxyheiidecoic, 44.
,, dioxypalmitic, 42, 44, 336.
„ dioxystearic, 28, 30, 41-45,
128, 190.
,, diricinoleic, 146.
,, diricinoleosulphuric, 146, 333.
,, dodecenoic, 25.
,, dodecoic — see Acid (lauric).
,, doeglic, 25.
,, ,, existence doubted. 24.
,, elceomargaric, 32.
,, eloeostearic, 32.
„ elaidic, 28, 29, 43, 44.
,, enneadecoic, 21.
,, ennenoic, 25.
,, eiinoic, 20, 36.
„ erucic, 25, 28, 29, 32, 44, 129,
180.
,, ,, characteristic of rape
class, 284.
,, ,, oxidation products of,
28, 29, 44, 129.
,, formic, 20, 288.
,, geoceric, 21, 22.
,, geranic, 15.
,, glycerosulphuric, 144.
, , hendecenoic, 20, 25, 32, 40, 44.
,, hendecinoic (hendecolic, unde-
colic), 31, 32.
,, hen decoic, 20.
,, hendecolic, 31, 32.
,, heptadecenoic, 25.
,, heptoic (cenanthic),20,40,41,146
Acid, hexabromostearic, 176.
,, hexacetyllinusic, 37.
, , hexoic (caproic), 20, 288.
,, hexoxacetylstearic, 37.
,, hexoxystearic, 19, 37, 43, 44,
128, 135.
,, hyaenic, 21, 22.
,, hydrobeiizoic, 32.
,, hydrochloric-see Hydrochloric
acid.
„ hypogseic, 25, 44, 180.
,, ,, doubt as to existence
of, 24, 111.
,, iodopropionic, 27.
,, iodostearic, 30, 38.
,, isobutyric, 20.
,, isodioxybenic, 29.
, , isodioxy stearic — .see Isomerides
(dioxystearic acid).
,, isohexoic, 20.
,, isohexoxystearic — see Acid
(isolinusic).
, , isoleic, 25, 29, 38, 43, 44.
,, ,, contained in distilled cot-
ton seed stearine, 305.
,, ,, in candle stearine, 262,
375, 380.
,, ,, formed from zinc chlo-
ride and oleic acid,
143, 262, 380.
,, ,, formed during distilla-
tion, 262, 380.
„ isolinolenic. 37, 43, 128, 135.
,, isolinusic, 37, 43, 128, 135.
,, isoricinoleic, 41.
,, isotrioxystearic, 40, 43, 44.
,, isovaleric, 20.
,, isoxy stearic — see Isomerides
(oxystearic acid).
,, lauric, 20, 71-74, 190, 288.
,, lignoceric, 21.
,, linoleic, 33, 134.
,, linolenic, 35, 36, 43, 44, 128,
135, 176, 180.
,, linolic, 30-33, 90, 176, 180.
,, ,, not contained in animal
oils, 291.
,, ,, oxidationproductsof,19,
34, 35, 43-45, 128-137.
„ linusic, 19, 37, 43, 44, 128, 135.
„ margaric, 21, 22, 309.
„ „ artificial, 21, 309.
„ medullic, 21, 22.
„ melissic, 13, 21, 358.
,, methyl crotonic — see Acid
(tiglic).
,, moringic, 24, 25.
,, myristic, 20, 31,32, 71-73, 113,
288.
INDEX.
527
Acid, myristolic, 31, 32.
,, nitrous, test with — see Elaidin
reaction.
, , nitric, test with — -sec Nitric acid
,, octenoic, 25.
,, octoic, 20.
,, oenanthic — see Acid (heptoic).
„ oleic, 25, 38, 68, 75, 90-92, 113.
,, ,, action of acetic anhy-
dride on, 190.
,, ,, ,, of bromine and iodine
on, 27, 176, 180.
,, ,, ,, of fused potash on,
24, 28, 30, 387.
,, ,, „ of nitrous acid on
(elaidin reaction), 28.
,, ,, ,, of sulphuric acid on,
27, 145, 149.
,, ,, ,, of sulphur chloride
on, 155, 156.
,, ,, ,, of zinc chloride on,
39, 142.
,, ,, amount in candle stear-
ine, 375-377.
,, ,, conversion into stearic
acid, 26, 386, 387.
,, ,, determination of ( Muter 's
process), 376.
,, ,, oxidation products of,
10, 28, 43-45, 128.
,, ,, separation from other
acids, 112, 376.
„ ,, soap — see, Soapmaking.
,, ,, yield from ox fat, 311.
See also Red oils.
,, oleo-oxystearic, 330, 331.
oleo-stearic, 331.
orthopropionic, 12.
,, oxybenzoic— see Acid (sali-
cylic).
,, oxyhypogaeic, 41, 43.
„ oxylinoleic, 125, 134.
,, oxymyristic, 37, 38.
,, oxy oleic, 41, 42, 43, 332.
, , , , contained in de"gras, 336.
,, formed in blowing oils,
319.
,, oxypalmitic, 38.
„ oxystearic, 25, 27, 38, 39, 43,
143-145, 330, 384.
„ oxystearosulphuric, 27, 29, 38,
144, 330.
,, palmitic, 21, 44, 72, 74, 91.
., , , , action of acetic anhy-
dride on, 190.
.,, ,, artificial, manufac-
ture of, 387.
.,, ,, formation from cety-
lic alcohol, 13.
Acid, palmitic, formation from oleic,
isoleic, and elaidic
acids, 30 — see also
Acid, oleic, action of
potash on.
,, ,, mixed with stearic — see
Candle stearine.
, , , , occurrence in arachis oil
denied, 111.
,, ,, present in spermaceti of
low grade, 361.
,, ,, separation from other
acids, 112, 113,376.
,, used for night lights, 407.
palmitolic, 31, 32, 45.
palmitoxylic, 45.
paraffmic, 21.
parasorbic, 32.
pelargonic— see Acid (ennoic).
pentadecoic, 20, 21.
pentaricinoleic, 147.
pentoic, 20.
pentolic, 32.
petroleumic, 25.
phoronic, 25.
phosphoric, colour test, 151.
physetoleic, 4, 25.
,, characteristic of train
oils, 292.
propiolic, 32.
propionic. 20.
pyroterebic, 25.
rapic, 41, 43, 284.
ricilinolic, 32, 36.
ricinelaidic, 40, 43, 44.
ricinic, 41.
ricinoleic, 39, 40, 90, 176, 180.
, , action of fused potash on,
40.
,, oxidation products of, 19,
40, 43, 44, 129.
, , polymerised, 1 46, 1 47, 333.
ricinoleos ul ph uric, 1 45 , 332, 333.
salicylic, 5, 19.
sativic, 19, 34, 35, 43-45, 135.
,, as characteristic oxidation
product, 128, 344.
,, formed from olive oil, 344.
,, not formed from animal
oils, 291.
sebacic, 40.
sorbic, 32.
stearic, 21, 72, 73, 88-92, 155,
156, 190, 309.
,, adulterant of beeswax and
spermaceti, 359, 361.
,, formed fromlinolic acid, 34.
,, ,, from oleic acid, 26,
386, 387.
528
INDEX.
Acid, stearic, formed from ricinoleic
acid, 40.
,, ,, formed from sativic acid, 35.
,, ,, separation from other
acids, 112, 113,376.
,, ,, yield from ox fat, 311.
See also Candle stearine.
,, stearidic, 25, 30.
„ stearolic, 31-33, 35, 45.
,, stearoxylic, 33, 36, 45.
,, stillistearic, 21, 22.
,, suberic, 36.
,, sulphuric— see Sulphuric acid.
,, sulphurous — see Sulphurous
acid.
,, tariric, 32, 36.
,, terebic, 25.
,, tetrabromostearic, 31, 176.
,, tetracetyl sativic, 35.
,, tetradecenoic, 25.
,, tetraricinoleic, 147.
,, tetrolic, 31, 32.
,, tetroxy stearic — see Acid (sati-
vic).
,, tetroxacetyl stearic, 35.
„ theobromic, 21, 22.
„ tiglic (methylcrotonic), 25, 288.
,, toluic, 19.
„ tridecenoic, 25.
,, tridecoic, 20, 22.
„ trioxy stearic, 19,40,43,44,129.
,, trioxacetyl stearic, 41.
,, triricinoleic, 147.
,, tritylic, 20.
„ umbellulic, 20.
,, undecolic — see Acid (hende-
colic).
„ undecylic — see Acid (hende-
coic).
,, undecylenic — see Acid (hende-
cenoic).
„ valeric, 20, 275, 288.
Acid number, free — see Acids (free
fatty).
,, ,, total — see Total acid
number.
,, process (oil refining), 259.
,, salts, 23.
Acidity of soaps, 24, 498.
Acids, dibasic, 18.
, , distilled (manuf acturingplant),
382-384.
,, ,, melting points, 384.
,, fatty; formed by hydrolysis and
saponitication, 7, 10,
12, 114.
„ „ „ during systematic
examination of oils,
&c., 124.
Acids, fatty; formed from alcohols by
action of fused potash, 13.
„ ,, from glycerides, yield of,
163.
,, ,, from soap, 172.
,, ,, from tallow, palm oil, &c. ;
valuation by melting
point, 75, 76.
,, ,, from various oils, &c. ;
melting points, 69-76.
,, ,, insoluble in water — see
Hehner number; Insol-
uble acid number.
,, ,, insoluble in petroleum
ether, from boiled oils,
135.
,, ,, iodine number of — see
Iodine number.
,, ,, mean equivalent, 116, 164-
173, 196.
,, ,, mean equivalent is less
than saponitication equi-
valent of glycerides by
12-67, 165, 197.
,, ,, melting points of — see
Melting points.
,, ,, mixtures of; calculation
of composition, 172.
,, ,, neutralisation numbers
of — see Neutralisation
number.
,, ,, oxidation during drying,
113.
,, ,, oxidation of, from drying
oils, 136.
,, ,, polymerised, from castor
oil, 146.
,, ,, separation of, as lead
salts, &c., 112, 128, 136,
356, 376.
,, ,, solid from tallow and
palm oil, 74-76 — see
Candle stearine.
,, ,, soluble in alcohol, 23.
,, ,, soluble in water, 23, 163,
167-170, 195.
,, ,, soluble in soap analysis,
497.
,, ,, soluble acid number — see
Soluble acid number.
„ „ volatile, 22, 113— see also
Boiling points.
,, „ ,, acid number — see
Volatile acid number.
,, ,, ,, contained in York-
shire grease, 275.
,, ,, ,, with superheated
steam — see Distil-
lation.
INDEX.
529
Acids, fatty, volatile, with wet steam,
22, 112 — see also Reich ert
number ; Volatile acid
number.
,, ,, unsaturated, in pressed
candle stearine, 375.
,, free fatty, amount present in
oilcakes, 115,214.
,, ,, as candle material
— see Candles,
stearine.
,, ,, determination of
free acid number,
24, 115-119, 194,
341.
,, ,, determination of,
by Burstyn's
method, 118.
,, ,, detrimental effects
of, 115,260,313,
322, 356.
,, ,, examination of, for
detecting adul-
teration, 356.
,, ,, formed by hydro-
lysis— see Hydro-
lysis.
,, ,, from Turkey red
oils, 334, 335.
,, ,, iodine number, 180,
184, 197, 356.
,, ,, iodine number ex-
ceeds that of gly-
cerides by about
4'5 per cent.,
185, 197.
,, ,, occurrence in natu-
ral oils, &c., 114-
119, 292, 355.
,, ,. production of, in
orease recovery,
271, 272.
,, ,, proportion usually
present, 115.
,, mineral, detection of, 123, 323.
,, ,, inadmissible in puri-
fying lubricants, 325.
,, ,, injurious eti'ects of,
115, 260, 322, 325.
,, monobasic, 18.
,, polyhydroxylated stearic, 43-
46, 128-137.
,, series of, acetic (stearic), 18,
19.
acrylic (oleic), 18, 24.
benzoic, 19.
bromoleic, 28.
cinnamic, 19.
dichloroacetic, 31.
Acids, series of, dibromoacetic, 26,31.
,, ,, diiodoacetic, 26.
,, ,, dioxystearic — see
Glyceric series.
,, ,, erythroglucic (trioxy-
stearic), 19, 43.
,, „ glyceric (dioxy-
stearic), 19, 27,43.
,, ,, gly collie — see Oxy-
acetic series.
,, ,, hexoxystearic, 19, 43.
„ „ linolenic, 18, 36.
,, ,, linolic— see Propiolic
series.
,, ,, oleic — see Acrylic
series.
,, ,, oxyacetic (oxy-
stearic, glycollic),
19, 27, 37.
,, „ oxyacrylic(ricinoleic).
19, 39.
,, ,, oxy benzoic, 19.
,, ,, oxy oleic — see Oxy-
acrylic series.
,, ,, oxystearic — see Oxy-
acetic series.
,, ,, propiolic ( linolic), 18,
28, 30.
,, ,, ricinoleic — see Oxy-
acrylic series.
,, ,, salicylic, 19.
,, ,, stearic — see Acetic
series.
,, „ stearolic, 30, 31, 45.
,, ,, stearoxylic, 33, 45.
„ „ tetroxystearic, 19, 43.
,, ,, trioxystearic — see
Erythroglucic series.
Acrojein (acrylic aldehyde), 15, 25.
,, in glycerine, 515.
,, produced by action of heat
on oils, 125.
,, ,, dehydration of
glycerol,8,513.
,, ,, oxidation of lin-
seed oil (lino-
leum), 318.
Actual density, incorrect use of term,
89.
Adipose tissues, Mege Mouries pro-
cess, 308.
,, rendering of, 245-251.
,, use of, as food, 303.
Adulteration, general methods of de-
tecting, 340-342— see also
each oil, &c., separately.
,, with solid suspended mat-
ters, determination, 123.
JSsculin, 50.
34
530
INDEX.
^Etherzahl — see Ester number.
Air, bleaching oils by means of hot,
264.
,, used in preparing blown oils —
see Oils, blown.
,, ,, ,, boiled oils — see Oils,
drying, boiling of.
,, wax bleaching by exposure to,
and light, -268.
Air bath, Pensky's,flashingpoint, 1 27.
,, Pohl's, melting point, 63.
,, specific gravity, 80.
Air blast, Dunn's (soapboiling),- 433.
Albuminous matters, determination,
119-123.
, , , , removal from crude
glycerine, 5 14,515.
,, ,, removal from oils,
&c. — see Oils
(clarification).
Alcohol, allylic, 15, 44.
,, amylic, 14.
,, benzylic, 16.
,, butylic, 14.
,, cerylic, 14.
,, ,, present in Yorkshire
grease, 272.
,, cetylic, 4, 6, 7, 14.
,, ,, action of acetic anhy-
dride on, 15, 191.
,, ,, action of fused potash
on, 13.
,, ,, contained in cetacean
oils, 114, 116, 121.
,, ,, contained in degras, 336.
,, ,, contained in spermaceti
— see Spermaceti.
,, ,, contained in Yorkshire
grease, 272.
,, palmitic acid from, 13.
cinnamic, 16.
decylic (decatylic), 14, 40.
dodecylic (dodecatylic), 14,
114.
ethylic, 4, 14.
hendecylic, 14.
heptadecylic, 14.
heptylic, 14.
hexadecylic, 14.
hexylic, 14.
isobutylic, 14, 20.
isocerylic, 14.
isomyricylic, 14.
isopropylic, 14.
methylic, 5, 14.
myricylic, 4, 14, 21, 358.
,, action of fused
potash on, 13.
nonylic, 14.
Alcohol, octodecylic, 14.
,, octylic, 5, 14.
,, pentadecylic, 14.
,, propylic, 14, 20.
,, sycocerylic, 16.
,, tetradecylic, 14.
,, tridecylic, 14.
xylylic, 16.
Alcohol, solubility in — see Solubilitjr.
Alcoholiform products of saponifica-
tion, 4-18, 121.
Alcohols, acetyl numbers of, 17.
,, dihydric — see Glycols.
,, fermentation — see Oils
(fusel).
,, free in oils, due to hydro-
lysis, 7, 114, 116, 171.
,, hexhydric, 5.
,, higher, contained in York-
shire grease, 272.
,, monohydric, 4, 13.
,, pentahydric, 5.
„ series of, acrylic (allylic),
13, 15, 44, 114.
benzylic, 15, 16.
cholesteric, 16.
cinnamic, 13, 16.
ethylic, 13, 14,
114, 116.
geranic, 15.
phenolic, 13, 15.
,, tetrahydric — see Erythrol.
,, trihydric — see Glycerols.
Aldehydes, 3, 6, 15.
,, hydrogenation of, 14.
,, oxidation of, 20, 25.
Alkali, calculated quantity requisite
for saponification — see Cal-
culations.
,, free, in soaps, injurious effects
of — see Soaps, alkaline.
Alkalies, action on brominated and
chlorinated acids, 28-32, 38.
,, effect of fusion with — see Hy-
drogen.
,, effect of fusion with, on oleic
acid and isomerides
see — Acid (oleic,
palmitic).
,, ,, on ricinoleic acid, 40.
,, manufacture of, 410.
,, mild and caustic, 409— see Po-
tash (caustic), Soda (caustic).
,, quantities mutually equivalent
to one another, 425.
, , use of, in refining oils, &c. , 260.
,, use of, in soapmaking, 409.
,, vegetableand mineral, 410 — see
Potash, Soda.
INDEX.
531
Alkalimetrical assay, 420.
Alkaline carbonates as saponifying
agents, 409, 410.
,, ,, causticising of — see
Causticising.
,, ,, direct use in soap-
making, 409, 433,
453, 460, 463.
,, earths, use in refining, 256.
,, refining processes-see Refining.
,, soap, injurious effects — see
Soap, alkaline.
,, solutions, strength of, 418, 419.
Alkalinity, degrees of— see Degrees,
negative, 498, 499.
of leys, 414-419.
,, ,, corrections for impur-
ities, 419.
,, ,, effect of temperature
on density, 416.
,, of soda, British trade cus-
tom, 420.
Allbright & Clark, spontaneous in-
""flammation, 132.
Allen, A. H., beeswax, 358, 359.
,, bromine reaction, 177.
,, distilled cotton seed
stearine, 305.
,, glycerine valuation, 519.
,, linolic acid, 34.
,, Maumene's test, 149.
,, melting points, 71.
,, nitric acid test, 140.
„ Reichert's test, 174.
relative density, 89, 93.
, , saponification equiva-
lents, 160.
,, soap analysis, 494, 507.
, , sugar test for sesame", 346.
,, sulphur in oils, 123.
,, sulphuric acid colour re-
actions, 151.
,, test for arachis oil, 344.
,, Valenta's test, 56.
„ viscosimetry, 99, 101, 104.
,, waggon grease, 327.
Allen and Nickels, glycerine extrac-
tion, 515
Allen and Thomson, free alcohols in
sperm oil, &c., 171.
,, unsaponifiable matters in
various oils, &c., 257.
Alligator fat, 299.
Allihn's condenser, 239.
Allyl cyanide, 25.
,, ethers, 15, 25.
Almonds, sweet and bitter — see Oil
(almonds).
Alpaca fat, 299.
Alum in lard, 307.
,, use in cleansing rancid tallow,
256.
Aluminium oleate used in thickening
oils, 121-124, 324, 329.
,, soaps, 121-124, 324, 328, 329.
Aluminoferric cake, aluminium sul-
phate, use in recovering grease,
270.
Amagat and Jean, oleorefractometer,
51.
Ambreol (ambergris), 3, 17.
Ambiihl, specific gravity vapour bath,
80.
American mineral oils, viscosity, 105.
Ammonia process for alkali manufac-
ture, 410.
,, saponification process, 379,
410, 515.
,, salt, dealkalising process
( Alder Wright's ) — see
Wright, Alder.
Angelica, 25.
Anglo-American system of oil pres-
sing, 210, 215-218.
Anhydrides, fatty, in analysis, 371.
,, of dioxystearic acids, 42, 46.
, , of nonhy droxy lated acids, 189.
,, of oxystearic acids, 30, 39.
Animal charcoal, use of, in decoloris-
ing oils, &c. , 263, 269.
,, ,, use of, in deodorising
cokernut oil, 310.
,, ,, ,, in purifying gly-
cerine, 514.
,, ,, ,, in purifying lan-
olin, 339.
,, fats, acids from, 21, 25.
,, ,, rendering of, 245-251.
Anise camphor (anethol), 192, 194.
Anschtitz, action of acetic anhydride
on benzoic acid, &c., 189.
Anthracene, extraction from anthra-
cene oils, 230.
,, oils (coarse lubricants), 328.
Antifriction ingredients, 324-328.
Aqua regia, colour test, 151.
Arachin (arachicglyceride), chief con-
stituent of Rambutan tallow, 296.
Arachis nuts, decortication of, 224.
Araeometer, 77.
,, (Burstyn's method), 118.
,, Lefebre's, 79.
„ thermal, 82, 347.
Archimedean screw (mixing soap),
440.
Archbutt, elaidin test, 138.
,, free fatty acids in burning
oils, 313.
532
INDEX.
Archbutt, Maumene's test, 149.
Argand lamp, 313.
Arnaud, tariric acid, 36.
Ashes as detergents, 409.
Artificial butter — see Margarine.
,, lard — see Lard.
Autoclave for soapmaking — see Soap-
making (hydrated soaps).
,, rock, 374.
,, stearine process, 373— see
Candle stearine.
Axle grease — see Lubricants.
B
BACH, absorption of oxygen, 134, 329.
,, melting points, 71.
Bagging for presscakes, 217.
,, of semisolid oils to separate
" stearines," spermaceti,
&c., 229, 305, 360.
Ballantyne, effect of light on oils,
130-132, 149— see also Thomson and
Ballantyne.
Balsam of Peru, 16.
Tolu, 19.
Barilla, 410, 473.
Barium polysulphide (colour test), 151.
,, sulphate, adulterant of wax, 359.
Barring (soap), 437, 438, 444.
Baths — see Air bath, Hot baths,
Chilling baths, Vapour baths,
Water baths, &c.
Bauerand Hazura, dry ing oils 136,290.
Baynes, Maumene's test, 149.
Beans, fatty matter contained in
various kinds of, 241-244.
Bears' grease, 299.
Beaume, rational scale, 86.
Becchi's test for cotton seed oil, 131,
306, 346.
Beech wood tar, 21.
Beef fat, beef tallow — see Tallow.
Beef stearine — see Stearine (beef).
Beeswax — see, Wax (bees).
Beet fusel oils, 14.
Bell, J. Carter, lubricating oils, 325.
Bender, viscosity, 106.
Benedikt, beeswax, 358.
,, density of glycerol solu-
tion, 517.
hydrometer scales, 85.
iodine numbers, 183.
iodine number of linseed
oil, 351.
phosphorus in oils, 124.
total acid numbers, 160.
use of acetylation test, 129,
516.
Benedikt, zinc chloride and oleic acid
39, 142.
Benedikt and Griissner, methyl num-
ber, 192.
Benedikt and Hazura, nonformation
of sativic acid from animal oils, 291.
Benedikt and Ulzer, acetylation test —
see Acetylation test.
,, ,, oxy oleic acid, 42.
,, ,, oxystearosulphuric
acid, 145.
Benedikt and Zsigmondy, glycerine
valuation, 519, 521.
Bennett and Oibbs (soapmaking under
pressure), 463.
Benno Jappe & Co., glycerine extrac-
tion, 515.
Bensemann, melting points, 71-
tubes, 62.
Benzene, 3.
as solvent, 55, 23 1 , 236, 252,
254, 337, 339, 359.
Benzoic aldehyde, 3.
„ ethers, 17.
Benzoline — see Petroleum ether.
Beyer, plotting machine, 448.
Bicarbonate formed during saponifi-
cation, 410.
Bichromate process, glycerol estima-
tion— see Glycerine,
manufacture of
(valuation).
,, (oil bleaching), 264-266.
,, ,, (wax bleaching), 266,
269.
Biliary constitu tents in liver oils,
292, 354.
Bishop, polarised light, 50.
Bladder lard, 306.
Bleaching oils, &c., 50, 263-269, 358,
364
, , powder, use of in decoloris-
ing oils, 264, 266, 267.
Blown oils — see Oils (blown).
Blowpipe, 428, 433.
Blubber, extraction of oil from, 247.
Bock's process, 384.
Boiling down blubber, &c., 247.
, , oils, changes occur ring during,
125, 129.
points, acetic acid series, 20.
,, acrylic, 25, 28, 29.
,, alcohols, 14.
,, pure triglycerides, 11.
processes, 313-318.
Bone fat (bone grease, bone oil), 67,
88-91,160,181-184,298,299.
,, adulteration of tallow fat
with, 355.
INDEX.
533
Bone fat, extraction of, from bones,
251-254.
,, removal of calcium phosphate,
&c., contained in, 256.
Bone tar (bone oil, Dippel's oil), 2, 5.
Borneol, 15.
Borith, 449.
Bosch— see Margarine.
Bottlenose whale— see Oil (Doegling).
Bran from cotton seeds, 304.
Brandy fusel oils, 14.
Brassica (rape, colza), various species
of, 348.
Braun and Liebreich, lanolin, 338.
Brez, de, moulded caudles invented
by, 363, 395.
Brine— see Salting out.
Brink, caoutchouc in lubricating oils,
323.
Brin's Oxygen Co. , oil boiling process,
321.
Bromine absorption, 26, 176-179.
,, reaction, forming propiolic
acids, 31, 32, 45.
Bromo substitution derivatives — see
Substitution.
Bruijn, de, and von Leent, oleore-
fractometer, 51-53.
Buccia (olive marc), 343.
Buisine, beeswax, 269, 358.
Bursty n's method, 118.
Butter, animal, 174, 298.
„ ,, (ewes', goats', por-
poises'), Reichert
number of, 174.
,, cow's, adulteration of, 310.
„ fat of, 3, 9, 299.
,, ,, ,, acids obtainable
from, 20, 25, 70.
,, ,, ,, Hehner number,
166, 310.
,, ,, ,, iodine number,
181-134, 310.
,, ,, ,, melting point, 67-
70.
,, ,, ,, refractive power,
51-53.
,, ,, ,, Reichert number,
174, 310.
„ ,, ,, saponification
equivalent, 160,
310.
,, ,, ,, solubility, 54-56.
,, ,, ,, specific gravity,
88-92.
,, ,, quality of, 303.
,, ,, salt contained in, 123.
,, ,, sweetening rancid, by
washing with water, 261.
Butter, cow's, water contained in, 122.
,, general nature of, 1.
,, mineral (antimony, tin), 1.
, , vegetable (vegetable fat, veget-
able tallow), 2, 6, 47.
„ ,, class, 282, 295.
Butters, vegetable, expression oleines
from — see Oleines.
?„ ,, lesser known, 295-298.
Butters, vegetable —
Andiroba fat — see Oil (carapa).
Bassia fat (Illipe butter, Mahwa
butter), 21, 56, 67, 87, 241, 243,
295, 363.
Bay berry fat — see infra Laurel
butter.
Borneo tallow (Malayan tallow,
Fever nut butter), 242, 296.
Butter nut fat, 297.
Cacao butter, 21, 241, 295.
,, chemical properties,
160, 174, 181-184.
,, physical properties,
55, 56, 67-70, 87,
88, 91.
,, theobromic acid in,
21, 22.
Carapa fat — see Oil (carapa).
Chinese (Stillingia) tallow, 21, 70,
295, 363.
,, ,, extraction by hot
water process,
201.
,, yield of, 242.
Chequito butter, 297.
Cocculus indicus fat, 297.
Coker butter — see Oil (cokernut).
Copra butter — ,, ,,
Caumou butter — xee Oil (comnu).
Dika fat, 2, 20, 242, 295.
Fever nut butter — see supra Borneo
tallow.
Fulwah butter (Indian butter), 242,
295.
Gal am butter — see infra (Shea
butter).
Goa butter (Kokum fat, Mangosteen
oil), 68, 242, 296.
Illipe butter — see supra Bassia fat.
Indian (Fulwa) butter— see supra
Fulwah butter.
Karanja butter, Korinje butter
(Ponga butter, Ponga oil, Poondi
oil), 242, 296.
Kokum fat — see supra Goa butter.
Laurel butter (Laurel oil, Bayberry
fat), 20, 56, 68, 181-184, 243, 296.
Macaja butter, 243, 297.
Mafura tallow, 243, 296.
534:
INDEX.
Butters, vegetable —
Mahwa butter — see supra Bassia
fat.
Malayan tallow — see supra Borneo
tallow.
Malabar (Piney) tallow, 70, 160,
244, 295, 363.
Myristica butters, 295.
Nutmeg butter — see Oil (nutmeg).
Ochoco fat, 297.
Ocuba fat, 295.
Otoba fat (Otoba wax), 243, 295.
Palm butter — see Oil (palm).
Palm kernel (Palm nut) butter — see
Oil (palm kernel).
Para butter (Assai oil), 297.
Pekea butter (Piquia fat) — see Oil
(piquia).
Persea fat— see Oil (alligator pear).
Phulwara fat — see Fulwah butter.
Pichurim bean fat, 20.
Piney tallow — see supra Malabar
tallow.
Ponga butter— see supra Karanja
butter.
Poona fat — see Oil (calabar bean).
Rambutan tallow, 296.
Sawarri (Souari) nut butter, 297.
Shea (Galam) butter, 2, 21, 70, 71,
160, 242, 295.
Sierra Leone butter, 244, 296.
Soapberry butter (Soap tree fat),
244, 297.
Soudan butter, 297.
Stillingia tallow — see supra Chinese
tallow.
Tacamahac fat— see Oil (calabar
bean).
Tangkallak fat, 244, 297.
Ucubafat (Ucuba wax, 295.
Virola fat, 68, 295.
Veppam fat— see Oil (zedrach).
Butterine (butter substitutes ; arti-
ficial butter) — see Margarine.
Butyrin (butyric triglyceride), 9,
,, not contained in butter, 9.
CABBAGE palm oil— see Oil(arecanut).
Cacao butter— see Butters, vegetable
(Cacao butter).
Cadmium salts, use in refining oils, 263.
Cailletet, bromine reaction, 177.
,, soap analysis, 507, 508.
Cake, cold press— see Cold press cake.
,, filter— see Filter cake.
,, hot press — see Hot press cake.
Cake, separation-see Separation cake.
Cakes, linseed, &c.— see Oilcakes.
,, moulded, 221-223.
Calcium chloride, use of, in grease
recovery, 271.
,, sulphate, formed in decom-
position of rock, 366.
Calculations, composition of mixtures..
172.
,, of rock, 372.
,, ,, of separation
cake, &c., 378.
,, respecting alkaline leys
and composition of
soaps, 421-426, 454-
456, 464-466.
Cambaceres, bi-aided wicks, 394.
Camphor, acids from, 25, 32.
,, analogues, 3, 6.
,, Borneo, 15.
,, sodium, oxidation of, 25.
Camp, moulding wheel, 398.
Candle polishing, 405.
Candle stearine, 110, 230, 393.
,, ,, breaking grain of, 368r
397,401.
,, ,, crystallising — see
Separation cake.
,, „ manufacture, 364-388.
,, ,, ,, autoclave lime
process, 364,
373-376.
,, ,, ,, conversion of red
oils into stear-
ine, 142,386-388.
,, ,, ,, cold pressing —
see Cold press.
,, ,, „ hot pressing —
see Hot press.
,, ,, „ hydrolysis by
water under in-
creased pres-
sure, 365, 385,
386.
,, ,, ,, open pan lime
process, 364-370.
,, ,, ,, rock (lime soaps)
366, 371-374.
,, ,, ,, sulphuric acid
processes, 365,
380-385.
,, ,, ,, unsaponified fat,
&c. — see Un-
saponified.
„ „ » yield, 368, 370-
374.
,, ,, mixed fatty acids — see
Acids, fatty, mixtures
of; Melting points.
INDEX.
535
Candle wicks— see Wicks.
Candlemaking materials, 302, 363.
,, processes, basting wax
tapers, &c.,389.
,, „ dipping by hand,
:i90, 391.
,, ,, dipping by machine,
391-394.
,, ,, drawing wax tapers,
spills,&c., 389,407.
,, ,, manipulation re-
quired in moulding
with various ma-
terials, 401.
,, ,, moulding by hand,
395-398.
,, ,, moulding by ma-
chine, 398-406.
,, „ pouring, 388, 389.
,, ,, threading wicks,
397, 399, 400, 406.
,, ,, trimming, 389.
,, ,, turnover machine,
405.
Candles, ceresin, ozokerite, and par-
affin, 363, 364, 401, 402.
,, composite, 364, 402.
, , early forms of, 312, 313, 362,
390, 391.
,, hollow, 402, 405.
,, medicated, 407.
,, self-fitting butt end, 402.
,, spermaceti (sperm), 360,
363, 402.
,, spiral, 402.
,, standard (photometric),
402.
,, stearine, 395, 401.
„ tallow, 363, 402.
„ tinted, 390, 401, 405.
wax, 301, 362-364, 389.
Caoutchouc, use in lubricating oils,
323.
Capillary tubes (m elting points) ,60-63.
,, (friction coefficient),
107, 109.
Capric aldehyde, 14.
Carapin, 296.
Carbolic acid— see Phenol.
„ soaps, 6, 477, 505, 506.
,, soaps, valuation of
phenoloids in, 506.
Carbon dioxide, atmosphere of, for
cod liver oil extraction, 248.
Carbon disulphide as solvent, 55, 123,
124,231-236,252,
254, 337, 339, 343.
,, diluent for sulphur
chloride, 155.
Carbon disulphide lamp for disinfect-
ing, 407.
,, ,, " sulphocarbon
oils " extracted
by, 344, 408.
Carbon tetrachloride as solvent, 55, 236
Carbonates, alkaline, direct saponifi-
cation by— see Alkaline carbonates,
Sodium carbonate.
Carnauba wax — see Wax (Carnauba).
Carriage grease— see Lubricants.
Carriers of oxygen (driers), 129, 264.
Cart grease — see Lubricants.
Casein in butter, 123.
Cast iron less corroded than wrought
by fatty acids, 277.
Castor beans, decortication of, 224.
Castorol (castoreum), 17.
Cattle food, 303 — see also Oilcake.
Caustic soda — see Soda, caustic.
Causticising alkaline leys, 409-414.
,, boiling process, 412.
,, cold process, 411.
,, under pressure, 413,
Centigrade scale, 57-60.
Ceresin (cerasin), 2, 88.
,, ,, detection of, in
beeswax, 359.
Cerolein, 358.
Ceroxylin, 301.
Cetaceans, oil from blubber of— see
Oils (cetacean).
Cetyl cyanide, margaric acid from, 21.
Cetylic ethers, 4, 7.
Chandlery (candlemaking trade), 363.
Charcoal, use of, in clarifying and
decolorising oils, &c., 255, 263,
269 — see also Animal charcoal.
Charring of wicks — see Wicks.
Chateau, colour reactions, 142, 151.
Chattaway's tube, 120.
Chemical changes during boiling, 317.
,, ,, during drying of oils
— see Oils (drying of).
Chevreul, researches on fats, 309.
Chevreul and Gay Lussac, candle
material, 365.
Chevreul-Milly process, 365.
Chequito, 297.
Chilling baths, 66, 67.
,, effect on viscosity, 106.
Chimneys (lamp), 313.
China clay as adulterant, 123, 355, 359.
,, (antifriction), 328.
Chinese wax— see Wax (Chinese).
Chlorate, potassium, use of, in bleach-
ing oils, &c., 264, 266.
Chloride of soda for soap bleaching,
267.
536
INDEX.
Chlorine, action 011 ethylene, 26.
,, bleaching by means of, 264-
267, 364.
,, gas, test for fish oils in
linseed oil, 352.
Chloroform as solvent, 17, 55, 231, 359.
Chlorophyll, 49, 50.
Chloro substitution derivatives — see
Substitution.
Cholesterol, allied bodies, and their
ethers, 3, 6, 16, 17,259.
,, and its ethers in York-
shire grease, 272-276.
,, determination of, in
lubricants, 329.
,, ethers, 17.
,, extraction from oils,
119-121.
lanolin, 337-339.
,, occurs in de"gras, 336.
,, ., liver and cetacean
oils, 17, 292.
,, ,, suint, 337.
Choline derivatives— -see Lecithin.
Chromate, processes for bleaching
oils, wax, &c. — -see Bi-
chromate.
,, reaction with glycerol —
ste Glycerol extraction
(valuation by bichro-
mate process).
Chrome recovery, 265.
Chromium compounds as driers, 314.
Cierges (altar candles), 389.
Cinchol, 22.
Claritication — nee Oils (clarification).
Clarke, oils boiled with manganese
driers, 314.
Clark's soap test for hard water, 485,
508.
Classification of oils, &c., according
to chemical com-
position, 5.
,, ,, according to com-
position, sources,
and texture, 281
302.
,, ,, according to rela
tive density, 89
92.
,, ,, according to sapo
nification equiva
lents, 158.
,, ,, according to uses
302-339.
,, of soaps according t<
alkalinity, 512.
"Clay, China— see China clay.
, , use of, in refining oils, &c. , 255
Cleansing engine waste, 237.
>loez, elseococca oil, 291.
)lose soap, 468, 473.
,, test (flashing point), 126.
)loth dressing, use of oils for, 302
Coagulate (grease recovery), 271, 272.
Coagulation of mucilage and albu-
minous matters — see Oils, clarifica-
tion of.
Joaltar oils — Sfc Oils (coaltar).
)obalt compounds as driers, 314.
Cochineal as indicator, 420, 497.
Jod livers, extraction of oil from, 247.
Joefficient of expansion of glass, 77.
oils, 79, 92-94.
,, friction in capillary tubes, 107.
,, ,, Traube's apparatus, 109.
ogan's process (oil refining), 259.
ohesion figures, 48, 345.
Coils, steam - see Steam (wetand dry).
?'0kernut, machine for splitting, 224.
,, oleine — see Oleine (cokernut).
,, spelling .of word, 3.
,, stearine— see Stearine (coker-
nut).
^old drawn oils — see Oils (cold
drawn).
,, press cake, 375.
,, ,, (candle stearine), 231,
355, 368.
, , process soaps — see Soap-
making.
Colloidal mucilage, 255.
, , state of soap, 458, 466, 481, 485.
,, ,, facilitated by presence
of alcohol,
sugar, glycerol,
458, 481.
,, ,, ,, by use of castor
oil, 481.
,, ,, ,, by use of potash
instead of soda,
459, 481.
Colorimeter, 50.
Colour of boiled oils, 315.
oils, 49, 263, 341.
Colour reactions with nitric acid, 139.
153.
,, ,, sulphuric acid,
151-153.
,, ,, zinc, chloride, &c.,
141, 151-154.
, , of seal, whale, liver,
arid fish oils, 294.
Colouring matters contained in oils,
49, 263.
,, ,, for candles, 405.
Colza (rape, coleseed), various species
of, 348.
INDEX.
537
Combustion, destruction of noxious
smells by, 247, 250.
Composite candles — see Candles.
Composition of mixtures, calculation
of, 172.
,, soaps by analysis — see
Soaps, commercial.
,, soaps, calculated — see
Calculations.
Compound ethers, 3, 4, 15.
,, ,, saponification equi-
valent of, 158.
,, ,, synthesis of, 13, 17-
Condensed ricinoleic acids — see Poly-
merised.
Congealing temperatures — see Melt-
ing points.
Consistency of elaidin formed — see
Elaidin ; also Classification
according to chemical na-
ture, &c., pp. 281-300.
,, of oils, &c., 47.
,, tester, Legler's, 139.
Cooling pans (candle stearine), 366.
Copper and nitric acid test, 137, 139.
,, compounds as driers, 314.
,, contained in glycerine, 515.
,, in oils, 121-124.
, , soaps, use of, in refining, 263.
,, sulphate, use of, in refining,
256, 263.
, , test for drying oils (Hiibl), 133.
,, test for sugar in soaps, 505.
Coppers for soap boiling — see Kettles.
Coprah (copra), crushing and grind-
ing appliances, 219-221, 224.
Correction for anhydro derivatives,
170.
,, ,, errors of hydrostatic
balance and hydro-
meter, 82-84.
,, ,, free fatty acids, &c.,
170.
,, ,, impurities (alkalin-
ity), 419.
,, ,, temperature (specific
gravity), 79.
Corrosion of bearings, &c. — see Acids,
free fatty (detrimental
effects of), and Acids
(mineral).
,, ,, iron by fatty acids, 277.
Cosmetics, oils used in preparation
of, 302.
Cottonseed, decortication of, 224.
, , stearine — see Stearine (cotton-
,, utilisation of a ton of, 304.
Cowles, candle moulding machines, 1 04
Cracklings, 246.
Crampton, expansion of oils, 93.
Creosote oils, 2, 451.
Jresol, 6, 16.
"ressonnieres', A. and E. des, drying
soap, 447.
Crocodile fat, 299.
Cross and Bevan, melting point de-
termination, 64.
ZJrotonol, 288.
Cruciferous plants, sulphurised oils
from, 123, 154.
Crushing rolls, 215, 218-220.
Crutching (soap), 438-440
rystallisation, fractional, separation
by, 112.
,, from solvents, 23.
,, of separation cake — see
Separation cake,
rystallising pans (stearine), 367.
Culinary uses of oils and fats — see
Oils (cooking).
Cupreol, 16.
Curbs, 432, 433, 453, 469.
Curd soap — see Soapmaking.
Curriers' grease, 326.
DALICAX'S process (tallow, &c.), 74.
D'Arcet's sulphuric acid process, 249.
Dechan, pharmaceutical soaps, 510.
Decolorising of oils — see Oils, bleach-
ing of.
Decomposing pan, stearine, 365.
Decortication of seeds, &c., 223-225.
,, ,, Dudley and Perry's
chemical process,
225.
Deering, free acids in rancid tallow,
355.
Degras, 336.
Degrees (alkalies), English, French,
and German, 420, 421.
,, Burstyn's, 119.
,, Centigrade, Reaumur, Fah-
renheit, 58.
Dehydration, formation of isoleic acid
by, 29.
,, of oxystearic acids, 29,
39, 42, 46.
,, of ricinoleic acid, 36.
Deitz, extraction apparatus, 235.
Delphinum phocasna, 20.
Density — see Specific gravity.
Deodorising cokernut oil, 261, 310.
,, soaps, &c., 267 — see Ran-
cid ; Noxious vapours.
Descroizilles, degrees (alkali), 420.
538
INDEX.
Destruction of noxious vapours by
combustion, 247, 250.
Destructive distillation — see Distilla-
tion.
Determination of fat in seeds, &c. —
see Yield.
Detrimental effects of free fatty acids
— see Acids (free fatty).
Detrimental effects of free mineral
acids — see Acids (mineral).
Diagometer, 53, 347.
Diallyl, oxidised to an erythrol, 44.
Dibromcamphor, 32.
Dibromides of acids, &c., 27, 29-31,
41, 43, 44, 176.
Dibromo substitution derivatives-
see Substitution.
Dichlorides of acids, &c., 26, 29, 31.
Dichloro substitution derivatives —
see Substitution.
Dichromate, bleaching with — see
Bichromate.
Dieff and Reformatsky, ricinoleic
acid, 40.
Dierucin, 11.
Dieterich, iodine number of linseed
oil, 350.
, , specific gravity of fats, 88, 355.
Digester, for extracting bone fat, 252.
,, Wilson's, for rendering tal-
low, &c., 250.
Diglycerides, 10, 468.
,, formed by action of sul-
phuric acid, 144-147.
,, synthesis of, 11.
Diglycerol, 8.
Diiodides of acids, &c., 26, 179-186.
Diiodo substitution derivatives — see
Substitution.
Dikafat— see Butters (vegetable).
Diminution in density with rising
temperature, 92-94.
Dippel's oil, 2.
Diricinolein sulphuric anhydride,
147.
Disintegrating machines, 224.
Dissolved impurities, 256.
Distearates, 23.
Distearin, 468.
Distillation acetyl number, 198.
destructive, 2, 3, 5.
Heyl's apparatus, 234.
of carbon disulphide solutions,
234-239, 254, 339.
of castor oil, 20, 25, 40.
of dioxystearic acid, 42, 46.
of glycerine, 513-516.
of oxystearic acid, 25.
of ricinoleic acid, 36, 40.
Distillation of spirit (transparent
soap), 446.
,, of turpentine spirit (Mein-
ecke's rosin soap), 473.
,, under diminished pressure,
14, 20, 21, 25, 28, 29, 34,
36, 40, 41, 113.
,, under diminished pressure;
technical processes, 383.
,, with superheated steam, 110,
113, 262, 271, 277, 278, 337,
513, 514.
,, with superheated steam, plant
used for, 382-386.
,, with wetsteam, 22, 112,173-176
— see also Reichert's test.
Distilled grease (Yorkshire), 277.
,, oleines — see Oleines (distilled).
Dog fat, 299.
DogH sh liver, extraction of oil f rom,247.
Dragon's blood, 19.
Driers, 129, 262, 314-317.
Dripping, 91, 303.
, , tallow adulterated with, 354.
Dry fusion, rendering animal fats by,
246.
,, steam — see Steam.
Drying soap, 438, 447.
Dubbin, 326.
Dubrunfaut, sulphuric acid process,
380.
Dudley and Perry, chemical decorti-
cation, 225.
Dugong blubber, extraction of oil
from, 247.
Dunn, air blast in soap boiling, 433.
, , boiler (hydrated soaps, &c. ), 463.
Dussauce, ley tanks lined with lead,
412.
Dutch liquid, 26.
Dyer, linseed cake, 214.
Dyestuffs for candles, 405.
EARTHNUT — see Oil (arachis).
Earthwax — see Wax (mineral).
Edgerunners, 215, 218-221.
Edible uses of oils and fats, 302-312.
Edinburgh wheel, 391.
Effect, detrimental, of free fatty
acids— see Acids (free fatty).
,, of light on physical properties
of oils — see Light (effect of).
Efflux viscosity — see Viscosity.
Egg, white of, used in clarifying
candle stearine, 370.
Elseococca vernicia — see Oil (Elseo-
INDEX.
539
Elaidin reaction, 28, 40, 341.
,, ,, methods of working,
137-139.
,, ,, solubility diminished
by, 55.
Elbow press, 202.
Electrical conductivity, 53.
,, method (melting points), 65.
Elevators, 221-225.
Ellinger, Danish butter, 53.
Ellwood, Valenta's test, 57.
Enfleurage, 302.
Engine waste, grease from — see
Grease.
Engler, viscosimeter, 101.
EnglerandKunkler, viscosimeter,101.
English degrees (alkali), 420.
Entozoa present in inferior margarine,
308.
Envelopes (oil pressing), 217, 221.
Equivalent quantities of soda and
potash, 425, 426.
Error due to neglect of expansion, 77,
78.
Errors, tables of, construction, 82-84.
Equivalent, mean, of fatty acids— see
Acids (fatty).
, , saponification — see Sa-
ponification equivalent.
Erucin (erucic triglyceride), 11.
Erythrol, 4.
Erythrols from diallyl hydrocarbons
by oxidation, 44.
Eschwege seife, 461.
Essential oils— -see Oils (essential).
Ester number (Esterzahl), 162, 195.
Estrayer cylinder (oil press), 204.
Ether as solvent for lead salts, 112,
128, 136, 356,
376, 501.
,, oils, &c., 55, 119-
124, 231, 262,
273, 328, 359,
495-497, 501-503.
Ether, petroleum — see Petroleum
ether.
Ethers, compound— see Compound
ethers.
Ethyl acetate, 4.
,, linolate, 34.
Ethylene, action of chlorine on, 26.
,, diacetate, 4.
Eugenol, 194.
Evaporating point (lubricating oils),
325.
Evrard, alkaline tallow rendering
process, 249.
Examination of oils, &c., general
scheme for, 124.
Expansion of glass, 77.
,, ,, correction for, 77, 78.
,, oils, &c., Allen's results,
92.
,, ,, Crampton's re-
sults, 93.
,, ,, Lohmann's re-
sults, 94.
,, ,, Wenzell's re-
sults, 93.
Experimental laboratory press, 213.
Expression in stages, 212.
Extraction of oils by solvents, ap-
pliances for, 232-240.
Extractive matters, fermentation,
causes hydrolysis, 10.
FAHRENHEIT scale, 57-59.
Fahrion, boiled oil, 135.
Fan (soapboiliug), 433, 434, 460, 469.
Farina as adulterant of fats, 123 — see
Starch.
Fat, animal, class, 282, 298.
,, nature of, 1.
,, uiisaponilied, determination of,
119.
Fats, animal, expression of oleines
from, 299.
,, ,, from birds, 298.
,, ,, from milk (animal but-
ters), 174, 298-see
also Butter (cow's).
,, ,, from reptiles, 299.
,, ,, refining and bleaching,
254-268.
,, ,, rendering of, 245-251.
,, ,, tallow, lard, butter
class, 282, 298.
,, vegetable — see Butters, vege-
table.
Fatty acids — see Acids, fatty.
,, matters in seeds, nuts, &c.,
115, 237-244.
Fawsitt, sulphur chloride and oils,
155.
Ferrous sulphate as decolorising
agent, 264, 269.
,, ,, used in soap mot-
tling, 471.
Fibre from cotton seeds, 304.
Ficus gummiflua, 14.
,, rubiginosa, 16.
Field, Leopold, candle nut oil, 287.
,, candles, £c., in the Ro-
man period, 363.
,, lamp chimneys, 31 3.
,, soaps, 509.
540
INDEX.
Field, Leopold, spermaceti, 360.
,, steariiie plant, 369, 382.
,, wax bleaching, 266.
Figging of soft soap, 459.
Filling (soap)— see Soapmaking.
Film test, 133, 351, 352.
Filsinger, soap analysis, 494.
Filter cake (red oils), 376, 377.
Filtration of oils without extra pres-
sure, 257, 264.
Filter presses, 226-229.
,, use in clarifying ex-
pressed oils, 228,
254-257.
,, ,, in purifying red
oils, 231, 376.
Fiukener on Dalican's method, 75.
Firing point (ignition point), 329.
First runnings, 304.
Fish livers, extraction of oil from, 247.
,, manure from residues of fish oil
extraction, 249.
Fit (coarse or fine) of soap, 471.
Fitted soap — see Soapmaking.
Fixed oils — see Oils (fixed).
Flambeau, 312, 362.
Flashing point, 125-128.
,, of coaltar oils, &c., 328.
,, of lubricating oils, 325-
qoq
o^y.
,, ,, insurance, 325.
,, of oleine from Yorkshire
grease, 279.
Flavour of oils, &c. , 49.
Flax plant, 349.
Flaxen wicks, 362.
Fleeces — see Wool.
Fletcher, thermhydrometer, 80.
Floating soaps, 441.
Flour as adulterant of fats, 123 — see
Starch.
,, in beeswax, 359.
Fluorescence, 50.
Fob (fitted soap), 471.
Foots, 115, 256, 259, 324.
,, avoidance of formation of, 228.
distillation of, 261, 383.
spermaceti, 261, 360.
utilisation of, 261, 324, 408.
Formula, alkaline degrees, 421.
,, equivalent quantities of
soda and potash, 426.
,, thermometer degrees, 58.
Foxy colour developed, 265, 266, 356.
Fractional crystallisation, 112.
„ distillation, 113.
,, precipitation, 112.
saturation, 112, 113.
Frames (soapmaking), 434-437, 444.
Frederking, oil boiling pan, 316.
Free fatty acids— see Acids, free fatty.
Free fire process of boiling oils, 315.
,, soap pans, 427.
Freezing points — see Melting points.
French degrees (alkali), 420.
Fresenius, absorption of oxygen, 134.
Friction coefficient, Mills, 107.
,, Poiseuille, 107.
Traube, 109.
Fuel from cotton and sunflower
seeds, 304, 305.
Fullers' earth, use in refining oils,
&c., 255.
,, grease, 272, 279.
,, ,, valuation of, 280.
Fusel oil, use in woolscouring, 337.
Fusel oils (fermentation oils) — see
Oils (fusel).
Fusing points— see Melting points.
Fusion with alkalies — see Hydrogen.
GALIPOT resin, 88.
Gay Lussac, candle material, 365.
degrees (alkali), 421.
Geitel, stearolactone, 38, 145.
,, sulphuric acid and oils, 144.
,, — see Schepper and Geitel.
Gelatin, removal of, from fish oils, &c.,
256, 263.
,, use of, to remove colouring
matters, &c., 263.
Gellatley, spontaneous combustion,
132.
Geraiiic aldehyde, 15.
Geraniol, 15.
Gerlach, specific gravity of potassium
carbonate solutions, 419.
,, vaporimeter (glycerine
valuation, 519.
German degrees (alkali), 420.
,, sesame —see Oil, Camelina.
,, soap process, 449, 472.
Girard, solubility in alcohol, 54.
Glacial acetic acid test — see Acid
(acetic).
Gladding's process, rosin in soap,
485, 501, 502.
Glass, expansion of— see Expansion.
Glassner, nitric acid test, 141.
Glycerides, 3, 9.
,, determination of, in lub-
ricants, 329.
,, hydrolysis of, in three
stages, 10.
,, iodine absorbed by pure,
180.
INDEX.
541
Glycerides, mixed— see Mixed gly-
cerides.
,, saponification equivalents
of pure, 158.
„ ,, of, in three stages,
468.
., synthesis of, 11.
Glycerine, manufacture of (glycerol
extraction), 513-516.
,, analysis and detection of
impurities, 515.
,, extraction from soap leys,
451, 468, 469,
541.
,, ,, from soap leys, com-
position, 514.
,, ,, from sweet waters,
513, 514.
,, loss in sulphuric acid hy-
drolysis processes, 381.
,, production in candlemak-
ing processes, 311, 366,
373, 385, 513.
, , production in soapmaking
processes, 450, 45 1 ,
466-470.
,, valuation, acetyl process,
8, 191, 516.
,, ,, bichromate process,
8, 516.
,, ,, David's process, 522.
,, litharge „ 524.
,, Muter's ,, 523.
,, ., oxalic acid process,
8, 519.
,, ,, by specific gravity,
516, 517.
„ ,, by tension of vap-
our, 518, 519.
, , yield from ox fat, 311,312.
,, ,, practical, from
various glycerides,
521.
„ ,, theoretical, 162, 195.
Glycerine soaps — see Soaps (special
kinds).
Glycerines (commercial products), 8,
110, 513.
Glycerol, 4, 7, 110, 513. [144.
,, action of sulphuric acid on,
,, ,, heaton— see Acrolein.
,, as standard in viscosi-
metry, 101.
,, calculated yield from tri-
glycerides, 521.
,, crystallised, 7. 514.
,, formation during examina-
tion of oils, 124.
,, ,, from allylic alcohol, 44.
Glycerol, formation on saponifying
adulterated beeswax,
359.
,, ,,011 saponifying adulter-
ated sperm oil, 354.
,, ,, on saponifying Tur-
key red oils, as a test
33-1
,, physical properties of, 7.
,, qualitative tests for, 8, 516.
,, quantitative— .see Glycerine,
manufacture of (valua-
tion).
,, retained in cold process
soaps, &c. , 450,
456-466.
,, ,, calculations respect-
ing, 464-466.
Glycol, 4.
,, from Carnauba wax, 5, 18.
,, ,, defines by oxidation, 44.
Goat's tallow— see Tallow.
Goods, "killing" of, in soapmaking,
433, 468.
,, rancid, deodorising soap made
from, 267.
Goose grease, 68, 184, 298, 299.
Gossage, method of emptying soap
pans, 434.
Graf, theobromic acid, 22.
Grain spirit fusel oils, 14.
Graining soap — see Soapmaking.
Granulating presscake — see Separa-
tion cake.
Grape fusel oils, 20.
Grease, birds, 298.
,, bone— see Bone grease.
,, curriers', 336.
,, distilled, 111 -see Distillation.
„ engine waste, 236, 279, 324.
,, from hot pressing — see Hot
press.
,, from silk soap suds, 279.
,, fullers', 279, 2hO.
,, horse,rnare's — .see Oils (horse).
,, lubricating — see Lubricants.
,, recovered, 262, 270-280.
, , used in soapmaking,
450, 453.
,, recovery by Yorkshire pro-
cess, 272 — see
Yorkshire grease.
,, ,, by lime process, 271.
,, trade refuse (tannery grease.
&c.), 299.
,, ,, used in soap-
making, 409.
,, Yorkshire — see Yorkshire
grease.
542
INDEX.
Greasy rags, spontaneous combustion
of, 132, 133.
Greaves, 246.
Green liquor — see Chrome liquor re-
covery.
Green oil (Yorkshire grease distilla-
tion), 277.
Grills and Schroeder, liquid sulphur
dioxide as solvent, 236.
Grimshaw, phosphated soaps, 476.
, , utilisation of cotton seeds, 304.
Grittner and Szilazi, rosin in soap, 502.
Grb'ger, dioxy palmitic acid, 44.
Ground mica (antifriction), 324.
Groundnut — see Arachis nuts and
Oil (arachis).
Ground plan of 16-press installation,
216.
Gum arabic, Eideal, 108.
,, benzoin, 19.
Gumming of oils, 129, 322, 325.
,, ,, practical test of, 323.
Gwynne, Jones, andWilson, sulphuric
acid process, 380.
H
HAUEMAN, soda crystals in oil refin-
ing, 2GO.
Hagenbach, viscosity, 107.
Hager, specific gravity of fats, 88, 355.
Hairs, hair envelopes, 217, 221.
Handpicking seeds, necessary to ob-
tain standards, 213, 340, 350.
Hartley, acid refining process, 259.
,, manganese sulphate in re-
fining, 260.
Hartley and Blenkinsop, patent re-
fining process, 263, 264, 315.
Hauchcorne, nitric acid test, 140.
Haussknecht, benoxylic acid, 45.
,, brassa'idic acid, 28.
Hawes' boiler (cold process soap),
457, 463.
Hazura, characteristic oxidation pro-
ducts, 128.
,, oxidation of stearolic acid,
36 — see "Benedikt and
Hazura ; Bauer and Hazura.
Hazura and Grlissner, glycerides in
linseed oil, 350,
351.
,, ,, liuolic acid, 35.
,, ,, linolic acid in olive
oil, 344.
,, ,, oxidation of drying
oil acids, 136.
,, ,, ,, of ricinoleic
acid, 40.
Hazura and Griissner, oxidation of
stearolic acid, 45.
,, ,, rule concerning oxi-
dation, 44.
Head matter (whales), 360.
Heat, coagulation of albuminous
matter by, 255, 263.
,, effect of, on oils — see Oils
(effect of heat on).
,, evolution with sulphuric acid
— see Oils (heat evolution).
Hehner, beeswax, 357, 358.
, , glycerine valuation, 516, 522.
number, 113, 157, 166-170,
195, 196, 341.
Heintz, melting point tables, 71-74.
Hell, hydrogen method, 13, 121.
Hempen wicks, 362.
Hersee, soap pump, 434.
Hervieux and Bedard, waggon grease,
327.
Hess, Yorkshire grease analysis, 276.
Hexacetyl derivatives, 37.
Hexbromides of fatty acids, 34-37,
176.
Heyl, distillation apparatus, 234.
Hippopotamus grease, 299.
milk, 298.
Hoffmeister, chilling baths, 67.
Holde, improved flashing point ap-
paratus, 127.
,, iodine absorption of drying
oils, 184, 351.
,, oleorefractometer, 52.
Holt, brassic acid, 29.
Homologous acids, separation of, 112,
113.
Homologues of linolic acid (supposed),
32, 34.
Honig and Spitz, extraction appara-
tus, 120, 239.
Hope, soap analysis, 494, 498, 499, 509.
Horse grease, horse fat — see Oil
(horse).
,, power requisite in oil mill, 215-
217.
Hot baths, 61-65, 80, 95-101.
Hot air bleaching processes — see Air.
Hot press, 231, 368.
cake, 368, 370, 375.
Hubl, beeswax, 358.
,, iodine test— see Iodine number.
,, melting points, 71.
,, modification of Livache's test,
133.
Hubl and Stadler, rosin in soap, 502.
Huiles d'enfer, 344.
tournantes, 116, 344.
Hulls from cotton seed, 304.
INDEX.
543
Hurst, efflux viscosity values, 105.
,, \ralenta's test, 56, 57.
,, viscosimeter, 101.
,, Yorkshire grease, 276-279.
Hyaena fat, 21.
Hydrated soaps — see Soapmaking.
Hydration of anhydrides, &c., 41-43,
45.
,, of isoleic acid, 38.
Hydraulic filter press — see Filter
press.
presses, 207-212, 215-218.
Hydriodic acid, action on isoleic
acid, 30.
,, ,, action on linolic acid,
34.
Hydrocarbons, 2, 3, 5, 54, 90.
, , detection in linseed oil, 352.
,, ,, in olive oil, 347.
„ 5, in rape oil, 349.
,, ,, in Turkey red oils,
335.
,, ,, in wax and sper-
maceti, 359, 361.
,, determination in lubri-
cants, 329.
,, insoluble in glacial acetic
acid, 57.
, , mineral, solid — see Cerasin,
Ozokerite.
,, miscible with blown oils,
320, 321.
,, presence of, in distilled
oleines, &c., 120, 258,
261,274-278,377,378.
,, ,, in engine waste
grease, 279.
,, saturated and unsaturated,
3, 26.
,, separation of, from oils,
119-124.
,, use of, in manufacture of
lubricants, 322-329.
,, used as adulterants, 120,
121, 335, 347-349, 352.
Hydrocarotin, 18.
Hydrochloric acid, evolved from
burning wax tap-
ers, 267, 365.
,, ,, formed in Turkey red
oil making. 331.
,, ,, removal of lime salts
from bone fat by, 256.
,, ,, used in grease re-
covery, 271.
,, ,, ,, in Mege Mouries
process, 308.
,, ,, ,, in oleic acid
valuation, 376.
Hy drochloricacid used with bleaching
powder, &c., in decolorising oils,
&c., 264-266.
Hydrogen, atmosphere of, in cod liver
oil extraction, 248.
,, evolved by fusion with
alkalies, from
acrylic acids, 24.
,, ,, from alcohols, 13, 121.
,, ,, from glycols, 18.
,, ,, from gly collie acids,
37.
,, nascent, as dechlorinising
agent, 31, 35.
,, peroxide as bleaching
agent, 264, 339, 359.
Hydrogenation of acids, 20, 26, 32,
34, 40.
aldehydes, 14, 15.
Hydrolysis accompanies rancidity,
10, 12, 114, 292.
,, but little effected by light,
131.
,, by superheated steam, 10,
110, 125, 261.
,, in autoclaves, &c., 373
— see also Distillation.
,, of condensed ricinoleic
acids, 146, 333.
„ ofoils,&c.,7, 10, 12, 114, 116.
,, of soap solutions, 12, 23,
486-488.
,, of soap solutions, rate
diminished by presence
of alkali, 487.
,, of sulphuric acid com-
pounds, 27, 29, 331, 333.
„ of Turkey red oils, 331-333.
,, water taken up during, 10,
275.
Hydrometer, 77.
,, scales, 84-86.
,, table of errors, con-
struction of, 83.
Hydrostatic balance, 77-79, 81.
,, table of errors, construc-
tion of, 83.
Hydroxylinolein, 136, 137.
ICELAND moss in lard, 306.
Ignition point, 329.
Illipti fat — see Butters, vegetable.
Impurities, systematic examination
for, 124.
Incipient melting and solidifying
points — see Melting point.
544
INDEX.
Increment in weight during drying of
fatty acids, 113.
Increment in weight during drying of
oils, 133.
Indicators in titration, 420 — see
Phenolphthalein, Titration, Cochi-
neal, Litmus, Methyl orange.
Indigo, used to tint soft soap, 459.
Inner anhydrides, 30, 39.
Insolation, effect of — see Light, effect
of.
Insoluble acid number, 168, 195, 341.
,, f atty acids— >ee Acids, fatty,
insoluble.
Installation (16-press), plan of, 217.
Insurance companies and lubricating
oils, 325.
Iodine candles, 407-
,, number (iodine absorption),.
26,34,157,176-186,341.
,, ,, as test of drying
power, 133.
,, ,, effect of light on, 131.
,, ,, lessens as oxysen taken
up, 42, 129,^135, 185.
,, ,, of free acids, 180, 184,
197, 356.
,, ,, of glyceride falls short
of that of free fatty
acid by about 4-5 per
cent., 185, 197.
,, ,, of oils, determinations
of, 181-184, 196.
lodo substitution derivatives — see
Substitution.
Irish moss (antifriction), 328.
Iron, cast, less corroded by fatty
acids than wrought iron, 277.
,, salts, use in refining, 263.
,, soaps — see Metallic soaps.
Isocholesterol, 16, 17.
, , and ether s in Yorkshire
grease, 272-276.
Isoglyceride theory, 12.
Isomerides of dioxybenic acid, 28, 29,
44, 129.
,, dioxystearic acid, 28, 30,
41, 43, 129.
linolic acid, 32, 35.
ofoleicacid, 28, 29, 129.
oxystearic acid, 29,38,39.
oxystearosulphuric acid,
27, 30, 38.
ricinoleic acid, 40, 41.
trioxystearic acid, 40,
43, 44, 129.
Isomerism of brassic and erucic acids,
28, 29.
,, stereochemical, 29.
JACKSON, African oils, 289.
Japanese wax — see Wax (Japanese).
Jean, adulteration of butter, 310.
,, oleorefractometerreadings, 51-53.
,, thermeleometer, 151.
Jellifying of soap solutions, 485.
Johnson & Co., filter presses, 229.
Juillard, Turkey red oils, 147, 330,
333.
KAOLIN as adulterant, 123.
Kauri gum admixed with thickened
oils, &c., 142, 318.
Keg lard, 306.
Kerosene, 2, 5.
Ketones, 3, 6.
Kettles for boiling drying oil, 315, 316.
,, for boiling soap, free fired, 426-
428.
,, for heating crushed seed, &c.,
215, 221.
,, heated by dry steam, 247, 428.
,, ,, by wet steam, 428.
,, skimmer pipe for, 433.
,, square, 433.
,, various older forms of, 429-432.
Kitchen grease, 299, 408.
,, ,, deodorising, 265.
,, tallow adulterated
with, 354.
Kcettstorfer's test (Kcettstorfer num-
ber)— see Total acid number.
Kidney fat (ox), 311.
" Killing the goods," 433, 468.
Knab's superheated steam distilla-
tion plant, 382.
Kohn, qualitative test for glycerol,
516.
Krafft, ricilinolic acid, 36.
,, ricinic acid, 41.
Krafft and Noerdlinger, brassic and
elaidic acids, 28.
Kingzett, glycerine extraction, 514.
Kulp livers, extraction of oil from,
247.
LABOUR requisite in oil mill, 215-218.
Lach, candlenut oil, 287.
,, French candle stearine plant, 386.
Lactucerol, 16.
Lamp for carbon disulphide (disin-
fecting), 407.
INDEX.
545
Lamps, 312, 313, 362.
Langbeck, lanolin 339.
Langlet, thermal areometer, 82.
Lanolin, 274, 336, 337-339.
,, in soaps, 448.
,, manufacture of, 337.
,, sulphurised, 339.
tests of quality of, 339.
Lant Carpenter, lubricating oils, 325.
,, soap analysis, 510.
,, soap boiling, 470.
,, sulphuric acid pro-
cess, 381 , 388.
Lard, 21, 164, 299, 303-308.
,, adulteration of, 306, 307.
„ artificial, 307.
,, damaged, used for soapmaking,
408.
„ free fatty acids in, small when
fresh, 307.
, , iodine number of, 181-184, 307,
356.
,, manufacture of, 306.
,, melting point of. 68, 306, 307.
,, oil — see Oil (lard).
,, Reichert number of, 175.
,, saponification equivalent of,
160, 307.
,, solid suspended matters in, 123.
,, solubility of, 56.
„ specific gravity of, 88-93, 307.
,, stearine (solar stearine) — see
Stearine (lard).
,, unsaponifiable constituents in,
&c., 257, 307.
,, vegetable, 305, 310.
,, water contained in, 122, 307.
Laurent, polarimeter, 50.
Laurie aldehyde, 14.
Laurin, lauric triglyceride, 11.
Lead acetate, use in boiling oils, 262,
314.
„ contained in oils, 121-124, 314.
, , oxide as saponifying agent, 410.
,, oxides as driers, 314.
,, plasters, 410, 485.
, , salts soluble in ether — see Ether
as solvent.
, , salts, use of, in refining, 256, 263.
,, test (Livache's), 133.
Leather currying, leather grease, 302,
336, 339.
Leblanc process of alkali manufac-
ture, 410.
Lecithin, 121, 240, 259.
,, determination of phospho-
rus in, 124, 240.
Leeds, soap analysis, 494.
Lefebre, oleometer, 79.
Leffmann and Beam, Reichert number,
175.
Legler, consistency tester, 139.
Lenz, density of glycerol solution, 517.
Lepenau, leptometer, 106.
Leuner, bonefat extraction apparatus,
253.
Lever presses, 199.
Lever and Scott, carbon tetrachloride
as solvent, 236.
Levinstein, lanolin, 339.
Lewkowitsch, acetylation test and
modification thereof,
189-191, 198.
, , distillation under dim-
inished pressure, 383.
,, rosin in soap, 502-504.
, , Yorkshire grease, 272.
„ analysis
of, 274.
Leys, alkalinity of — see Alkalinity.
, , calculations respectingquantity
and strength of — see Calcula-
tions.
, , causticising — see Causticising.
,, spent— see Soapmaking, Glycer-
ine manufacture.
,, use of, in soapmaking — see
Soapmaking.
Liechti and Suida, sulphuric acid and
oils, 144.
Liebig, distillation of acids, fractional
saturation, 112.
Light coaltar oils, 2.
, , petroleum distillate — see Petro-
leum ether.
Light, effect of, on oils — see Oils, effect
of light on.
, , facilitates air bleaching of wax,
268, 269.
,, polarised (polariscope), 17, 50,
347, 352.
,, ,, sugar valuation in
soap, 505.
Limburg cheese, 20.
Lime, use of, in causticising alkalies
— see Causticising.
,, ,, making railway
grease, 327.
,, ,, recovering grease, 270.
,, ,, refining oils, 256, 261.
,, steariue manufacture,
365, 369.
Lime rosin soap (railway grease), 327.
Lime soap (grease recovery), 271.
,, in candlemaking — see
Candle stearine.
,, in lard, 307.
in lubricants, 324,327,328.
35
546
INDEX.
Limpach, stearolic acid, 36.
Linoleum, 302, 318, 319.
Linolic anhydride, 125.
Linolin (linolic triglyceride), 134, 139.
Linoxyn, 134, 136.
Linseed cake — see Oilcake
Linseed, sources of, 349.
,, usually mixed with hemp-
seed, 349.
Lint, 304.
Litmus as indicator, 420.
Liquid waxes— see Waxes.
Litharge as drier — see Driers.
Livache, comparative action of
driers, 314.
Livache's test, 133, 351, 352.
Livers, fish and shark, &c., extrac-
tion of oil from, 247.
Loading (soap) — see Soapmaking.
Lcewe, melting points, 65.
Lohmann, expansion, 93.
Lubricants, analysis of, 328-330.
, , coarse, 27 1 , 280, 324, 326-328.
,, corrosion by free acids in,
115, 260, 322.
,, for hot rollers (pitch from
Yorkshire grease), 277.
,, greases (cart, carriage, wag-
gon, railway grease, anti-
friction grease, &c.), 325-
329, 409.
., materials used for, 302, 321-
328, 339.
,, use of blown oils for, 320.
„ viscosity of — see Viscosity.
Lubrication, 5, 48.
Lunge and Hurter, Beaume" scale, 86.
,, ,, specific gravity of al-
kalineleys, 416-418.
Lupeol, 17, 259.
M
M 'NAUGHT, pendulum machine, 94.
Magma (grease recovery), 271, 272.
Magnesia as saponifying agent, 379,
410.
,, calcined, use of, in refining,
256, 261.
Magnesium soaps, 121.
Manganese compounds, use of, as
driers, 314, 315.
, , dioxide, use of, in bleach-
ing, 268.
,, salts, use of, in refining,
256, 260-264.
Mangold, glycerine valuation, 521.
Mannitol, 5.
Mansbridge, analysis of Yorkshire
grease, 275, 276.
Manteau Isabelle (mottled soap), 472.
Manure from fish oil extraction resi-
dues, 249.
,, scraps from ox fat, 311, 312.
,, sludge from suds and sud-
cake, 271, 2/2.
Mare's grease— -see Oil (horse).
Margarin, glyceride of artificial mar-
garic acid, 21, 22, 110, 309.
Margarine (Oleomargarine, Butterine,
Artificial butter, Dutch
butter, Bosch, Butter sub-
stitutes), 22, 114, 299, 305,
308-312.
,, cokernut and palmnut oils
in, 310.
,, Hehner number, 166, 310.
,, iodine number, 181, 184, 310.
,, manufacture, 246, 247, 308-
312.
,, manufacture byMegeMouries
process, ;,08.
,, origin of name, 308.
,, Reichertnumber,173,174,310.
,, specific gravity, 88, 91.
, , total acid number and saponi-
fication equivalent, 159.
,, use of oleorefractometer in
detecting, 53.
,, vegetable, 305.
Marine soap - see Soapmaking.
Maritime alkali — see Barilla.
Marix, distillation under diminished
pressure, 383.
Marrow, 21.
Massie, nitric acid test, 141.
Maumene's test— see Oils (heat evolu-
tion).
Meal as adulterant, 123.
Mean equivalent — see Acids, fatty,
(mean equivalent).
Meats from cotton seed, 304.
Mechanical viscosity testers, 94.
Mege M curies process, 308.
Meinecke's process (rosin soap), 473.
Meissl, Beichert number, 53, 174.
Melting points (Congealing, Solidifica-
tion, Fusing, Freezing
points), acetic acid
series, 20.
,, acrylic acid series, 25.
,, alcohols, 14.
,, candle stearine, 370,375. 377.
,, cholesterol and allied
bodies, 17.
,, congealing of lubricants,
67, 325.
INDEX.
547
Melting points, determination of,
60-67.
„ distilled fatty acids, 384.
,, erucic and brassic acid
derivatives, 29.
,, mixed fatty acids,69-76,341.
,, oils and fats, &c., 67-69.
,, polyhydroxylated stearic
acids, 43.
,, propiolic acids, 32.
,, synthetic triglycerides, 11.
Mercuric bromide, use of, in Hiibl's
test, 179.
,, nitrate, colour test, 151.
Mercury and nitric acid test, 138.
Merryweather & Sons, improved dry
heat rendering arrangement, 247.
Metallic salts, used in refining oils,
262, 263.
soaps, detection in olive oil, 347.
formed in paint, 135.
in lubricants, 324, 328.
in oils, &c., 121-124, 315,
324, 485.
in ordinary soaps, 410.
iron soap in mottling, 472.
isolation of metallic con-
stituent (analysis), 328.
Methyl esters (brassic and erucic), 29.
,, number (methyl iodide test),
157, 191-194, 196.
,, orange as indicator, 420, 497,
507.
Methylic ethers, 5.
Mica (antifriction), 324, 328.
Michaud Freres, glycerine manufac-
ture, 515.
Milk fats, composition unlike that of
body fats, 298.
,, Reichert number, 174.
Milling machinery (toilet soaps), 446-
448.
Mills, viscosity, 107, 108.
,, W., oil bleaching, 264.
Mills and Akett, Mills and Snodgrass,
bromine absorption, 177.
Milly, de, candle material, 365.
,, wicks, 394.
Mineral acids, injurious effect of — see
Acids, mineral.
Moellon, 336.
M oiler, improved cod liver oil extrac-
tion process, 248.
Moinier and Bontigny, candle stear-
ine, 369.
Monoglycerides, 10.
,, synthesis of, 11.
Morawski and Demski, iodine absorp-
tion, 184.
Morfit, oleine soap process, 453.
,, steam series of soap pans, 432.
,, steam twirl, 428, 429.
,, ,, use in making lub-
ricating grease, 325.
,, ,, use in making resin-
ate of soda, 453.
Mortars (mortuary candles), 406.
Mottled soaps — see Soapmaking.
Moulding, Moulding machine (oil
pressing), 215, 221-223.
Mountain ash berries, 32.
Mucilage (vegetable mucus), deter-
mination of,
118-123.
,, ,, removal from
oils— see Oils
(clarification).
Miiller- Jacobs, sulphuric acid and
oils, 144.
Muirhead and Alder Wright, zinc
i chloride and oils, 141.
Mulder, drying oils, 134, 136.
Muntz, thermal arceometer, 82.
Muter, colour reactions, 142.
,, determination of oleic acid,
376.
,, olein tube, 376.
,, specific gravities, 88.
Muter and Koningh, separation of
fatty acids, 307, 356.
Mutton tallow — see Tallow.
Myricin (myricylicpalnritate), 4, 358,
359.
Myristic aldehyde, 14.
Myristin (myristic triglyceride), 11.
N
NATRON, 409, 449.
Natural naphtha— .see Oils (mineral).
Negative alkalinity, 498, 499.
Negur (negre, nigre, nigger) of fitted
soaps, 471.
Neill & Sons, modern soap coppers,
433.
,, rem citing pans, 441.
Neutral oil (Yorkshire grease), 276-
279.
Neutralisation number of fatty acids,
164, 169.
,, ,, mixed acids, calcu-
lation of composi-
tion from, 172.
Nightlights, 312, 402.
,, manufacture of, 406.
Niin fat, Niin wax, 302.
Nitric acid test, 139, 153, 294, 341.
548
INDEX.
Nitric acid as standard acid in soap
analysis, 497.
,, use of in wax bleaching
264, 265.
Nitrous acid test — see Elaidin reac-
tion.
Nocciulo (olive marc), 343.
Noerdlinger, oilcakes, 114, 214.
„ refining oil, 263.
,, see Krafft and Noerd-
linger.
Norton and Richardson, linolic acid,
34.
Noxious smells evolved in rendering
animal fats, 247, 249.
Number, acetyl — see Acetylation test.
, , ester — see Ester number.
, , free acid — see Acids, free fatty.
,, Hehner— see Hehiier number.
,, Hiibl— see Iodine number.
,, iodine — see Iodine number.
,, insoluble acid — see Insoluble
acid number.
,, Koettstorfer — see Total acid
number.
, , methyl — see Methyl number.
,, neutralisation — see Neutrali-
sation number.
,, Reichert — see Reichert num-
ber.
,, saponificatioii — see Total acid
number.
,, soluble acid — see Soluble acid
number.
, , total acid — see Total acid num-
ber.
, , volatile acid — see Volatile acid
number.
Nuisance in rendering fats — see
Noxious smells.
Nutmeg butter— see Oil (nutmeg).
Nuts strung together used as candles,
363.
,, yield of fat from various kinds
of, 241-244.
OAKBARK infusion, use of, in refining,
256, 263.
Octylic ethers, 5, 20.
Odour of oils, &c., 49, 341.
,, rancid, removal of — see Ran-
cid, R,ancidity.
CEnanthol (oenanthic aldehyde), ac-
tion of acetic anhydride on, 25.
, , formed by heating castor oil, 40.
,, hydrogenised to heptylic alco-
hol, 14.
CEnanthol, oxidised to heptoic acid, 20.
Oil. For the specific gravity and other
physical properties of each oil
severally, vide Chaps, iv., v.
(pp. 47-109).
,, For the chemical properties and
reactions, vide Chaps, vi., vii.,
viii. (pp. 110-198).
,, acajou — see Oil (cashew).
,, adul, 288.
,, alligator pear (avocado oil,
persea fat), 296.
,, almond, 3, 19, 241, 257, 283.
class, 281, 282.
,, ,, detection of adultera-
tions, 347t
,, anchovy, 294.
,, angelica, 37.
,, anise, 192, 194.
,, apricot kernel, 283.
,, American walnut — see Oil (hic-
kory nut).
,, arachis (earthnut, groundnut,
peanut), 21, 25, 241,
258, 283.
,, ,, adulteration of, 347.
,, ,, detection of, in olive oil,
344.
,, ,, doubt as to existence of
hypogseic acid in, 24, 111.
,, ,, natural variations in com-
position of, 111.
,, ,, relative price of, 342.
,, ,, tests for, in olive oil, 344.
,, ,, use of, in soapmaking —
see Soapmaking.
,, ,, used as lubricant, 322.
,, arctic sperm — see Oil (doegling).
,, areca nut, 241.
,, argan, 288.
,, assai — see Butters, vegetable
(Para butter).
,, avocado, 296.
,, bankulnut— see Oil (candle nut).
,, beechnut (beechmast) 241, 283.
,, belladonna seeds, 241.
,, ben (behen), 21, 25, 241, 283.
„ detection of adulterations, 347.
benne — see Oil (sesame^,
bitter apple — see Oil (colocynth).
blackfish, 293.
bladdernut, 288.
boma nut, 288.
bone — see Bone fat.
bottlenose whale — see Oil (doeg-
ling).
brazil nut (castanha nut), 241,
242, 288.
breadnut, 289.
INDEX.
549
Oil, cabbage, 115.
,, calabar bean (poon seed, dilo,
domba, pinnay, tamanu oil ;
poona fat, tacamahac fat), 241,
291, 296.
,, camelina (German sesame", gold
of pleasure), 241,
286.
,, ,, ,, tests for sulphur in,
123.
,, ,, ,, use in soapmaking
— see Soapmaking.
,, canary— see Oil (Java nut).
,, candle nut (bankulnut, kekune),
241, 287.
,, carapa nut (crab wood nut oil,
touloucoona oil, coundi oil,
andiroba fat), 242, 296.
caryocar, 297.
cashe\v (acajou), 241, 289.
cassia, 19.
castanha — see Oil (brazil nut),
castor, 14, 20, 25, 43, 241, 285.
,, action of sulphuric acid —
see Oils (Turkey red).
,, zinc chloride on, 141.
blown, 321.
class, 281, 284.
effect of exposure to air, 136.
,, heat on, 40.
extraction by hot water
process, 200.
relative price of, 342.
soap — see Soapmaking.
soluble, 188, 321 — see Oils
(Turkey red).
,, use in soapmaking, 408.
centaury, 242.
chamomile, 14, 25.
charlock, 241.
chaulmoogra, 20, 242, 297.
cherry kernel, 283.
Chinese cabbage, 284, 348.
chironji, 242, 289.
cinnamon, 19.
cloves, 194.
cod (lubricating), 330.
cod fish and cod liver, 257, 258, 294.
, , , , extraction of, 247,
248.
,, ,, extraction of, ex-
clusion of air dur-
ing, 248.
,, ,, relative price of,
342 — see Oils
(liver, fish liver).
,, ,, used for soapmak-
ing— see Soapmaking.
cokenmt, 20, 241, 257, 258, 295.
Oil, cokernut, deodorisingrancid,261,
310.
,, ,, separation of coker
stearine from, 231,
305 — see Stearine
(cokernut).
,, „ spelling of, 3.
,, ,, use in soapmaking — see
Soapmaking.
,, colocynth (bitter apple, 241, 288.
,, colza (cole, cole seed, kohlsaat),
348— see Oil (rape).
,, combo nut, 242.
,, copra (coprah)-see Oil (cokernut).
,, corn poppy, 242.
,, cotton seed, 241, 257, 258, 286.
,, ,, absorption of oxygen
by, 330.
,, ,, action of sulphuric
acid on — see Oils
(Turkey red).
,, ,, adulteration of, 347.
,, ,, adulteration of lard
with, 306-308.
,, ,, as lubricant, 322,325.
,, ,, Becchi's test for —
see Becchi's test.
,, ,, blown, 319.
,, ,, clarifying and refin-
ing, 255-263.
class, 281, 286.
,, ,, refined, use as edible
and cooking oil, and
as adulterant of sa-
lad oils, 267, 304.
,, ,, relative price of, 342.
,, ,, use in soapmaking —
s<>e Soapmaking.
,, ,, utilisation of a ton of
cotton seeds, 304.
,, coumu nut (coumu butter), 289,
297.
„ cow parsnep (heracleum), 5, 14, 20.
, , crab wood nut-see Oil (carapa nut).
,, cress seed, 241, 286.
,, croton, 20, 25, 287.
,, curcas (purqueira, purgir, jatro-
pha), 20, 285.
,, datura (strammonium seed), 21,
244.
,, dilo, 291 — see Oil (calabar bean).
,, doegling (bottlenose whale, arctic
sperm), 3, 25,258,300,360.
,, ,, doubt as to existence of
doeglic acid in, 24.
,, ,, relative price of, 342.
,, ,, yields spermaceti of higher
melting point thancachelot
spermaceti, 360.
550
INDEX.
Oil, dogfish liver, 247, 294.
,, dogwood berry, 288.
,, dolphin, 293, 301.
,, ,, bottlenose, yields sper-
maceti, 301.
,, domba, 291 — see Oil (calabar
bean).
,, dugoiig, 247, 293.
,, earth nut — see Oil (arachis).
,, egg — see Oil (lien's egg).
,, eleeococca (Japanese wood, tung,
wood oil), 32, 291.
,, ,, extremely rapid dry ing
qualities, 291.
,, eucalyptus, 6, 178.
,, ,, medicated candles, 407.
,, euonymus — see Oil (spindlenut).
, , fever nut — see Butters, vegetable
(Borneo tallow).
,, fish, class, 281, 292.
.,, gamboge (gamboge butter), 242,
296.
,, garlic, 15.
,, gaultheria-see Oil (winter-green).
,, geranium, 3, 15.
,, German sesame" — see Oil (came-
lina).
.,, gherkin seed, 288.
3, gingelly — see Oil (sesame").
,, gold of pleasure — see Oil (came-
lina).
,, gourd seed— see Oil (pumpkin
seed).
,, grape seed, 25, 242, 285.
,, green (Yorkshire grease distilla-
tion), 277.
,, groundnut— -see Oil (arachis).
,, gundschit — see Oil (lallemeiitia).
,, hammerfish, 294.
,, hazelnut, 242, 283.
,, hedge radish (hedge mustard),
284.
,, hempseed, 33, 35, 242, 257, 291.
,, ,, detection of , in linseed
oil, 352, 353.
,, ,, use as cooking oil, 304.
,, ,, ,, in soft soapmaking
—see Soapmaking.
,, ,, usually mixed with lin-
seed oil, 349, 352.
,, henbane seed, 242.
,, hen's egg, 121, 298, 299, 408.
,, heracleum— see Oil(cowparsnep).
,, herring, 294.
,, hickory nut (American walnut
oil), 242, 289, 291.
,, holly seed, 242.
,, horned poppy — see Oil (yellow-
horn poppy).
Oil, horse (horse grease, horse fat,
mare's grease), 286, 299.
,, ,, deodorising,465- see Rancid.
,, ,, use in soapmaking, 408.
,, horsefoot, 286.
,, horsechestnut, 242, 288.
,, Indian cress, 242.
,, Japanese wood— see Oil (elseo-
cocca).
,, Japan fish, 342.
,, jatropha — see Oil (curcas).
,, Java nut, Java almond (canary
oil), 242, 296.
,, kekune— see Oil (candle nut).
,, kulp liver, 247, 294.
,, laintlaintain seed, 289.
,, lallemantia (gundschit), 242, 291.
,, lard, 231, 286, 307.
,, ,, class, 2S1, 285.
,, ,, relative tendency to gum-
ming, 323.
,, ,, used as lubricant, 322, 325.
,, laurel berry— see Butters, veget-
able (laurel).
,, lettuce seed, 243.
,, linden seed, 243.
,, ling liver, 178.
„ linseed, 32-34, 243, 257, 258, 291.
,, ,, acid process for refining,
259.
,, adulterations of, 351, 352.
,, boiled, 262, 313-318.
class, 281, 290.
,, ,, film test, Livache's test,
133, 351.
,, ,, iodine number, 351 (see
Iodine number).
, , ,, pure, only obtainable by
handpickiiig, 350.
,, ,, relative price of, 342.
„ ,, ,, tendency to gum-
ming, 323.
,, ,, use as cooking oil, 304.
,, ,, ,, in soft soapmaking
— see Soapmaking.
,, ,, various glycerides con-
tained in, 350, 351.
,, liver class, 281, 292, 294.
,, louar, 294.
,, mabo nuts, 289.
,, maccassar, 184, 297.
„ madia, 243, 286.
,, maize, 243, 286.
,, malabar, 294.
,, malaka, 289.
,, manatee, 293.
,, mango seeds, 289.
,, mang;osteen — see Butters, veget-
able (goa butter).
INDEX.
551
Oil, margosa— see Oil (zedrach).
,, menhaden (porgie), 249, 258, 294.
,, ,, relative price of, 342.
,, meni seed, 289.
,, morse, 293.
,, m'poga nut, 289.
„ mustard, 15, 21, 25, 243, 234, 348.
,, ,, tests for sulphur in, 123.
„ neat's foot, 286, 298.
,, ,, as lubricant, 322, 325.
,, ,, relative price of, 342.
, , nettle seed, 243.
,, neutral (Yorkshire grease), 276-
279.
,, niger seed (ramtil), 243, 286,408.
, , , , relative price of, 342.
night shade seed, 243.
niko nut, 289.
nimb (neem)— tee Oil (zedrach).
nut (walnut), 243, 291.
nutmeg, 20, 243, 295.
odal, 288.
olive, 243, 257, 258, 283, 322.
,, absorption of oxygen by, 330.
,, action of sulphuric acid on
— see Oils (Turkey red).
, , adulterations of, 344-347.
,, as lubricant, 326.
,, class, 281, 282.
,, extraction by hot water
process, 200.
,, relative price of, 342.
,, relative tendency to gum-
ming, 323.
,, sources and production of,
342-344.
,, taste improved by presence
of free acids, 116.
,, used for soapmaking — see
Soapmaking.
olive kernel, 243, 343.
,, ,, extraction of, 343.
oolachan, 294.
opochala, 288, 289.
owala, 288, 289.
palm (palm butter), 21, 243, 257,
295, 322.
,, bleaching processes, 264, 265.
,, as candle material — see
Candle stearine.
,, extraction of, by hot water
process, 200.
, , use in soapmakiug — see
Soapmaking.
palmkernel(palmnut),20,243,295.
,, extraction by sol-
vents, 200.
, , use in soapmaking —
see Soapmaking.
Oil, pea, 121, 259.
peach kernel, 243, 283.
peanut — see Oil (arachis).
pelargonium, 20.
pilchard, 161, 294.
pine — see Oil (red pine),
pinnay, 291 — see Oil (calabar
bean).
piquia (pekea), 297.
pistachio nut, 244, 289.
plum kernel, 283.
poppy seed, 33, 243, 257, 291.
, , relative price of, 342.
, , use as cooking oil, 304.
,, ,, in soft soapmaking
— see Soapmaking.
porpoise (Delphinus phocsenaoil),
247, 293.
,, contains valerin, 301.
ponga — see Butters, vegetable
(karanja butter),
poon seed — see Oil (calabar bean),
poondi — see Butters, vegetable
(karanja butter),
porgie — see Oil (menhaden),
pumpkin seed (gourd seed), 243,
288.
purgir nut (purqueira, jatropha,
curcas) — see Oil (curcas).
radish seed, 244.
ramtil — .see Oil (niger seed),
ray liver, 294.
rape (colza), 21, 25, 49, 257-259,
284, 313, 322.
,, absorptionof oxygen by, 330.
,, adulteration of, 349.
,, as standard of viscosity,
101, 349.
,, blown, 319, 320.
,, class, 281, 284.
,, fatty acids and glycerides
contained in, 11, 41.
,, injurious effects of free
acids on, 115, 313.
,, insoluble in acetic acid, 55,
349.
,, refining of —see Oils, refining.
,, relative price of, 342.
,, ,, tendency to gumming,
323.
,, tests for sulphur in, 123.
,, used for soapmaking, 408.
,, yield of, 241, 348.
raps (rapsamen), 348.
red pine seed (pine oil, pinaster
oil), 244, 287.
rosemary, 15.
rosin — see Rosin oils,
riibsen, 348.
552
INDEX.
Oil, rue, 3, 14, 20.
„ safflower seed, 244.
„ sanitas, 6, 477.
„ sapucaja nuts, 244.
,, sardine, 294.
,, Scotch fir seeds, 244.
„ seal, 247, 258, 293, 303.
,, ,, relative price of, 342.
,, ,, used for soapmaking — see
Soapmaking.
,, sesame* (gingelly, benne", til oil),
244, 286.
,, ,, Baudoin's sugar test for
— see Sugar test.
„ „ class, 281, 286.
,, ,, detection of adultera-
tions in, 347.
,, ,, relative price of, 342.
„ „ used for soapmaking,408.
„ shark, shark's liver, 247, 294, 408.
„ sheep's trotter, 52, 286, 298.
,, soap berry — see Butters, vege-
table (soap berry).
„ soja bean, 287.
,, sperm, 3, 14, 258, 313.
adulteration of, 353.
as lubricant, 322-325.
blown, 320.
class, 282, 299.
deposits spermaceti, 300, 353.
relative tendency to gum-
ming, 323.
,, ,, sources, 300, 353.
,, spindlenut (euonymus), 244, 288.
,, spirit (Yorkshire grease distilla-
tion), 277, 278.
„ sprat, 294.
„ spring poppy seed, 244.
,, spruce fir seed, 244.
„ spurge, 244.
,, strammonium seeds — see Oil
(datura).
,, sunflower, 244, 286, 304, 408.
, , , , production in Russia, 305.
,, tacamahac (tacamahac fat) — see
Oil (calabar bean).
„ tallow, 231, 285, 286.
,, tamanu, 291 — see Oil (calabar
bean).
,, tansy, 3.
„ tea seed, 244, 283.
,, thistle seed, 244.
„ til — see Oil (sesam§).
„ tobacco seed, 244, 291.
,, touloucoona— see Oil(carapanut).
„ train— see Oil (whale).
,, tung, 291— see Oil (elaeococca).
„ tunny, 294.
,, turpentine, 6, 25.
Oil, turpentine, distilled off in Mei-
necke's process, 473.
,, ,, facilitates air bleaching
of wax, 269, 359.
,, ,, oxidation of, 477.
,, ,, solvent for manganese
salts as driers, 315.
,, ungnadia, 244.
,, valerian, 15.
„ valve (valveoline), 330.
,, walnut — see Oil (nut).
„ walrus, 293.
„ watermelon seed, 244, 288.
,, weld seed, 244, 291.
„ whale (train), 247, 258, 293, 303,
322.
„ class, 281, 292, 293.
,, ,, communicates unpleasant
smell to soft soap, 459.
,, ,, relative price of, 342.
,, ,, used for soapmaking — see
Soapmaking.
,, wild radish seed, 244.
,, wintergreen (gaultheria), 3, 5,
14, 19, 192.
,, wood (elaeococca, Japanese wood),
— see Oil (elaeococca).
,, wool (from Yorkshire grease dis-
tillation), 279.
,, yellow horn poppy, 242.
,, zedrach (margosa, nimb, neem
oil, veppam fat), 297.
Oil baths for tempering metals, 302,
Oilcake parings, use in clarifying
oils, 255, 256.
Oilcakes, 114, 211-214, 303-305.
acrid, from mustard seed, 349.
composition of, 213-214.
cotton seed, 212, 214, 304.
dimensions and weight of, 21 1.
fatty matters contained in,
115, 213-217.
free fatty acids contained in,
115, 214.
sunflower, superior to hemp
and rape, 305.
Oil lamps — see Lamps.
Oil mill plant, 214-229.
,, used in olive oil pro-
duction, 200, 343.
Dils, absorption of oxygen by — see
Absorption.
, , acety lation test for— see Acety-
lation test.
„ adulteration of, 340-361.
„ animal, 281, 282, 285, 292, 298,
299, 325.
,, ,, do not yield sativic
acid, 291.
INDEX.
Oils, anthracene— sec Anthracene.
,, Benedikt and Ulzer's test — see
Acetylation test.
,, blacktish, 293.
,, bleaching of, 263-268.
„ ,, partly effected by pre-
cipitation of mucilage,
&c., 263
,, blown, 4-2, 90, 125, 130.
,, ,, chemical changes during
manufacture of, 319-321.
,, ,, manufacture of, 264, 319.
,, blubber — see Oils (cetacean).
,, body of — see Viscosity.
, , boiled — see Oils, drying (boiling
of).
,, bone — see Bone fat,
,, bromine absorption of, 176-179.
,, burning (lamp oils), 2, 5, 302,
312.
,, injurious effect of free
acid on, 116,260,313.
,, cetacean (blubber oils, train
oils), 6, 113, 116,
292, 293, 299, 360.
,, ,, extraction of, 247.
,, from toothed whales
yield spermaceti,
293, 300, 301.
,, ,, separation of alco-
holiform constitu-
ents from, 121.
,, ,, separation of sper-
maceti from, 300,
301, 360.
„ characteristic oxidation pro-
ducts of, 123.
,, chemical changes during drying
of, 134-137.
,, clarification of, by chemica]
processes, 254-263, 349.
„ ,, by filter presses and ordin
ary filters, 228, 255, 257
,, ,, by standing in contact
with water, 344.
,, classification of — see Classifica
tion.
,, cleansing of— see Oils (refining)
,, coaltar, 2, 5, 50, 328.
,, cod, 294— see Oil (codfish, cod
liver).
,, cohesion figures of — see Cohe
sion figures.
„ cold drawn, 114, 212.
,, colour of— see Colour.
}} ,, reactions of — see Coloui
reactions.
,, congealing point of— see Melt
ing points.
Oils,
553
cooking, 302-304.
creosote, 2, 328.
cylinder, 105, 128, 324.
dead, 324, 328.
decolorising of — see Oils,
bleaching of.
dissolved impurities, 256.
dolphin, 293.
drying, 32, 33, 55.
„ boiling of, by air blowing
process, 314-316.
,, ,, by free fire process,
314, 315.
,, by oxygen process,321.
class, 281, 290.
decolorising high class, 268.
film test, Livache'stest, 133.
present in nonxlrying oils
in small quantity, 185,
282, 344.
,, relative proportions of dif-
ferent glycerides in, 136,
290.
,, used in paint manufacture,
&c., 313.
,, ,, soft soapmaking —
see Soapmaking.
drying of, chemical changes dur-
ing, 129, 134-137.
edible, 302-312.
elaidin test— see Elaidin test,
effect of heat on, 125-128, 314.
„ light on, 130-132, 139,
149.
,, polarised light — see
Light (polarised),
electrical conductivity of, 53.
engine, 324.
essential, artificial, 6.
,, natural, 2, 5, 20, 53.
ester numbers of — see Ester
number,
examination of, general scheme
for, 124.
expression of, 303— see Presses,
extraction of, by solvents, 231-
244, 303.
,, fish and liver, by
hot water, 248.
, , vegetable, fats, &c. ,
by hot water, 200.
fish, 248, 259, 263, 294, 299.
,, bleached by hot air, 264.
J} ,, bichromate, 265.
, , colour reactions of, 294.
,, detection in linseed oil,
352.
,, give unpleasant smell to
soft soap, 459.
554
INDEX.
Oils, fish, used as adulterants, 348.
,, ,, used for soapmaking, 408
— see Soapmaking.
,, fish liver, 247, 294, 408— see
also Oil (cod liver).
,, fixed, 2.
,, flashing points of— see Flashing
point.
,, free acid, number of — see Acids
(free fatty).
„ fusel, C, 14, 20, 53.
,, fusing points of — see Melting
points.
,, general nature of, 1.
,, glyceridic, 3, 93, 281.
,, ,, detected in sperm oil by
saponificatiou, 354.
,, gumming of — see Gumming.
,, heat evolution with sulphuric
acid, 147-151, 341.
,, ,, with sulphuric acid,
effect of light on,
131, 139.
,, Hehner's test for — see Hehner
number.
,, herring, 294.
, , Hiibl's test — see Iodine number,
,, hydrocarbon, 2, 5, 54, 90 — see
also Oils (mineral, paraffin,
coaltar).
,, hydrolysis of — see Hydrolysis.
,, insoluble acid, number of — see
Insoluble acid number.
,, iodine number of (iodine absorp-
tion of) — see Iodine number.
,, kerosene, 2, 5.
,, Koettstorfer's test — see Total
acid number.
,, lamp — see Oils (burning).
,', lesser known, 287-289.
,, ,, some probably
valuable, 289.
,, liver, 294—see; Oils (fish liver,
shark liver).
,, ,, colour reactions of, 294.
,, ,, contain cholesterol and
biliary constituents, 292.
„ lubricating, 2, 5, 67, 321-330.
,, ,, absorption of oxygen
by, 134, 329, 330.
,, ,, analysis of, 328.
,, ,, characters and be-
haviour of, 325, 326.
,, ,, congelation of, 67,325.
„ ,, flashing points of —
see Flashing point.
,, ,, free mineral acids in,
260, 322 — see also
Lubricants.
Oils, lubricating, manufacture of, 321-
328.
,, ,, metallic soaps con-
tained in, 121, 324,
,, ,, of fine quality from
degras, 337.
,, ,, specific gravity of, 325.
,, ,, spontaneous combus-
tion of, 133.
,, ,, viscosity of — see Vis-
cosity.
,, ,, volatility of, 325.
,, machinery, 128, 324.
,, medicinal, 303.
,, malabar, 294.
,, melting points of — see Melting
points.
,, methyl iodide, test for — see
Methyl number.
,, mineral (petroleum, natural
naphtha), 2, 5, 25.
,, ,, absorption of oxygen
by, 330.
flashingpointof,126-128.
lubricants containing,
322-330.
refraction of, 52.
relative price of, 342.
specific gravity of, 90,91.
use of, in early ages for
burning, 312.
,, viscosity of, 105.
nitric acid on, action of — see
Nitric acid test.
nitrous acid on, action of —see
Elaidin reaction,
nondrying, 281.
,, usually contain small
quantities of drying oils, 185,
282, 284, 344.
nonglyceridic, 3, 93, 282.
odour of — see Odour,
order of price of, 342.
oxidation of — sf e Absorption of
oxygen, Oils (blown), Oils
(drying), Gumming,
oxidised— see Oxidised oils,
paraffin, 2, 5, 91, 313.
,, in soap, 258 — see Soap,
special kinds of.
petroleum — see Oils (mineral),
phosphorised, from leguminous
plants, 123, 259.
polarised light, action of, 50.
porpoise, 293.
proximate constituents of, 110-
124.
purification (Noerdlinger's),
263.
INDEX.
555
Oils, pyrene, 344.
,, rancidity in— see Rancid, Ran-
cidity.
,, ray, 294.
,, red — see Red oils.
,, refining of, 254-263.
, , refractive index of — see Refrac-
tive index.
, , Reichert's test for— seeReichert
number.
, , rosin — see Rosin oils.
„ salad, 212, 257, 303, 344.
,, ,, refined cotton seed oil
intermixed with, 267.
,, saponaceous matters contained
in, 121.
., saponifiable, 3, 6, 323.
,, saponification number of — see
Total acid number.
,, saponitication equivalents of —
see Saponitication equivalents.
„ seal, 293.
,, ,, colour reactions of, 294.
„ semidrying, 286, 290.
., ,, proportions between
different glycerides
in, 290, 291.
,, separation of stearines from —
see Stearines.
„ shale, 2, 5, 90, 91, 313, 322.
,, shark liver, 247, 294, 403.
„ sod, 336.
,, solidifying points of — see Melt-
ing points.
, , soluble acid numbers of — see
Soluble acid number.
,, solubility in solvents of — see
Solubility.
,, specific gravity of, 76-94, 341.
,,' e fleet of light on, 130.
,, spindle, 128, 324.
, , spontaneous combustion of, 132.
,, ,, oxidation of — see
Spontaneous oxidation.
,, standard, preparation of — see
Standard.
,, sulphur chloride on, action of
— see Sulphur chloride.
,, sulphocarbon, 344, 408.
,, sulphuric acid on, action of —
see Sulphuric acid.
,, sulphurised, tests for, 123, 154.
,, summer, 257, 304, 348.
,, table — see Oils (edible, salad,
virgin).
,, taste of — see Taste.
,, tournantes — see Huiles.
,, total acid numbers of — see
Total acid number,
Oils, train — see Oils (cetacean).
„ class, 281, 292, 293.
„ Turkey red, 27, 42.
,, ,, adulterations of, 334-
336.
,, ,, analysis of, 332-336.
,, ,, bibliography of, 331.
,, ,, constitution of, 143-
147, 330, 331.
,, ,, manufacture of, 330-
332.
,, turret, 324.
,, uses of, 302.
,, unsaponifiable matters con-
tained in — see Unsaponifi-
able matters.
„ vegetable, 281-285, 286-291,
295-298.
,, ,, lesser known, 287.
,, virgin, 304,344 — see also Oils
(salad).
,, viscosity of— see Viscosity.
„ volatile, 2.
,, ,, acids from — see Vola-
tile acids.
,, ,, number of — see Vola-
tile acid number.
,, vulcanised, 154.
,, water contained in — see Water.
,, whale, 293 — see Oils (cetacean).
,, ,, colour reactions of, 294.
„ winter, 230, 257, 348.
,, yield of, from seeds, &c. — see
Yield.
, , , , fatty acids from, 76, 1 63.
,, Zeisel's test for— see Methyl
number.
, ,<- zinc chloride on, action of — see
Zinc chloride.
Olberg, water bath, 61.
Olefjant gas, 26.
Olefines form glycols by oxidation, 44.
Olein (oleic triglyceride), 7, 11, 28,
110, 285.
,, action of nitrous acid on — see
Elaidin reaction.
,, ,, sulphuric acid on — see
Oils (Turkey red).
Oleine, candle — see Red oils.
„ cokermit, 90, 92, 231, 283.
,, palm kernel, 283.
Oleines (commercial products), 90,
92, 110, 285.
animal, 285, 299.
distilled, 110, 262, 277, 285,
324, 377.
,, ,, hydrocarbons pre-
sent in — see Hy-
drocarbons.
556
INDEX.
Oleines, from wool grease, 276-279.
,, Turkey red oils, 285.
,, vegetable expressed, 110,
229, 257, 283.
Oleine soaps — see Soapmaking.
Oleomargarine — see Margarine.
Oleometer, Lefebre's, 79.
Oleonaphtha, 330.
Oleorefractorneter, 51-53, 347.
Oleostearine, 93.
Olive stearine, 230.
Olive trees, different species and
varieties of, 342.
Opderbeck, oxygen process, 321.
Open test (flashing point), 126.
Oudemauns, Kambutan tallow, 296.
,, stearidic acid, 30.
Overbeck, oxidation of stearolic acid,
36, 45.
,, oxyoleic acid, 41.
Ox tallow — -see Tallow.
Ox, utilisation of fat of an, 311.
Oxalic acid from glycerol, 8, 519-522.
,, acids from glycols by fusion
with potash, 18.
Oxidation during boiling, 125.
of aldehydes, 20, 25.
,, of fatty acids during dry-
ing, 113.
of oils by light, 130-132,
139, 149.
,, of oils during drying, 42,
129-137 — see Absorption
of oxygen, Gumming.
,, products of fatty acids, 19,
33/36, 40, 43.
,, ,, characteristic,
128, 129.
,, spontaneous — see Spon-
taneous oxidation.
Oxidised oils (oils naturally contain-
ing oxygen), 3.
,, (commercial; really are
sulphurised), 154.
,, (linseed "skins" for
linoleum), 318.
, , (oils treated with oxidis-
ing materials), 42 —
see al*o Oils (blown,
and refining of).
Oxy acids formed during drying, 135.
Oxygen, absorption of — see Absorp-
tion.
,, addition to " unsaturated "
acids, 33, 36, 45.
Oxyoleates, 42, 332.
Oxyoleic acid, 41.
,, mixed glyceride, 144.
Oxyolein, 139.
Oxystearic mixed glyceride, 144.
Ozokerite (solid mineral hydrocar-
bons, earthwax), 2, 5, 6, 88,
91, 364 — see also Cerasin.
,, used as beeswax adulterant,
359.
Paint, 135, 302.
Palmer, metallic wick, 394.
Palmieri, electrical conductivity, 53.
Palmitin (palmitic triglyceride), 11,
285.
,, chief solid constituent of
olive oil, 344.
Palmitine (commercial product), 387,
407 — see also Candle stearine.
Pans for boiling oil, soap, &c. — see
Kettles, Decomposing pan,
Cooling pan, lie-melting pan,
Crystallising pan, &c.
,, crutching soap, 438-442.
Paracholesterol, 18.
Paraffin wax — see Wax (paraffin).
Paraphytosterol, 16, 17.
Paring machine (oilcake), 223.
Parings, edge runners for grinding,
220, 223.
Paris Municipal Laboratory, 65, 82.
Parnell, causticising under pressure,
413.
Paterson, spectrum colorimeter, 50.
Payne, glycerine manufacture, 515.
,, melting points of distilled
fatty acids, 384.
Pea nut — see Oil, arachis.
Pearlash, 409.
Pearlashing, 451, 479, 489.
Peh-la— see Wax, Chinese.
Pelargonium, 20.
Pendulum machine, M'Xaught's, 94.
Pensky, flashing point apparatus, 127.
Perfumes, injurious effects of excess
of, in toilet soap, 480.
,, oils used in extraction of,
302, 479.
,, used for soap— see Soap-
making (perfuming).
Permanganate, oxidation by, charac-
teristic pro-
ducts of, 128,
129.
,, ,, of acrylic acids,
28, 30, 41-44.
,, ,, of animal oils does
notformsativic
acid, 291.
,, of linolenic acid,
37, 43, 128.
INDEX.
557
Permanganate, oxidation of linolic acid
34, 35, 43, 128.
,, ,, of ricinoleic acid,
40, 43, 129.
,, ,, of stearolic acids,
33, 36, 45.
,, ,, rule respecting,
44.
,, wax bleached by
means of, 269.
Peroxide of hydrogen as bleaching
agent — see Hydrogen peroxide.
Peters, linolic acid, 34.
,, polarised light, 51.
Petroleum — see Oil (mineral).
,, ether (light petroleum spirit,
benzoline), 2, 5.
,, ,, as solvent, 55, 115, 118-
124, 231, 236, 252,
262, 273, 275, 328,
329, 336, 337— see also
Soap analysis.
,, ,, fatty acids insoluble in,
from boiled oil, 135.
,, ,, preferable to ordinary
ether as solvent, 118,
120, 273, 275.
Phasol, 16, 259.
Pheasant grease, 298.
Phenol (carbolic acid) and homologues,
3, 6, 15, 16, 53.
,, determination of, in soap, 506.
,, extraction from coaltar, 230.
,, use of, in disinfectant soaps
— see Soaps, special kinds of
(carbolic, disinfectant).
Phenolphthalein as indicator, 23, 115-
117, 124, 328, 333, 359, 497.
Phlorol, 16.
Phosphorised constituents, 121.
Phosphorus, determination of, 124.
Physical properties of glycerol, 7.
„ ,, oils, &c., 47-109.
Phytosterol, 6, 16, 17, 240, 259.
, , determination of inoils, &c.,121.
Pichurim bean fat, 20.
Pickling soap bars, 438.
,, wicks, 394, 395.
Pigments (mottled soap), 472.
Piston candlemoulding machines, 399,
Pitch, Burgundy, adulterant of bees-
wax, 359.
Pitch formed in Wilson's process, 381,
,, from distillation of foots by
superheated steam
261.
,, ,, of Yorkshire grease
by superheated
• steam, 277.
'itchused as coarse lubricant,277,324.
:*liny, early soapmaking processes,
449.
'lotting (milled soap), 448.
^lumbago (antifriction), 324.
3ohl, melting points, 64.
oiseuille, viscosity, 107.
5olariscope, polarised light — see
Light, polarised.
Dolishing candles, 406.
,. soap tablets, 448.
^olyglycerols, 8.
Polymerised fatty acids formed by
elaidin reaction, 139.
, , glycerides formed during
boiling and drying,
135, 318.
,, oleo-oxystearic acid, 330.
,, ricinoleic acids — see
Acid, ricinoleic.
Pomades, lanolin used in making, 339.
,, oils used in making, 302.
Porpoise blubber, extraction of oil
from, 247.
Potassium carbonate, causticising— see
Causticising.
,, ,, leys, alkalinity
of, 419.
,, ,, used in Mege
Mouries pro-
cess, 308.
,, ., used in pearl-
ashing — see
Pear-lashing.
,, ,, used in soap-
making — see
Soapmaking.
,, chloride, action on soda
soaps, 490, 491.
,, ,, source of potash,
410.
Potash, action on brominated acids,
28.
,, caustic (potassium hydroxide),
effect of fusion with — see
Hydrogen.
,, from sunflower seeds, 305.
„ leys, alkalinity of, 417, 419,
420.
,, leys, preparation of, 411-414.
,, neutralised — see Free acid
number, Total acid number,
&c.
,, quantity equivalent to soda,
425.
„ to fats — see
Calculations.
,, soaps, action of soda salts on,
451, 472, 473.
558
INDEX.
Potash, use of, in refining oils,256,261.
,, vegetable alkali, 409.
Potato fusel oils, 14.
Poullain and Michaud, zinc oxide
process, 379, 515.
Poutet, elaidin reaction — seeElaidin.
Power requisite in oil mill, 215-217.
Precipitation processes (removing
mucilage, &c.), 255, 262, 263.
Press cake — see Cold press cake, Hot
press cake, Separation cake.
Presses, cold — see Cold press,
earlier forms of, 199.
elbow, 2U2.
hot — see Hot press,
hydraulic, 207, 343.
pressure requisite in, 211.
screw, 205, 343.
wedge, 203.
Pressure, distillation under dimin-
ished— see Distillation.
„ in autoclaves, 373.
,, in oil presses, 211.
,, rendering tallow under in-
creased, 250.
,, soapmaking under in-
creased, 462-464.
Prices of oils, &c., 342.
Primrose soaps, 474, 509, 510.
Printing ink, 125, 317, 318.
Proximate constituents, 110-124.
,, ,, information wanted
concerning, 113.
,, ,, separation of, 111-
113.
,, ,, variation with soil,
climate, &c., 111.
Pumps, soap, 434.
Pulfrich, refractometer, 51.
Purvis, waggon grease, 327.
Pyknometer, 77.
Pyramid drainage surface (filter-
press), 229.
„ night lights, 406.
Q
QUANTITATIVE reactions of oils, &c.,
156-198.
„ tests for oils, tabulated,
194-198.
Quantity of alkali requisite for
saponification — see Calculations.
Quebrachol, 16.
Quicklime— -see Lime.
Quinquet, use of lamp chimneys, 313.
EADISSON, palmitic acid process, 387.
Railway grease— see Lubricants.
Rancid tallow, &c., cleansing of,
256, 260, 261, 265, 310.
Rancidity, 10, 49, 69, 255.
,, due to oxidation, 132.
,, light promotes, 132.
,, produces much free fatty
acid, 10, 114, 255, 355.
Rape seed (colza, cole seed), various
species of, 348.
Raphigaster, 25.
Rational Beaume scale, 86.
Raw oils, 313— see Oils (drying).
Reaction, specific temperature, 149.
Reactions of oils, &c., quantitative,
156-198.
Reaumur scale, 57, 58.
Recovered greases— .see Grease.
Red oils (crude oleic acid, candle
oleine), 110, 231, 285.
analysis of, 375, 378.
expression of, 231, 370.
filter cake— see Filter cake,
palmitic acid from, 387.
soap from — see Soapmaking
unsaponified grease in — see
Unsaponified fat.
,, utilisation of, 386-388.
,, yield from ox fat, 311, 312.
Redwood, viscosimeter, 98.
,, ,, results obtained
by, 101-105.
Refining oils, &c., 254-263.
,, acid processes, 259, 349.
„ alkaline „ 260, 349.
,, ,, process removes free
acids, 12, 115, 260, 322.
, , by treatment with water, 344
,, Hartley and Blenkinsop's-
process, 263.
,, Noerdlinger's process, 263»
, , precipitation processes, 262.
,, virgin oils, 304.
Reformatsky, linolic acid, 34, 35.
Refractive index, refractometer, 51 ,.
341.
Reichert's test (Reichert number), 23,
53, 157, 195, 341.
,, mode of working, 173-176.
Reichert-Meissl test, 174, 195.
Reichert- Wollny „ 175.
Reichl, test for glycerol, 8, 516.
Reimer and Will, dierucin, 11.
,, rapic acid, 41.
Relative density — see Specific gravity.
,, viscosity — see Viscosity.
Remelting pans, 441-443.
Renard, test for arachis oil, 344.
Rendering animal fats, 245.-251.
INDEX.
559
4tf S
Resin (pine)— see Rosin.
,, used for early torches, 312.
Resinate of soda, 450, 453.
, , calculations respect-
ing, 455, 465.
,, useofjinsoapmaking
— see Soapmaking ;
Soap, special kinds
(yellow soap).
Resinous constituents of oils, 118.
,, ,, removal of, from
oils, 255, 256,
260, 262, 322.
Resins and resinoid bodies, 3, 25.
,, ,, used as beeswax
adulterants, 359.
Richards, testing liability to spon-
taneous inflammability, 133.
Richardson and Watts, railway
grease, 327.
Richmond, density of glycerol solu-
tion, 517.
Ricinelaidin, 40, 137.
Ricinolein (ricinoleic triglyceride),
,, action of nitrous acid on, 137.
,, distillation of, 40.
Rideal, viscosity of gum solutions,
108.
Ritsert, causes of rancidity, 132.
,, glycerine testing, 515.
Rock— see Candle stearine.
Rolls — see Crushing rolls.
Rose, Down and Thompson, oil press
machinery, 215.
Rosin, (colophony), 88, 92, 118, 178.
,, action of sulphur chloride on,
156.
., admixed with thickened oils,
&c., 142.
,, adulteration of linseed oil
with, 352.
,, ,, of beeswax with, 359.
,, manufacture of resinate of
soda, 453.
,, use in making lubricating
greases, 327-329.
„ ,, soapmaking — see Soap-
making.
,, window glass, 474.
Rosin oils, 2, 92.
,, ,, absorption of oxygen by,
330.
,, ,, action of, on polarised
light, 50.
,, ,, adulteration of linseed
oil with, 352.
,, ,, detection of, in Turkey
red oils, 335.
,, „ fluorescence of, 50.
Rosin oils, refractive index of, 52.
,, ,, relative price of, 342.
,, ,, solubility in glacial acetic
acid, 55, 57, 329.
, , , , use of, in preparing lubri-
cants, 322-324, 327-329.
,, ,, viscosity of, 105.
Rotation of polarised light — see Light
(polarised).
Roy an, candle moulding machine,
398.
Riidorff, melting points, 69.
Rule followed in oxidation, 44.
Rush lights, rush pith wicks, 312, 362r
390.
Russian mineral oils (viscosity), 105.
Rutschmann, stripping machine, 446.
SAKE, grease recovery, 272.
Salad oils— see Oils (salad),
alt as source of alkali (soda), 410.
,, in butter, &c., 123, 307.
Salting out, 23, 33, 54.
,, in refining oils, &c., 256.
,, in soapboiling — see Soap-
making.
,, in Turkey red oil mak-
ing, 331.
Sand, use of, in clarifying oils, 255.
Sanza (olive marc), 343.
Saponaceous matters in oils, &c., 121-
124, 135, 315, 324, 328, 347.
Saponitication by alkaline carbonates,.
409, 410.
Saponification equivalents, 33, 158,
194, 341.
,, ,, determination of r
161-170.
,, ,, of glycerides ex-
ceed mean equi-
valents of acids
by 12-67, 165.
,, in three stages, 468.
, , number— see Total acid:
number.
,, quantity of ley requisite-
for — see Calculations.
Saponification, typical reactions of,.
3-5.
Saponin, 297.
Sarg, utilisation of fat of an ox, 311.
Saturated hydrocarbons — see Hydro-
carbons.
Saturation, fractional, 112, 113.
Saytzeff, dioxystearic acids, 28, 30,
41, 42, 46, 129.
560
INDEX.
Saytzeff, oxystearic acids, 38, 39.
, , use of mercuric bromide in
Hiibl's test, 179.
Scales, hydrometer, 84-86.
,, thermometer, 57-60.
Schadler, amounts of fatty matter in
seeds, &c, 241-244.
,, cohesion figures, 49.
,, colour reactions, 154, 294.
,, distillation with superheated
steam, 383.
,, hydrometer scales, 85.
,, iodine numbers, 182.
,, melting points, 67-70.
,, nonexistence of doeglic acid,
24.
,, polarised light, 50.
, , Reichert-Meissl numbers, 1 74
,, Roy an's candle moulding
machine, 398.
,, solubilities, 54, 55.
,, specific gravities, 87.
,, total acid numbers, 160.
,, unsaponifiable matters, 257.
,, yield of linseed oil, 351.
,, ,, rape seed oils, 348.
Schepperand Geitel, melting points. 76
,, separation cake, 376.
Scheme for examination of oils, 124.
, , , , soaps, 506.
Scheurer Kestner, Turkey red oils,
146, 333.
Schlink, deodorising cokernut oil,310.
Schmid, viscosimeter, 95.
Schmidt's process (zinc chloride and
oleic acid), 142, 386.
Schmitz and Toenges, oxyoleates, 332,
Schnaible, toluene as solvent for wax
in soap, 496.
Schfin, hypogseic acid, 24.
Schroder, oxyhypogseic acid, 41.
,, palmitoxylic acid, 45.
,, — see Grills and Schroder.
Schiibler, viscosimeter, 95.
„ results with, 102.
Schuler, linoleic acid, 33.
Scotch mineral oils, viscosity of, 105.
Scourtins (oil extraction), 204.
Scraps from ox fat, 311.
Screens for sifting seeds, &c., 223.
Screw presses, 205-207.
Scribe for marking soap blocks, 437.
Seal blubber, extraction of oil f rom,247
Sealing wax, 302.
Sea weed jelly (antifriction), 324, 328.
Seed crushing — see Oil mill plant, anc
Crushing rolls.
Seeding (of press cake) — see Separa
tion cake.
seeds, determination of fat in, 237.
, , yield of fatty matter from, 241-
244.
eibel, sulphurised lanolin, 339.
teltsam, bone fat extraction process,
253, 254.
Separation of fatty acids, 112, 113.
,, proximate constituents,
111.
Separation cake, (press cake), 311.
,, analysis of , 375, 378.
,, seeding (granula-
tion, crystallisa-
tion) of, 355, 367-
'Shale oils — see Oils (shale).
Shark livers, extraction of oils from,
247.
Shaving cream. 483.
Shea butter — see Butters, vegetable
(Shea).
Qheep's tallow— see Tallow.
hoddy scourings, grease from, 276.
Silver, bromostearate, action of water
on, 25, 30.
,, hydroxide, action on bromin-
ated acids, &c., 27, 30, 41, 43.
,, nitrate test, 152-154.
,, test(Becchi's) — seeBecchi's test.
Skalweit, density of glycerine solu-
tion, 516, 517.
Singer and Judell, wool scouring, 337.
Skimmer pipe (soap kettle), 433, 434.
Skins from drying oils, 135, 381.
, , tanning and currying, 302, 336.
, tender, injurious effects of
alkaline, highly perfumed,
and sugared soaps on — see
Soap, alkaline ; Soap, special
kinds of (transparent; highly
scented).
Slabbing soap, 437, 438, 444.
Smith, Watson, wool scouring, 337.
Soap, alkaline, calculations respecting
excess of alkali in, 454, 464.
,, ,, degree of alkalinity judged
by tongue, 510.
,, ,, injurious effects of, on ten-
der skins, 458, 479.
,, ,, ,, on wool, silk, &c.,.
453, 461.
Soap analysis —
Cailletet's method, 507, 508.
Calcium salt test, 508.
Classification of toilet soaps, 512.
Determination of actual soap, 492,
493.
,, ,, calcula-
tion respecting, 493.
„ of alcohol, 505, 506.
INDEX.
561
Soap analysis —
Determination of average molecular
weight of fatty acids,
172, 494.
,, crude fatty acids, 492,
493, 496, 506.
„ fatty anhydrides, 493,496,
497, 50(5.
,, free alkali, 492, 497-501,
507, 512.
,, ,, as caustic, 498-500,
507.
,, ,, ascarbonate,500,507.
,, ,, by alcohol test, 498.
,, ,, by fatty acid titra-
tion test, 499.
.,, ,, by salting out test,
500.
,, », by salting out test,
excess found by,
500.
,, glycerol 494, 504-506, 512.
,, hydrocarbons (paraffin,
&c.), 258, 495, 496,506.
,, mineral weighting ad-
mixtures (China clay,
steatite, &c.), 494, 504,
507.
.,, organic weigh ting admix-
tures (starch, oatmeal,
sawdust, &c.), 494,
504, 507.
,, phenol and phenoloids,
506.
,, pigments, 504.
„ potash, 501, 506.
, , rosin acids, 474, 497, 506,
508.
.,, ,, by Gladding's pro-
cess, 485, 501,
502, 511.
,, ,, ,, sources of er-
ror in, 502.
,, ,, by modified Glad-
ding's process, 502.
.,, ,, bv Twitchell's pro-
cess, 503, 504, 511.
.,, salts (sulphates,chlorides,
&c.), 494, 497, 499, 506,
507.
, , silicate, 494, 497, 504, 507-
„ soluble acids, 496, 497,
499
„ sugar, 494, 504-506.
, , total alkali, 492, 493, 496,
497, 506.
,, unsaponifiable matters
119, 258, 492-495, 497,
506.
Soap analysis —
Determination of unsaponified fat,
492, 495-497, 506.
,, volatile matters, 505.
„ water, 494, 495, 506.
,, waxy matters (beeswax,
spermaceti, cholesterol,
&c.), 495, 496,506.
General schemes, 494, 506, 507.
Typical results ( manufacturers',
pharmaceutical, toilet, soft soaps,
&c.), 508,511.
Soap, bleaching dark coloured, 267.
chemistry of, 484-492.
Soap factory plant, 426-448.
Crutchincr pans, 438-441.
Curbs, 432, 433.
Cutting appliances, 437, 438.
Fan, 433, 434, 460.
Frames, 434-437, 444.
Kettles (coppers, pans) — see Ket-
tles.
Milling machinery, 446.
Plotting machinery, 448.
Pumps, 434.
Remelting pans, 441-443.
Slabbing and barring machines,
437, 438.
Stamping machines, 444, 445.
Steam twirl, 428 — see also Morfit.
Stripping machine, 446.
Soap, fused, reaction of salts, &c. , on,
451, 473, 488-492.
,, ,, alkaline carbonates
on, 451, 489, 490—
see also Pearlashing.
historical references to, 449.
hydrolysis of, 486-488.
,, Wright and Thompson's
experiments, 487.
leaves, 483.
powders, 477.
saline matters in, calculations
respecting, 455, 465.
Soap, special kinds of —
Aluminated, 451, 475.
Bleached palm oil, 508.
Borax, 451, 475.
Castile, 467, 472, 508.
Carbolic, 451, 477.
Carbonated, 451, 462, 475, 477—
see also Pearlashing.
Cold water, 477, 509, 510.
Curd — see Soapmaking.
,, amount of water present in,
470.
,, analysis of, 508, 510.
Dealkalised (neutralised), 453, 461,
480, 481, 483, 484.
36
562
INDEX.
Soap, special kinds of—
Disinfectant ( carbolic, cresylic,
naphthol, sanitas, terebene, &c.),
451, 476, 477.
Emollient (containing lanolin, sper-
maceti, vaseline, wax, &c. ), 448,
478, 479.
Fancy — see infra (Toilet).
Filled— see Soapmaking (tilling).
Fitted — see Soapmaking (fitting).
,, amount of waterpresentin, 470.
Floating, 441.
Glycerine, 458.
,, containing additional
glycerol, 458, 479, 482, 512, 513.
Harlequin, 483.
Highly scented, injurious action of,
480, 512.
Ivory, 509.
Little pan, 479.
Marbled, 483.
Marine — see Soapmaking.
,, analysis of, 508, 509.
Marseilles, 407, 472, 508, 509.
Medicinal (creosote, cresylic, ich-
thyol, iodine, mercurial, naph-
thol, sanitas, sulphur, terebene,
&c.), 477.
Metallic— see Metallic soaps.
Milled, 446-448, 457, 479, 480, 511.
Mottled — see Soapmaking.
,, amount of water present
in, 472.
Neutralised — see supra (Dealka-
lised).
Normandy, 475.
Oil (red oil, oleine) — see Soap-
making.
Old brown Windsor, 480.
,, ,, modern inferior
kinds of, 481.
Oleine — see Soapmaking.
,, analysis of, 509, 510.
,, contains hydrocarbons, 258,
279, 496.
Olive, 467, 472, 508.
Paraffin and petroleum, 458, 476.
Perfumers', 450, 456, 479.
Pharmaceutical, 510.
Phpsphated, 476.
Primrose — see infra Rosin soap.
Remelted and blended toilet, 441,
478.
Rosin (yellow), 450, 451, 453, 473,
474, 509.
,, calculations respecting, 455,
465.
„ French process, 473.
„ primrose, 474, 509, 510.
Soap, special kinds of —
Rosin, primrose, analyses of, 509,
510.
Sand (brickdust, emery, fullers'
earth, kaolin, pipeclay, pumice-
stone, &c.), 476.
Shaving cream, 483.
Silicated, 451, 453, 462, 472, 474,
475.
,, calculations respecting,
455, 4(55.
,, objectionable for wool
scouring and laundry
purposes, 461, 475.
,, wastes less rapidly, 475.
Soft— see Soapmaking.
Starch (oatmeal, bran, cornflour,
dextrine, gluten, Iceland moss,
sawdust, &c. ), 477.
Sugared— see infra Transparent.
Sulphated, 451, 475.
Superfatted, 478, 479.
Toilet (fancy), 409, 441, 478-480.
,, analyses of, 511.
,, classification of, 512.
Tooth, 476.
Transparent, cold process, 450, 458,
476, 482.
,, - ,, analysis of, 511.
,, ,, calculations re-
specting, 465.
,, ,, injurious effects
on tender skins,
458, 459, 480,
482, 512.
,, ,, sugared, 458, 480,
482, 511, 512.
,, ,, transparency in-
creased by alco-
hol, glycerol,
sugar, 458, 481.
,, spirit process, 445, 446,
458, 474, 482.
,, ,, analyses of, 511.
,, ,, distillation of
spirit, 446, 482.
White Windsor, 481.
Wool scouring, 458.
Soap, water in, calculations, respect-
ing, 454, 464.
,, „ determination of — see
Soap analysis (water).
Soapmaking, classification of pro-
cesses — direct neutralisa-
tion, 450-456.
,, glycerides used and glycerol
retained, 450, 456-466.
,, glycerides used and glycerol
eliminated, 451, 466-473.
INDEX.
563
Soapmaking, factory operations —
Cleansing curd, 467.
Crutching, 438-440, 441.
Cutting, slabbing, and barring, 437,
438, 444, 449.
Dealkalising — see Soap, special
kinds of (dealkalised).
Drying, 438, 447.
Filling (loading), 438,450, 458, 462,
465, 472, 476, 483, 511.
Fitting, 451, 467, 470, 471.
Framing, 434-437, 444, 449.
Graining (cutting the soap ; salting
out), 54, 413, 433, 450, 469,
485.
Killing — see infra Manufacture of
curd.
Loading — see supra Filling.
Manufacture by cold process, 450,
457, 513
,, ,, calculations
respecting, 464-466.
,, by old German process,
449, 451, 472, 473.
,, of curd soap, boiling for
curd, 451, 467-470.
,, ,, analysis of curd
soap, 508, 510.
,, of fitted soaps — see supra
Fitting.
,, of hydrated soap, 450,
456, 461.
,, ,, (Swiss soap, Esch-
wegeSeife),461.
,, ,, under pressure, 450,
456, 461.
,, of marine soap, 450, 456,
461, 508, 509.
,, of milled soap — see infra
Milling.
,, of mottled soap, 451, 466,
471, 472, 509.
,, ,, modern inferior
kinds, 467, 472.
,, of oleine soap (oil soap),
258,451-453.
,, „ analyses of, 509, 510.
,, ,, calculations respect-
ing, 454-456.
,, of resinate of soda, 453.
,, of soft soap, 450, 456,
459, 466.
,, ,, analyses of, 510.
,, of transparent soap — see
Soap, special kinds of
(transparent).
,, of yellow soap (rosin soap)
— see Soap, special
kinds of (rosin).
Soapmaking, factory operations —
Milling, 446, 457, 479, 480.
Pearlashing, 451, 479, 489.
Perfuming (scenting), 441,444,448,
457, 478-480, 483, 512.
Pickling bars, 438.
Plotting, 448.
Preparation of leys, 411-426 — see
also Alkali, Alkalinity, Caus-
ticising, Potash, Soda.
,, calculation of quantity re-
quisite for saponification,
421-426.
Kernel ting, 441-443, 478.
Running off spent leys, 428, 432,
433, 469.
Salting out — see supra Graining.
Slabbing and barring, 437, 444, 449.
Stamping tablets, 444, 445, 449.
Stripping, 446.
Tinting, 441, 479.
Soapmaking, raw materials for, 302,
408-411.
Soaps, colonial, 509.
,, commercial (manufacturer's,
laundry, &c.), composition
of, by analysis, 508-510.
, , discoloration of, 266, 356, 479.
,, discoloured, bleaching of, 267.
,, ingredients in lubricating
' mixtures, 324-329.
,, jellifying of, 485.
,, manufacturers — see Soaps,
commercial.
,, metallic— see Metallic soaps.
, , mixed, formed from mixture of
acids and excess of alkali, 491.
,, salting out from solution
(Whitelaw) — see Soapmak-
ing (graining), 486.
,, solubility in water, &c., 485.
,, toilet, classification of, accord-
ing to free alkali, 512.
,, ,, composition of, by
analysis, 511.
Soapsuds, recovery of grease from —
see Grease.
Soap test, Clark's (water hardness),
485, 508.
Soda ash, 410.
„ ,, causticising — see Causti-
cising.
,, caustic (sodium hydroxide),410.
„ „ colour test, 151, 153,352.
,, ,, effect of fusion with
(soda lime) — see
Hydrogen.
,, ,, leys, alkalinity of, 414-
416, 419, 420.
564
INDEX.
Soda, caustic leys, employment in
soap boiling — see
Soapmaking.
,, ,, ,, preparation of, 411-
414.
,, ,, ,, quantity equiva-
lent to fats — see
Calculations.
,, ,, ,, storage of, 412.
,, ,, ,, variation of density
of, with tempera-
ture, 416.
,, ,, manufacture of, 410.
,, ,, use in making waggon
grease, 327.
,, ,, „ refining oils, 260, 261.
,, crystals, fused, use in oil re-
fining, 260.
,, degrees — see Degrees.
,, quantity equivalent to potash,
425.
,, trade, British custom as to
alkalinity, 420.
Sodium carbonate, action on potash
soaps, 488-490.
,, as lard adulterant, 306.
, , direct use in soapmaking,
409, 433, 453, 463.
„ leys, alkalinity of, 418
— see also Caustic soda.
,, use in making waggon
grease, 327.
,, use in refining oils, 256,
261.
Sodium chloride, action on potash
soaps, 451, 473, 490.
,, silicate, manufacture of, 463.
,, sulphate, Leblanc process, 410.
,, ,, used in refining oils, 256.
Soft soap — see Soapmaking.
Softening point, 61.
Solar stearine — see Stearine (lard).
Solutions for chilling baths, 67.
Solid adulterants of fats, &c., 123.
Solidification points — see Melting
points.
Soluble acid number, 168, 195.
Solubility of blown oils, 320.
of fatty acids in alcohol, '23.
, , in water, 23.
of lead salts in ether — see
Ether.
of oils, &c., in alcohol, 54.
,, in glacial acetic acid,
55-57, 329, 347, 349.
„ , , in water, 53, 54.
Solubility of oils in various solvents,
55, 341.
,, of wax in various sol vents, 359.
Solvents, extraction of oils by means
of, 114, 231-244, 303.
, , for oils, &c. — see Solubility.
,, oils used as, for odorous
matters, 302.
,, treatment of wool with, 337.
Souche're, adulteration of olive oil, 345.
Soxhlet's tube, 119, 238.
,, modifications of, 239.
Specific gravity of alkaline leys, 415-
419.
,, caustic soda, effect of
temperature on, 416.
,, lubricating oils, 325.
,, oils, &c., 76-94, 341.
,, ,, effect of light on, 130.
,, ,, ,, temperature
on, 79, 92-94.
Specific temperature reaction, 149.
Spectroscope, absorption, 50.
Spermaceti, 4, 14, 21, 292, 302, 353,
359-361.
,, added to soaps, 448.
,, adulterations of, 360.
,, candles — see Candles
(sperm).
,, chiefly obtained from oils
of toothed whales, 293,
300, 301.
class, 282, 301.
,, foots, 261, 360.
,, free cetylic alcohol in,
116, 171, 361.
,, iodine absorption of, 182.
„ refining, 261, 360.
,, saponification equivalent
of, 161.
,, various physical proper-
ties of, 68-70, 88, 91-93, 360.
Spills, manufacture of, 407.
Spirit oil (Yorkshire grease dis-
tillation), 277, 278.
Spirit soap (transparent) — see Soap-
making ; Soap (special kinds).
Spontaneous combustion, 132.
, , oxidation, 42, 1 1 3, 1 29 1 37, 323.
,, ,, more rapid under influence
of light, 130-132.
Square soap kettles, 433.
Squirting soap, 448.
Stamping machines, 444, 445.
Standard candles (sperm), 402.
,, oils, preparation of , 213, 340.
,, water as, specific temperature
reaction, 149.
Standards of comparison, oils and
mixtures, &c. , 340, 346.
,, efflux viscosity, 101.
„ specific gravity, 78, 89.
INDEX.
565
Stannic chloride, colour test, 151.
Starch as adulterant of beeswax, 359.
,, „ fats, 123, 307, 355.
Starch in soft soap, 459.
Steam, distillation with — see Distilla-
tion.
,, dry, 428-433, 459.
,, kettles heated by, 428, 432,
433, 441, 452, 459.
,, twirl (Morfit's) — see Morfit.
,, wet, 428-433, 459.
Stearic aldehyde, 1 4.
Stearin (stearic triglyceride), 4, 11,
110, 285.
Stearine, beef, 307, 309.
. , candle — ste Candle stearine.
,, candles — see Candles.
,, cokernut, 91, 92, 231, 283,
305, 3G3.
,, ,, use for nigh tlights,
candles, &c.,~363,
364, 407.
cotton seed, 91, 184, 230,
295, 304, 305,
307, 354.
,, ,, socalled, from distilla-
tion of foots, 262, 305.
,, French, 365.
,, lard (solar stearine), 93,
231, 307.
olive, 230.
,, tallow (pressed tallow), 231,
361, 407.
,, yield from ox fat. 311, 312.
Stearines (commercial products), 88,
91-93, 230, 285.
distilled, 110, 262, 277, 305,
324.
,, ,, adulteration of
tallow with, 355.
,, ,, from cotton seed
foots, 262, 305.
,, ,, from Yorkshire
grease, 277, 355.
,, ,, useinsoapmaking,
450.
, , expressed from natural oils,
&c., 11 0,229, 257,
305, 309, 407.
,, ,, used as lard adul-
terants, 307.
,, ,, . ,, as tallow
adulterants, 354.
,, from animal oils and fats,
230,231, 307, 311.
Stearolactone, 30, 39, 143,262,273,384.
, , correction for presence
of, 170, 273.
Stearyl cyanide, 21.
Steatite added to soft soap, 459.
,, (antifriction), 324.
Stein, Berge", and de lloubaix, sul-
phurous acid process, 380.
Stereochemical isomerism, 29.
Stills — see Distillation.
Stoddart, nitric acid test, 140.
Storax, 16, 19.
Stripping (soap), 446.
Strohmer, density of glycerol solu-
tion, 517.
,, refractive index, 51.
Stiircke, Carnauba wax derivatives,
18, 37.
Substitution derivatives, bromo, 26-
28, 30, 31, 34, 38,
41, 42, 45, 176.
,, ,, chloriodo, 177.
,, chloro, 30-32,267,364
„ ,, iodo, 26, 27, 30, 31,
38, 177 — see also
Iodine number.
Sudcake, 272.
Suds, grease recovered from — see
Grease.
Sugar in toilet soaps — see Soap,
special kinds (transparent).
,, test for sesame oil, &c., 153,
346 352.
Suet, 55, 70,' 91/161, 164, 181, 298.
Suint, 337.
Sulphur, adulterant of beeswax, 359.
,, candles, 407.
, , chloride reaction, 154-156,341 .
„ dioxide (liquefied) as solvent,
236.
,, ,, use in candle stearine
making, 369, 370.
,, trioxide, use of, in bleaching
oils, 264.
Sulphuric acid, action on glycerol, 144.
,, ,, isoleic acid, 38.
,, ,, oleic acid, 27, 29.
,, ,, olein and ricin-
olein — see Oils
(Turkey red).
,, colour reactions with oils,
151-153, 294, 341,352,354.
,, decomposing rock by, 366.
,, heat evolved by — see Oils
(heat evolution).
,, preparation of, of constant
strength, 148.
,, presence of, in oils, &c., 123.
,, reaction with cholesterol
and allied bodies, 17.
,, refining with, 123, 255, 259.
,, removal of lime salts from
bone fat by, 256.
566
INDEX.
Sulphuric acid, saponificatioii by, 143,
145, 380-382.
,, test for hydrocarbons in
beeswax, 359.
,, use of, in finishing hot
press cake, 368.
,, ,, in rendering tallow, 249.
,, ,, in Yorkshire grease
process, 271.
Sulphurised constituents of oils, 123,
154.
Sulphurous acid as bleaching agent,
264.
,, ,, saponifying agent,3SO.
Sumbul root, 25.
Summer oils — see Oils, summer.
„ railway grease, 327.
Superheated steam — see Distillation
(with superheated steam).
Suspended matters, action of. in re-
moving mucilage, 255.
,, in solid fats, &c., 123, 341.
,, removal of, from oils, &c.,
228, 254-256.
Sustainer for night lights, 406.
Sweet water (crude glycerol solution)
— see Glycerine manufacture.
Sycocerylic alcohol, 16.
.Synthesis of glycerides, 11.
TABLES of errors, hydrometer, 82, 83.
,, hydrostatic balance, 83, 84.
Tablets (soap), cutting and stamping,
444.
Tallow (ox tallow, mutton tallow ;
ox, sheep, &c. , fat ; beef
fat), 3, 21, 55, 56, 29 3, 299,
303, 311, 322, 354.
, , adulteration of, 1 23, 258, 354-
356, 370.
bleaching of, 264-266.
candles— see Candles (tallow),
different varieties of, 354.
engine, 324.
flashing point, 128.
free fatty acids present in,
355, 356.
iodine number, 181-184, 356.
,, useful as test of
quality, 356.
melting point, 68, 69, 355.
,, of fatty acids
from, 69-71,
74-76.
neutralisation number of
fatty acids from, 164.
Tallow oil — see Oil (tallow).
,, rancid, cleansing of — see
Rancid.
,, Reichert number, 175.
,, relative viscosity, 102-105.
,, rendering, 246-251.
,, saponification equivalent and
total acid number, 159,
161, 355.
,, specific gravity, 88-93, 355.
,, stearine — see Stearine
(tallow).
,, unsaponifiable matters
present in, 257.
,, use of, in lubricating mix-
tures, &c. , 322-328, 356.
,, ,, in soapmaking, 356, 408
— see Soapmaking.
,, valuation of, by Dalican's
method, 74, 355.
,, „ de Schepper and
Geitel's tables, 76.
Tallows, vegetable — see Butters, vege-
table.
Tannery grease, 299.
Tannin, use of, in refining, 256, 263.
Tapers, 389.
Tar as lubricant — see Lubricants.
Tariri, 36.
Taste of oils, &c., 49, 341.
,, improved by presence of
free acid, 116.
Teal, oil bleaching, 264.
Temperature of complete fusion, 61.
,, of incipient fusion, 62.
,, of turbidity (Valenta's test),
55-57.
,, reaction, specific, 149.
,, variation of specific gravity
with, 92-94, 416.
,, ,, viscosity with, 102-106.
Tempering metals in oil baths, 302.
Testing machines, viscosity, 94.
Tetrabromides, 31, 34, 36, 176.
Tetracetyl derivative, 35.
Tetrachloride of carbon — see Carbon.
Tetraiodides, 31.
Textile fabrics, oil used in prepara-
tion of, 270, 272, 279, 302.
Texture, physical, of oils, &c., 47, 341.
Thenard process (oil refining), 259.
Thermal araeometer, Langlet's,82,347.
Thermeleometer, Jean's, 151.
Thermohydrometer, Fletcher's, 80.
Thermometric scales, 57.
Thiocyanic ethers, 15, 123.
Thomson and Ballantyne, blown oils,
320.
,, ,, iodine numbers, 180.
INDEX.
567
Thomson and Ballantyne, iodine num-
bers of linseed oil,
180, 351.
,, ,, specific temperature
reaction, 149,349.
,, ,, unsaponifiable mat-
ters, 259.
,, ., Valenta's test, 57.
Thousandfold scale of specific gravity,
83, 84.
Thum, fractional saturation, 13.
,, free acids formed by hydro-
lysis, 12.
Thymol,
Tilghmann, hydrolysis under pres-
sure, 385.
,, soapmaking under pres-
sure, 463.
Time of efflux — see Viscosity.
Titration, 23, 116, 161, 168, 173, 323,
328, 352, 359, 420— see
also Soap analysis.
,, acetyl number, 198.
,, of alkaline leys preferable
to density valuation, 420.
,, test, fatty acid — see Soap
analysis (determination
of free alkali).
Toluene (solvent for wax in soap), 496.
Tomlinson, cohesion figures, 345.
Torches, 312, 362.
Total acid number (saponification
number, Kcettstorfer number), 33,
157, 168, 194, 341.
Transparent soap — see Soapmaking,
Soap (special kinds), Colloidal
state of soap.
Traube, friction in tubes, 109.
Triacetin, 8, 186.
Triglycerides, 9.
,, synthesis of, 11.
Triglycerol, 8.
Tiinnermann, specific gravity of alka-
line leys, 415, 417.
Turkey fat, 298.
,, red oils — see Oils (Turkey red).
Turpentine — see Oil (turpentine).
Turpentine, crude (Meinecke's rosin
soap), 473.
Turtle fat, 299.
Twaddell, hydrometer scale, 84, 86.
Twitchell, rosin in soap, 503, 504.
u
UNIT mill (Anglo-American system),
217.
Unsaponifiable matters contained in
oils, &c., 116,257,258,341,355.
Unsaponifiable matters in candle
stearine products, 371-374.
,, in Yorkshire grease, 273-279.
,, determination of , 119-124.
,, proportions usually present in
oils, 257, 258.
,, ,, in soaps, 258.
Unsapoiiified fat, amount less with
longer time, 373.
,, in red oils, 370,
377-379.
in rock, 371-374.
,, in separation
cakes and press
cakes, 376-379.
,, in soap, 119, 371.
, , interferes with
crystallisation,370.
Unsaturated compounds, acids, 24.
,, alcohols, 15.
,, hvdrocarbons, 3,
"24, 26.
, , oxidation of, 44.
Unguents in toilet soaps, 448.
, , lanolin preparations as, 338.
,, oils used for, 302.
Ure, soft soap analyses, 510.
Urine, damaluric acid from, 25.
Utilisation of fat of an ox, 311.
red oils— see Red oils.
VALENTA'S test— see Acid (acetic).
Valerin (valeric triglyceride), 20, 301.
Vapour bath, AmbuhFs, 80.
Varnish making, 302.
Variation of constituents of oils with
soil, climate, &c., 111.
,, density with tempera-
ture— see Expansion.
Vaseline, 91.
,, in soaps, 448.
Vegetable alkali, 410.
,, fats, butters, and tallows
— see Butters (vegetable).
,, lard— see Lard.
Versmann, glycerine manufacture,
515.
Villavecchia and Fabris, test for
sesame oil, 346.
,, ,, viscosity, 106.
Vincent, boiling oils, 317.
Viscidity of oils increased by blowing,
164— see Oils (blown).
Viscosimetry, 94-109.
Viscosity (body), 47, 94, 101.
,, degree, 102.
568
INDEX.
Viscosity, determination in absolute
measure, 107.
„ effect of lighten, 131.
„ efflux, 48,94-106, 324-326,341.
,, of oils increased by addition
of caoutchouc, 323.
„ „ by blowing, 320.
,, ,, by metallic soaps,
121, 324.
,, standards of, 101.
Voelcker, amount of oil in linseed
cake, 213.
Volatile acid number, 176, 195, 341.
„ acids, 22, 113.
,, ,, determination of — see
Reichert test.
Volatility of lubricating oils, 325.
Vulcanising, 154, 318.
W
WAGGON grease — see Lubricants.
Wagner, refining with, zinc chloride,
260.
,, rule concerning oxidation, 44.
Wakefield fat — see Yorkshire grease.
Walton, linoleum manufacture, 318.
Wanklyn, aldepalmitic acid, 24.
,, and Fox, glycerine valua-
tion, 519.
Warren, sulphur chloride and oils, 155.
Washballs (soap), 448.
Waste cleansing — see Engine waste.
Water, action of, on silver bromo-
stearate, 25, 30.
,, agitation with, as purifying
agent, 261.
,, as standard for efflux velo-
city, 101.
,, ,, for specific tem-
perature reaction, 149, 150.
,, contained in beeswax, 359.
oils, 122-124,341.
,, hot, extraction of vegetable
oils, &c. , by means of,
200-202.
,, ,, rendering animal fats,
&c., with, 247.
,, solubility in — see Solubility,
Water bath for melting points, 60-64.
,, ,, specific gravity, 80.
,, ,, viscosimetry, 95-101.
Watt, bichromate bleaching process,
265.
,, chloride of soda bleaching pro-
cess for soaps, 267.
Watts— see Richardson and Watts.
Wax candles — see Candles.
Waxes, animal and vegetable —
Abyssinian, African, Andaquia,
Antilles, 302.
Beeswax, 4, 14, 21, 357-359.
,, addition of fatty matter or
oil of turpentine facilitates
air bleaching, 268, 269, 358.
,, adulterations of, 359.
„ air bleaching, 264, 268, 357,
358.
,, ,, produces little change
in density, 358.
,, bibliography of, 359.
,, bleached by chlorine apt to
contain chloro substitution
products, 267, 364, 390.
,, bleaching by chemical pro-
cesses, 264-267, 357.
,, ,, increases total acid
number, and renders
more crystalline,
266, 269, 364
,, bromine absorption, 178.
,, class, 282, 301, 302..
,, ester number, 358.
,, free acid number, 358.
,, fusing point, 68, 69, 358.
,, iodine number, 269, 358.
,, iodine number diminished
by chemical bleaching, 269.
,, preparation of 201, 357.
,, saponification equivalent
and total acid number,
160, 269.
,, solubility in solvents, 357.
,, specific gravity, 88, 91-93,
358.
,, virgin, 357.
Carnauba wax, 14, 21, 301.
,, an oxyacetic acid from,
37.
bromine absorption, 178.
class, 282, 301.
glycol from, 5, 18.
saponification equiva-
lent, 160.
specific gravity, 91.
used as beeswax adul-
terant, 359.
Chinese wax (Peh-la), 14, 21,91, 302.
,, extraction by hot
water process, 201.
Cordillera wax, 301.
Cowtree wax, 301..
Ficus wax, (fig wax, Getah wax),
14, 301.
Indian wax (Arjun wax), 302.
Japanese wax, 5, 21, 295.
,, bromine absorption, 178.
INDEX.
569
Waxes, animal and vegetable —
Japanese wax contains practically
no olein, 295.
,, fusing point, 68-71.
,, iodine number, 181-184.
, , purification and bleach-
ing, 268.
,, saponiti cation equiva-
lent and total acid
number, 160.
,, solubility in alcohol, 55.
,, specific gravity, 88, 91-
93.
,, unsaponifiable matter
contained in, 257.
„ yield of, 242.
Myrtle wax, 71, 91, 178, 295.
Niin wax (niin fat), 302.
Ocuba wax, 243, 295.
Otaba wax, 295.
Palm wax, 301.
Paraffin wax, 2, 5, 21, 91-93.
,, adulterant of bees wax and
spermaceti, 359, 361.
,, as candle material — see
Candles.
„ manufacture of, 230, 364.
Pe-la (Peh-la, Pe-lah) wax — see
supra, Chinese wax.
Petha wax, 301.
Spermaceti wax— see Spermaceti.
Ucuba wax, 295.
Waxes, free alcohols in, 114, 116.
,, general nature of, 1.
, , glyceridic and non-glyceridic,
3-5, 282, 301, 302.
,, liquid, 6.
,, mineral (earthwax) — see Ozo-
kerite.
,, mostly indigestible, 303.
,, used as spermaceti adulter-
ants, 361.
,, vegetable, hot water process
of preparation, 201.
Waxy matters, separation from oils,
119.
Wedge presses, 1 99, 203.
Chinese, 200.
Wenzell, expansion, 93.
Werner, oxyoleates, 332.
Westphal, hydrostatic balance, 79, 80.
Wet steam — see Steam.
Whale blubber, extraction of oil
from, 247.
Whales, toothed, yield most sper-
maceti, 293, 300, 301.
Whitelaw, salting out soap, 486.
Whitelead in paint, 135.
Whiting, adulterant of tallow, 355.
Wicks, 312, 362, 363, 394.
,, charring of, 116, 260, 313.
,, Palmer's metallic, 394.
,, pickling, 394.
Wilde, de, and Eeichler, conversion
of oleic into stearic acid, 387.
Wilson, acetyl number, 188, 335.
,, analysis of Turkey red oils,
333-335.
,, soap analysis, 495, 499.
,, viscosity, 102.
,, water in soap, 495.
Wilson and Payne, hydrolysis by
superheated water, 385.
Wilson's process (preparing candle
material), 262, 380, 334.
„ ,, (tallow rendering), 250.
Wimmell, melting points, 68.
Winter oils — see Oils (winter).
,, railway grease, 327.
Wire (soap cutting), 437.
Wollny, Keichert number, 53, 175.
Wool cleansing, wool scouring, 271,
337, 338.
,, ,, injurious effect of
alkaline and
silicated soaps
— see Soap,
alkaline ; Soap
(special kinds),
silicated.
Wool fat, analysis of, 276.
Woolgrease, 3, 70, 161, 182, 184, 299,
302, 337, 461 -.see York-
shire grease; Lanolin.
,, effect on soap, 258.
,, tallow adulterated with,
258, 354, 369.
Wool oil (from Yorkshire grease dis-
tillation), 279.
Wright, Alder (author), analyses of
manufacturers' and toilet
soaps, 508-512.
,, analysis of rock, steariiie
cakes, red oils, &c.,
371-375.
, , analysis of soap (free alkali).
500.
,, autoclave experiments, 373.
,, Cantor lectures, 487, 512,
523.
,, classification of soaps ac-
cording to alkalinity, 512.
,, dealkalising process, 453,
461, 484.
,, glycerine valuation, 523.
, , hydrolysis of soap solutions,
487.
,, methoxyl test, 192.
570
INDEX.
Wright, Alder, use of iodine number
in tallow valuation, 356, 375.
Wright (Alder) and Muirhead, zinc
chloride and oils, 141.
Wright (Alder) and Thompson, chem-
istry of soap,
490-492.
,, ,, Cladding's pro-
cess, 502.
,, ,, hydrolysis of
soap, 487.
,, ,, systematic soap
analysis, 494.
XYLENOL, 16.
YELLOW ochre, beeswax adulterant,
359.
Yield of fatty acids from oils, &c.,
74, 163.
,, fatty matter from seeds, nuts,
beans, &c., 241-244, 348, 351.
,, glycerol from oils, &c. , 75, 162.
,, solid stearine, 368.
Yorkshire grease, 110, 271-279, 324.
,, adulteration of tallow with,
258, 354.
,, amount of unsaponifiable
matters increases with
the density, 277.
Yorkshire grease, analysis of, 273.
,, distillation of, 277, 383.
,, hydrocarbons in distilled,
262.
,, injurious effect on soap, 258.
ZEISEL'S test — see Methyl number.
Zinc and hydrochloric acid, as de-
chlorinising agents, 35. 36.
,, chloride, action on oils, 141, 142,
153.
,, ,, action on oleic acid, 39,
142, 262, 386.
,, ,, colour test, 153. 341.
,, ,, refining by means of,
255, 260.
,, dust, as dechlorinising agent,
27, 31.
,, isoleate, 30.
,, oxide (antifriction) , 328.
,, ,, as saponifying agent, 379,
410, 515.
,, salts, separation of rapic and
erucic acids by, 41.
,, used in refining, 262, 263.
,, sulphate (boiled oils), 262.
,, soap, added to oils, &c., 121.
,, white, in paint, 135.
Ziirer, conversion of oleic into stearic
acid, 386.
SJjpx
OF THE
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