Book _JP^5__
11 '2-0
THE
FOUNDER'S MANUAL
A PRESENTATION OF MODERN
FOUNDRY OPERATIONS
FOR THE USE OF
FOUNDRYMEN, FOREMEN, STUDENTS
AND OTHERS
BY
DAVID W. PAYNE
EDITOR OF " STEAM "
245 ILLUSTRATIONS
SECOND PRINTING, CORRECTED
NEW YORK
D. VAN NOSTRAND COMPANY
25 Park Place
1920
'S ^^^
Copyright, 1917, by
D. VAN NOSTRAND COMPANY
?> 0-1 \ ey b
^3 ■'^<^6Z?^>
Stanbopc jprcss
F. H.GILSON COMPANY
BOSTON, U.S.A.
PREFACE
While there is li-ttle a foundryman needs to know
which has not been fully treated by competent authori-
ties, there is not, so far as I am aware, any summary of
this great mass of publications.
In a foundry experience covering many years, I have
frequently spent hours at a time in searching for special
information. Believing, therefore, that a compilation of
this matter, with authoritative instruction for the solu-
tion of the many problems which are continually pre-
sented in the foundry, all properly arranged for ready
reference, would receive a favorable reception, an attempt
has been made to meet this need by the production of
this book.
The material for the Manual has been drawn from
every available source. The proceedings of the American
Foundrymen's Association have furnished no end of
information. The publications of Professors Turner,
Porter, Reis, Dr. Moldenke, Messrs. Keep, Longmuir,
Outerbridge, West and others have been most carefully
searched. Much has been taken from " The Foundry,"
" Castings " and " Iron Age." A great many of the
" Foundry " records are given in full.
Possibly, in some cases, special credit for extracts
has not been accorded; for such omissions indulgence
is asked, as there has been no intentional neglect or
lack of courtesy.
iv Preface
In tlu- sck'ction of the iiKilcrial for the Ijook, i)ropcr
consideration has Ijccn takt-n of Ix-Kinners and others
who niay ha\e not gotten xcry far in their acfjuisition
of foundry information. For such men, it is also hoped
the bo(jk will be of good service.
As regards the price lists and discounts which are
given in connection with man)- ftjundry supplies, it
should be stated that these are not quoted as current
prices. They are olTered simply as furnishing a guide
to close approximation of costs.
The matter for the preliminary portion of the book
relating to elementary Mathematics, Mechanics, etc.,
has been taken in large part from such authorities as
Rankine, Bartlett, Wentworth, Trautwine, Kent, Jones
and Laughlin, Carnegie Steel Co., and the Encyclopedia
Britannica.
D. W. P.
New York, Jan., 1917.
CONTENTS
Page
CHAPTER I
Elementary Mathematics i
Ratio and Proportion, i. Root of Numbers, 3. Percentage,
5. Algebra, 7. Equations, 11. Plane Geometry, 15. The
Parabola, 22. The Hyperbola, 23. Properties of Plane Fig-
ures, 24. Mensuration, Plane Surfaces, 26. Solids, 30.
CHAPTER II
Weights and Measures 35
Commercial Weights and Measures, 36. Metric Weights and
Measures, 40. Measures of Work, Power and Duty, 45.
Mathematical Tables, 46.
CH.\PTER III
Natural Sines, Tangents, Etc 107
Solution of the Right-angled Triangle, 109. Solution of Ob-
lique-angled Triangles, 109. Tables of Sines, Tangents and
Secants, no. Approximate Measurement of Angles, 115.
Tapers per foot and Corresponding Angles, 117.
CHAPTER IV
Materials 119
Wire and Sheet Metal Gauges, 119. Weights of Iron and
Steel, 122. Cold-rolled Steel Shafting, 140. Galvanized and
Corrugated Sheet Iron, 141. Sheet Tin, 142. Copper and
Brass, 143. Metal Fillets, 145. Iron Wire, 146. Nails and
Tacks, 148. Threads, 149. Bolts, Nuts and Washers, 150.
Set Screws, 160. Turnbuckles, 162. Cotters, 164. Thumb-
screws, 165. Rivets, 166. Iron Pipe, 167. Tin and Zinc,
169. Lead Pipe, 171. Chains and Cables, 173. Sprocket-
wheels, 176. Modulus of Elasticity, 181. Deflections, 184.
Modulus of Rupture, 185. Moment of Inertia, 187. Strength
of Beams, 188.
V
vi Contents
PaKC
CIIAITKR V
Mk( nANics 191
Acceleration of Falling Bodies, igi. Center of Gravity, 194.
Radius of Gyration, 197. Si>ccific Gravities, 108. Physical
Constants, 202. Kxpansion of Solids, 205. Measurement
of Heat, 207. Radialiun of Heat, 208. Equivalent Tem-
IKTalurcs, 211. Strength of Materials, 213. Properties of
Air, 215. Pressure of Water, 219. Electrical and Mechanical
Units, 220.
(IIAITKR \I
Alloys 222
Alloys of Cop|)er, Tin and Zinc, 222. Aluminum bronze, 226.
Bearing Metals, 226.
Belting 227
Formulas for Width of Bells, 228. Speed of Belts, 229. Rules
for Speeds and Diameters of Pulleys, 231. Formulas for Cast
Iron Fittings, 232.
CIL\PTER VII
Useful Information 234
Shrinkage of Castings, 234. Window Glass, 236. Fire Clays,
236. Weight of Metals, 239. Iron Ores, 240.
CHAPTER VIII
Iron 241
Physical Properties of Iron, 241. Grading Pig Iron, 242.
Standard Specifications for Pig Iron, 246. Machine-cast Pig
Iron, 248. Charcoal Iron, 250. Grading Scrap Iron, 250.
CH.\PTER IX
Chemical Constituents of Cast Iron 252
Influence of Carbon, 252. Loss or Gain of Carbon in Re-,
melting, 254. Influence of Silicon, 256. Influence of Sulphur,
260. Influence of Phosphorus, 263. Influence of Manganese,
265. Aluminum, 266. Nickel, 267. Titanium, 267. Vana-
dium, 268. Thermit, 270. Oxygen, 270. Nitrogen, 271.
CHAPTER X
Mixing Iron 273
Mixing by Fracture, 273. Mixing Iron by Analysis, 274.
Castings for Agricultural Machinery, Cylinders and Fly-
wheels, 277. Castings for Chills, Motor Frames and Gas En-
Contents vii
Page
gines, 278. Castings for Gears, Hydraulic Machinery and
Locomotives, 280. Castings for Pulleys, Radiators and Heat-
ers, 284. Castings for Weaving, Woodworking Machinery,
etc., 287.
CHAPTER XI
Steel Scrap in Mixtures of Cast Iron 290
Recovering and Melting Shot Iron, 291. Burnt Iron, 293.
Melting Borings and Turnings, 293.
CHAPTER XII
Test Bars 294
Report of Committee on Test Bars of American Foundry-
man's Association, 294. Proposed Specifications for Gray
Iron, 296. Patterns for Test Bars of Cast Iron, 297. Erratic
Results, 298. Table of Moduli of Rupture, 299. Comparison
of Test Bars, 302. Casting Defects, 304. Circular Test Bars,
304. Effect of Structure of Cast Iron Upon its Physical Prop-
erties, 306. Mechanical Tests, 307. Chemical Analysis, 308.
Chilled and Unchilled Bars, 310. Forms of Combination of
Iron and Carbon, 313.
CHAPTER XIII
Chemical Analyses 315
Strength, 315. Elastip Properties, 322. Hardness, 324.
Grain Structure, 329. Shrinkage, 329. Fusibility, 332.
Fluidity, 334. Resistance to Heat, 335. Electrical Proper-
ties, 338. Resistance to Corrosion, 340. Resistance to Wear,
342. Coefficient of Friction, 342. Casting Properties, 343.
Micro-structure of Cast Iron, 345.
CHAPTER XIV
Standard Specifications for Cast Iron Car Wheels 350
Chemical Properties, 350. Drop Tests, 350. Marking, 351.
Measures, 351. Finish, 351. Material and Chill, 351. In-
spection and Shipping, 352. Retaping, 353. Thermal Test,
353. Storing and Shipping, 354. Rejections, 354.
Standard Specifications for Locomotive Cylinders 355
Process of Manufacture, 355. Chemical Properties, 355.
Physical Properties, 355. Test Pieces, 355. Character of
Castings, 355. Inspector, 355.
viii Contents
Standard SPECiricATioNS for Cast Iron Pipe 356
Allowable Variations, 356. Defective SpJRots, 357. Si)ccial
Castings, 357. Tables of (Jeneral Dimensions, 358. Marking,
360. Quality of Iron, 360. Tests, 361. Cleaning and Coat-
ing, 301. Contractor, Engineer, Inspector, 362. Tables of
Weight of I'ipc, 364.
CHAPTER XV
Mechanical Analysis 371
Shrinkage Chart, 372. Keep's Strength Table, 375. Stand-
ard Methods for Determining the Constituents of Cast Iron,
377-
CJLVPTER XVI
Malleable Cast Iron 382
Black Heart, 382. Ordinary or Reaumur Malleable Iron, 385.
Temperature Curve for Annealing Oven, 386. Analysis Be-
fore and After Annealing, 387. American Practice, 389.
Specifications, 392. Comparison of Tests, 392.
CHAPTER XVII
Steel Castings in the Foundry 394
Normal Steels, 396. Bessemer Process, 396. The Baby Con-
verter, 397. Annealing, 400. Tropenas Process. 401. Chem-
istry in the Process, 403. Converter Linings, 404. Standard
Specifications, 409. Open Hearth Methods, 411. Compara-
tive Cost of Steel Castings, 417. Basic Open Hearth, 418.
Acid Open Hearth, 419. Converter, 420. Converter with
Large Waste, 421. Crucible Castings, 423. Electric Fur-
nace, 424.
CHAPTER XVIII
Foundry Fuels 425
Anthracite Coal, 425. Coke, 425. By-product Coke, 426.
Effect of Atmospheric Moisture Upon Coke, 427. Specifica-
tions for Foundry Coke, 428. Fluxes, 429. Comparison of
Slags, 432. Fire Brick and Fire Clay, 434. Fire Sand, 435.
Magnesite, 436. Bauxite, 436.
CHAPTER XIX
The Cltola 437
The Lining, 437. Tuyeres, 439. The Breast, 440. Sand
Bottom, 441. Zones of Cupola, 442. Chemical Reaction in
Contents ix
Page
Cupola, 443. Wind box, 445. The Blast, 446. Sturtevant
Blowers, 448. Buffalo Blowers, 449. Root Blowers, 449.
Diameter of Blast Pipe, 450. Dimensions of Cupolas, 451.
Charging and Melting, 452. The Charging Floor, 453. Melt-
ing Losses, 454. Melting Ratio, 461. Appliances About
Cupola, 462. Ladles, 462. Tapping Bar, 463. Bod Stick,
463. Capacities of Ladles, 464. Applying Metalloids in La-
dles, 465. Cranes, 466. Spill Bed, 466. Gagger Moulds, 467.
CHAPTER XX
Moulding Sand 468
Bonding Power, 468. Permeability and Porosity, 468. Re-
fractoriness, 469. Durability, 469. Texture, 469. Grades,
470. Sand for Brass, 472. Testing Sand, 473. For Dry Sand
Moulding, 477. Skin Drying, 469. Core Sand, 479. Core
Mixtures, 480. Dry Binders, 481. Parting Sand, 486.
Facings, 486.
CHAPTER XXI
The Core Room and Appurtenances 492
Core Oven Carriages, 496. Mixing Machines, 497. Sand
Conveyors, 497. Rod Straighteners, 497. Wire Cutter, 497.
Sand Driers, 49S. Core Plates, 498. Core Machines, 499.
Cranes and Hoists, 499.
CHAPTER XXII
The Moulding Room 501
Cranes, 502. Hooks, Slings and Chains, 502. Lifting Beams,
503. Safe Loads, 504. Binder Bars, 505. Clamps, 506.
Flasks, 506. Iron Flasks, 510. Sterling Steel Flasks, 515.
Snap Flasks, 517. Slip Boxes, 519. Pins, Plates and Hinges,
519. Sweeps, 522. Anchors, Gaggers and Soldiers, 523.
Sprues, Risers and Gates, 524. Top Pouring Gates, 526.
Whirl Gates, 527. Skim Gates, 527. Horn Gates, 527.
Strainers and Spindles, 528. Weights, 528. Chaplets, 528.
Liquid Pressure on Moulds, 529. Nails, 536. Sprue Cutters,
537-
CHAPTER XXIII
Moulding Machines 538
Jigs, 540. Flasks, 547. Moulding Operations, 549.
X Contents
Pace
cnAi'iik xxi\'
CoNTiNLors .Mki.tin<; 551
Multiple Moulds, 555. iVrmancnt Moulds, 558. Centrif-
ugal Castings, 561. Castings Under Pressure. 562. Direct
Casting, 562. Car|K'ntiT Shoj) and Tool Room, 502. The
Cleaning Room, 563. Tumbling Mills, 563. Chipping, 566.
Grinding, 566. Sand Blast, 566. Pickling, 567.
CHAPTER XXV
IJktkrmination ov Weight ok Castings 56Q
My Wci^hl of Patterns, 504. Weight of Pallern Lumber, 569.
I'orniulas for Finding Weight of Castings, 570. Formulas
for Weight on Cope, 575.
CIIAl'TER XXVT
Water, Lighting, Heating and Ventilation 577
Water Supply, 577. Lighting, 57S. Heating and Ventila-
tion, 579.
CHAPTER XXVn
r'ouxDRv Accounts 587
Foundry Requisition, 588. Pattern Card, 589. Pig Iron
Card, 590. Core Card, 591. Heat Book, 592. Cleaning
Room Report, 597. Weekly Foundry Report, 600. Monthly
Expenditure of Supplies, 601. Comparison of Accounts, 605.
Transmission of Orders, 611. American Foundrymen's As-
sociation Methods, 612. Cost of Metal, 617. Moulding, 619.
Cleaning and Tumbling, 620. Pickling, 621. Sand Blast-
ing, 622. Core Making, 623. A Successful Foundry Cost
System, 625. Castings Returned, 629.
CHAPTER XXVni
Pig Iron Directory 633
Classification and Grades of Foundrj' Iron, 633. Coke and'
Anthracite Irons, 635. Chnrcoal Irons, 655.
Authorities 660
Index ? ; 663
Most readers of this book will, without doubt, be familiar with the
ordinary mathematical processes; to them, such brief references as may-
appear, will, perhaps, seem superfluous. There may be, however, those
who, from disuse or otherwise, are not so circumstanced. For their
convenience such information will be given as may facilitate the inter-
pretation of the formulas and calculations herein.
SIGNS AND ABBREVIATIONS
A prime mark ' above a number
means minutes or linear feet;
as lo' means ten minutes or ten
linear feet.
Two prime marks " likewise mean
seconds; or linear inches; as lo"
indicates lo seconds or lo linear
inches.
The sign D means square, as D'
square foot, D " square inch.
The sign O means round or cir-
cular, as O" circular inch.
The sign / means an angle.
The sign L means a right angle.
The sign J- means a perpendicular.
The sign ir, called Pi, means the
ratio of the circumference of a
circle to the diameter, and is
equal to 3.14159.
The sign g means acceleration due
to gravity and equals 32.16 foot
pounds per second.
The sign E indicates the coefl&cient
of elasticity.
The sign / indicates the coefficient
of friction.
The sign M indicates modulus of
rupture.
The sign log indicates the common
logarithm.
The sign log e ) hyperbolic
or log hyp. ) logarithm.
R.p.m. revolutions per minute.
H.P. horse power.
K.W. Hr. Kilowatt hours.
A.W.G. American wire gauge.
B.W.G. Birmingham wire gauge.
A.S.M.E. American Society of
Mechanical Engineers.
A.F.A. American Foundrymen's
Association.
B. F. A. Birmingham Foundry-
men's Association.
I.S.I. Iron and Steel Institute.
FOUNDERS MANUAL
ELEMENTARY MATHEMATICS
CHAPTER I
SECTION I
ARITHMETIC
It is deemed unnecessary to present anything under this branch of
mathematics, except Ratio and Proportion, Square and Cube Roots,
AUigation and Percentage. These operations are applied so frequently
in the foundry that, it is believed, a simple explanation of them will not
be out of place.
Ratio and Proportion
The ratio of two numbers is the relation which the first bears to the
second and is equivalent to a fraction obtained by dividing the first
number by the second.
Thus: 5:7 = 5 or 7:5 = 1.
When the first of four numbers is the same fraction of the second, as
the third is of the fourth, the first has the same ratio to the second as the
third has to the fourth, and the four numbers are in proportion. Pro-
portion, therefore, is the equality of two ratios.
Thus:
I = T5 = I-
The proportion is expressed, 4 : 6 :: 10 : 15, and is read, 4 is to 6 as 10
is to 15. The first and fourth terms are called the extremes; the second
and third the means.
The product of the extremes is equal to the product of the means;
thus in the above proportion 4 X 15 = 6 X 10 = 60. Hence where
three terms of the proportion are known the fourth can be found.
, .1 c
, BC „ BC „ AD ,. AD
BC, — = T-, -
= -^, D = —r, B = ,r, C = - ..- .
^' B D'
D' .1 ' C ' B
2 Arithmclic
Thus: Find the numlxir to which lo bears the same ratio as 4 does to 6.
4 : f) :: lo : re(iuired number.
Required number e(|uals "/ = '5-
Where one extreme and both means are known, to find the other
extreme, divide the product of the means by the known extreme.
Where Ijolh extremes ami one mean are known, to find the other mean,
divide the prcKiuct of the extremes by the known mean.
I'or the purpose of illustrating these rules replace the figures in a
proportion, by the letters .1, B, C, D, and write .1 : B :: C : D; then,
AD
To state the terms of a simple proportion where three are given;
l)lacc that as the third term which is of the same kind as the required
lerm; then consider whether the required term should be greater or less
than the third term; if greater, make the greater of the two remaining
terms the second and the other the first term. But if the required term
should be less than the third term, place the smaller of the first two as
tiie second term and the greater as the first.
Thus: What is the price, per net ton, of pig iron sold at $17.50 gross
ton?
.'Vs the price is required, Si 7.50 becomes the third term. Since the
net price is less than the gross, 2000 is the second term and 2240 the first.
Tlie proportion is then written:
2240 : 2000 :: Si 7.50 : answer.
2000 X Si 7.50
2240
Si 5. 62 = required price.
.'\gain the ratio of net to gross is m^ = .892 +. Therefore, the net
price is equal to the gross multiplied by 0.892 +; or Si 7.50 X .892 =
S15.62; or the net price being known the gross is equal to the net miilli-
]jiied by UU; $15.62 X 1.12 = Si7-50-
Compound Propojtion
Where the ratio of two quantities depends upon a combination of
other ratios, the proportion becomes a compound proportion. In this
as in simple proportion, there is but one third term, and it is of the same
kind as the required term; there may be two or more first and second
terms. Set down the third term as in simple proportion; consider each
pair of terms of the same kind separately and as terms of a simple pro-
portion, and arrange them in the same manner, making the greater of
Men
25 :
36::
Days
16 :
17 ::
Fifths of work
3 :
2
36 X 17
X 2
X 10
25 X
16X3
Roots of Numbers 3
the pair the second term, if the answer considered with reference to this
pair alone should be greater than the third term; or the reverse if it
should be less.
Set down the terms under each other in their order of first and second
terms. Multiply the product of all the second terms by the third term
and divide this product by that of all the first terms.
Example. — If 36 men working 10 hours per day perform f of a piece
of work in 17 days, how long must 25 men work daily to complete the
work in 16 days?
The length of the day will be greater the fewer the men, and the fewer
the days are; and less, the less the work is; hence, the above problem
is stated as follows:
5ji- = 10.2 hours per day.
Roots of Numbers
To Extract the Square Root of a Given Number
Point off the number into periods of two figures each, beginning with
units; if there are decimals, begin at the decimal point, separating the
whole number to the left and the decimal to the right into such periods,
supplying as many ciphers in groups of two, as may be desired.
Find the greatest number whose square is less than the first left hand
period and place this to the right of the given nvunber as the first figure
of the root. Subtract its square from the first left hand period and to
the remainder annex the second period for a dividend.
Place before this as a partial divisor, double the root figure just found.
Find how many times the dividend, exclusive of its right hand figure,
contains the divisor, and place the quotient as the second figure of the
root, and also at the right of the partial divisor.
Multiply the divisor thus completed, by the second root figure and
subtract the product from the dividend. To this remainder annex the
next period for a new dividend, and double the two root figures for a
new partial divisor. Proceed as before until all the periods have been
brought down.
Arithmetic
Example. — Extract the s^iuarc root of 7840.2752 +•
78'40-27'52/88.S4S3
64
168)1440
1344
1765)9627
882s
[7704)80252
70816
177085)943600
8S5425
1770903)5817500
5312709
To Extract the Square Root of a Fraction
Find the roots of the numerator and denominator separately; or
reduce to a decimal and take its root.
* /Q "^9 3 9,- /
Example.— \/^= —p^ = 7; "r r^ = 0.5625, V0.5625 = 0.75.
T lb V16 4 10
To Extract the Cube Root of a Number
Beginning; at the right, point off the number into periods of three
figures each. If there are decimals, begin at the decimal point, separate
the whole number to the left, and the decimal at the right into such
periods; find the greatest cube conLained in the left-hand period, and
write its root as the first figure of the root required.
Subtract the cube of the first root figure from the left-hand period,
and to the remainder annex the ne.\t period for a dividend. Then
multiply the square of the first figure of the root by 300 and use the prod-
uct as a trial divisor; write the quotient as the second root figure.
Complete the trial divisor by adding to it 30 times the product of the
first root figure by the second, and the square of the second; multiply
the com[ileted divisor by the second root figure and subtract the product
from the di\adend. To the remainder annex the next period and proceed
as before, to find the third figure of the root, i.e., square the first two
figures of the root and multiply by 300 for a trial divisor. To this add
30 times the product of the first two root figures by the third, and the
square of the third for the completed divisor, etc.
The cube root will always contain as many figures as there are periods
in the given number.
Percentage
Example. — Extract the cube root of 78, 402, 752
78'402'752/428.
64
4^ X 300 = 4800 14402
4 X 2 X 30 = 240
5044 10088
42^ X 300 = 529200 4314752
42 X 8 X 30 = 10080
82 = 64
539344 4314752
Alligation
Alligation is the process of determining the value of a mixture of
different substances, when the quantity and value of each substance
is known. *
Ride. — Take the sum of all the products of the quantity of each
substance by its respective price, and divide it by the total quantity;
the result is the value of one unit of the mixture.
Example. — What is the value per ton of a mixture containing 500 lbs.
of pig iron at $18.00 per ton, 275 lbs. at $16.50 and 800 lbs. of scrap at
$14.00?
500 X 18 = 9000
275 X 16.5 = 4537-5°
800 X 14 = 11200.00
1575 24737.50
= $15,706 per ton.
1575
Percentage
Per cent means so many parts of 100, and is expressed decimally
as three per cent .03, meaning yf q; one-fourth of one per cent .0025 =
2 5
lOCJOO-
Percentage covers the operations of finding the part of a given
number at a given rate per cent; as 6 per cent of 2750, 2750 X .06 =
165.00; of finding what per cent one number is of another as: WTiat
per cent of 780 is 39?
39 -^ 780 = .05 per cent;
of ascertaining a number when an amount is given, which is a given
per cent of that number; as 62.5 is .04 per cent of what number?
62.5 -H .04 = 1562.5.
Arithmclic
Dkcimal EguivALENTs OF Parts of One Inch
1-64
.015635
17-64
.365625
33-64
.515625
49-64
57662s
1-32
.O.^Ii^O
<)-32
.381250
17-32
.531250
25-32
781250
3-64
.' ■/ ^ ■ :
..,64
.29687s
35-64
.546875
51-<i4
796875
1-16
.' ' ,
■; 16
.313.S00
9-16
.562500
13-16
813500
s-64
,07M-'.S
ii-64
.328125
37-64
.578125
53-64
828135
3-33
. 09.17 >°
n-32
..343750
19-32
.593750
27-32
843750
7-U
. 109.173
2J 64
• 359.175
39-64
.609375
55-64
85937s
1-S
.liSooo
3-8
.375000
5-8
.625000
7-8
875000
9-64
. 140625
25-64
.390625
41-64
.64062s
57-^4
89062s
S-32
.156250
I.?-32
.406250
21-32
.656250
29-32
906350
11-64
.171875
27-64
.42187s
43-64
.671875
59-64
93187s
3-16
.187500
7-16
.437500
11-16
.687500
15-16
937SOO
13 64
.203125
29-64
4.53125
45-64
.703125
61-64
953125
7-32
.218750
15-32
.468750
23-32
.718750
31-32
968750
iS-64
.234375
31-64
.484375
47-64
.734375
63-64
98437s
1-4
.250000
I -a
.500000
3-4
.750000
I
I
:ncues to
Decimals
OF A
Foot
0
I
2
3
4
5
6
7
%
9
10
II
0833
.1667
.2500
.3333
.4167
5000
.5833
.6667
7500
8333
9167
A
.0026
.0859
.1693
.2526
3359
.4193
.5026
5859
■ 6693
7526
8359 .9193
i\>
0052
.0885
.1719
.2552
.3385
4219
.5052
.5885
.6719
7552
838s .9219
A
0078
.0911
1745
.2578
3411
.4245
.5078
59"
6745
.7578
8411 9245
i
0104
.0938
I77I
.2604
3138
.4271
.5104
5938
6771
7604
8438 .9271
A
.0130
.0964
• 1797
.2630
.3464
4297
.5130
.5964
6797
76.30
8464
9297
A
.0156
.0990
.1823
.2656
3490
.4323
.5156
5990
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Algebra
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SECTION II
ALGEBRA
In algebra quantities of every kind are denoted by letters of the
alphabet.
The first letters of the alphabet are used to denote known quantities,
and the last letters unknown quantities.
The sign + (plns) denotes that the quantity before which it is placed
is to be added to some other quantity. Thus: a + b denotes the sum
of a and b.
The sign — (minus) denotes that the quantity before which it is
placed is to be subtracted from some other quantity. Thus: a — b
denotes that b is to be subtracted from a.
When no sign is prefixed to a quantity, + is always understood.
Quantities are said to have like or unlike signs, according as their
signs are like or unlike.
8 AlReljra
A quantity which consists of one term is said to be simple; but if it
consists of several terms connected ljy the signs + or — , it is said to be
comjKJund. Thus: a or — b arc simple quantities; but — a — 6 is a
compound <|uaiility.
Addition of Like Quantities
Add together the tocliiLicnts uf ihc c|uanlilies having like signs, and
subtract the negative sum from the positive. Thus: Add 7 a + 2 a,
^a — a, and 60 — 40.
7 (i — a
2 a — 4 a
3a
6a
18a — 5 a = 13 o.
Addition of Unlike Quantities
If some of the quanlilics are unlike, proceed as before with each like
quantity, and write down the algebraic sum of all the quantities. Thus:
Add 70 + 26, 3 a — i, 66 — 4a and 50-46.
70-40 26— b
Sa — 66 — 46
150- 40 86 — 56
-40 - 5 6
11 a 36
Ans'd'cr = 11 o + 3 6.
The process is the same with compound quantities. Thus: Add
0-6 + 2 cd^ to - 2 a^b + c(P = 3cd"- - a^b.
Subtraction
Change the sign of the subtrahend and proceed as in addition. Thus:
Subtract 3 0-6 — 9 c from 40^6 + c; changing the signs of the subtra-
hend and adding, the expressions may be written
4 0^6 — 3 o''6 + f + 9 f or 0*6 -(- 10 c.
Multiplication
If the quantities to be multiplied have like signs, the sign of the
product is +; if they have unlike signs, that of the jiroduct is — .
Powers of Quantities 9
Of Simple Quantities
Multiply the coefficients together and prefix the + or — sign, accord-
ing as the signs of the quantities are like or unlike. Thus:
Multiply + ahy + b. Product equals -{- ab.
Multiply + 5 6 by — 4 c. Product equals — 20 be.
Multiply — 3 ax by + 7 a&- Product equals — 21 a'bx.
Of Compound Quantities
Multiply each term of the multiplicand by all the terms of the multi-
plier, one after the other as by former rule; collect their products into
one sum for the required product.
Example. —
Multiply a — b + c
by a -\- b — e
-a<r
- &2 + be
+ be -
-C2
Multiply
by
2x -\- y
X — 2 y
-V^^ 2be-
2 y
-C2
2 x"^ -\- xy
- 4xy -
2 x^ — 2, xy — 2 y^
Powers of Quantities
The products arising from the continued multiplication of the same
quantity by itself are called powers of that quantity; and the quantity
itself is called the root.
The product of two or more powers of any quantity is the quantity
with an exponent equal to the sum of the exponents of the powers.
Thus:
a^ X d^ = fl'; a^b X ab = aW; 4 a5 X — 3 ac = — 12 a%e.
The square of the sum of two quantities equals the sum of their
squares plus twice their product.
{a + &)2 = a2 + 52 4. 2 ab.
The square of the difference of two quantities is the sum of their
squares minus twice their product.
(a — 6)2 = a^ -f 6^ — 2 ab.
lo Algebra
The prmlutl of the sum an<l difTcrencc of two quaotilics is equal to
the difTcrencc o{ liieir squarcb.
(a f b) (a-b) =a^- I?.
The squares of half the sum of two quantities is equal lo their product
plus the scjuarc of half their difTcrencc.
Thus: (a + A)» , , (<j - 6)»
— — = u« i
2 2
The square of a trinomial is equal to the sum of the squares of each
term plus twice the product of each term by each of its following terms-
Thus: (a + 6 -f c)* = a* -f t^ + c' + 2 aft + 2 or + 2 6c.
(a — 6 — c)* = a' + 6* + c' — 2 a6 — 2 ac + 2 6c.
Parenthesis ( )
When a parenthesis is preceded by a plus sign, it may be removed
without changing the value of the expression.
Thus: {a-\-b) + {a-\-b) = 2a + 2h.
But if preceded by a minus sign, if removed, the signs of all the terms
within the parenthesis must be changed.
Thus: {a-\-b)-{a-b)=a-\-h-a + h = 2b.
When a parenthesis is within a parenthesis, remove the inner one -first.
Thus: a-\h-[c-{d- c)]] = a - [b - [c - d + e]] =
a — [b — c-\-d — c] = a — b-^c — d-\-c.
WTiere the sign of multiplication ( X ) appears, the operation indicated
by it must be performed before that of addition or subtraction.
Division
If the sign of the divisor and dividend be like, the sign of the quotient
is plus (+); but if they be unlike the sign of the quotient is minus ( — ).
To Divide a Monomial by a Monomial
Write the di\idcnd o\er the divisor with a line between them. If the
expressions have common factors remove them.
Thus: ,, , a-bx ax o' i ,
a^bx -J- aby = -7— = — ; -b = -; = <i~
aby y a" or
To Divide a Polynomial by a Monomial
Divide each term of the polynomial by the monomial.
Thus: (8a6 — i2ac) -r- 40 = 26 — 3c.
Simple Equations il
To Divide a Polynomial by a Polynomial
Arrange the terms of both dividend and divisor according to the as-
cending or descending powers of some letter, and keep this arrangement
throughout the operation. Divide the first term of the dividend by
the first term of the divisor, and write the result as the first term of the
quotient.
Multiply all the terms of the divisor by the first term of the quotient
and subtract the product from the dividend. If there is a remainder
consider it as a new dividend and proceed as before.
Thus: (o2 - b^) -^(a + b)
a + b)a^-bHa-b
a- -\- ab
-ab-b^
— ab — b^
(i) The difference between two equal powers of the same quantities
is divisible by their difference.
(2) The difference between two equal even powers of the same quan-
tities is divisible by their sum or difference.
(3) The sum of two equal even powers of the same quantities is not
divisible by their sum or difference.
(4) The sum of two equal odd powers of the same quantities is
divisible by their sum.
(5) The sum of two equal eveti powers, whose exponents are composed
of odd and even factors, is divisible by the sum of the powers of the
quantities expressed by the even factor.
Thus: (.1"® + y^) is divisible by (x^ + y^).
Simple Equations
An equation Is a statement of equality between two expressions; as
a + b = c + d.
A simple equation, or equation of the first degree, is one which contains
only the first power of the unknown quantity.
If both sides of the equation be changed equally, by addition, sub-
traction, multiplication or division, the equality will not be disturbed.
Any term of an equation may be changed from one side to the other
provided its sign be changed.
Thus: a + b = c + d, a = c + d — b.
1 7 AlKchra
To Solve an Equation Having One Unknown Quantity
TransiK>sc all the terms cuntaining the unknown quantity to unc side
'if the equation, and all llic other terms to the other side.
Combine like terms, and divide both sides by the coefficient of the
unknown quantity.
Thus: 8 X- — 29 = 26 — 3 X, 1 1 jr = 55, x = $.
Simple algebraic problems containing one unknown quantity, are
solved by makinj^ x equal the unknown quantity, and stating the con-
ditions of the problem in the form uf an algebraic equation, then solving
the equation.
Thus: What two numbers are those whose sum is 48 and difference 14?
Let X = the smaller number.
Then x -{- 14 = the greater number.
a; + X + 14 = 48,
2 X = 34.
Therefore x = 17,
and X -f 14 = 31,
31 + 17 = 48.
Find the number whose treble exceeds 50 by as much as its double
falls short of 40.
Let X = the number.
Then 3 x — 50 = 40 — 2 x,
5 X = 90, X = 18.
Equations Containing Two Unknown Quantities
If one equation contains two unknown quantities, an indefinite number
of pairs of values for them may be found, which will satisfy the equation;
but if a second equation be given, only one pair of values can be found
that will satisfy both equations. Simultaneous equations, or those
which may be satisfied by the same values of the unknown quantity,
are solved by combining the equations so as to obtain a single equation
containing only one unknown quantity.
This process is called elimination.
Elimination by Addition or Subtraction
Multiply the equations by such a number as will make the coefficients
of one of the unknown quantities equal in both. Add or subtract
according as they have like or unlike signs.
Elimination by Comparison 13
Solve 2 a; + 3 3* = 7
4X- sy = 3
Multiply by 2 4^ + 6 y = 14
Subtract 4-*-— 5y= 3
II y = II
y = I.
Substituting the value of y in the first equation
2 a; + 3 = 7, .: X = 2.
Elimination by Substitution
From one of the equations obtain the value of one of the unknown
quantities in terms of the other. Substitute this value of this unknown
quantity for it, in the other equation, and reduce the resulting equations.
Solve 2 re + 3 y = 8 (i)
3 A- + 7 y = 7 (2)
From (i) X = ^~^^
2
Substituting this value in (2)
(8 — 3 3')
3 1-7 3' = 7, 24-9y + I4y = 14, .•- y = — 2.
Substituting this value in (i);
2 a; — 6 = 8, .'. X = "/.
Elimination by Comparison
From each equation obtain the value of one of the unknown quantities,
in terms of the other. Form an equation from these equal values of the
same unknown quantity and reduce.
Solve 2 .T — 9 y = II (i)
Sx-4y= 7 (2)
From (I) X = '-1±^
2
From (2) X = ^±43:
3
Placing the values of a; in a new equation
11 + 93' 7 + 4y
2 3
Substituting this value of y in (i)
2x + g = II,
I9y=-I9, A y=-i.
1 4 AlKfl)ra
If three simultaneous equations are ^iven containinK three unknown
f|uantilics, one of the unicnown quantities must he eliminated between
two pairs of the ecjuations, then a second between the two resulting
efjualions.
Quadratic Equations or Equations of the Second Degree
A quadratic equation contains the square of the unknown quantity,
but no higher power. A i)urc quadratic contains the square only; an
adfected quadratic contains both the square and the first power.
To Solve a Pure Quadratic
Collect the unknown (|uantities on one side, and the known quantities
on the i)lher; divide by the coefl'icient of the unknown quantity and
extract the square root of each side of the resulting equation.
Solve 3r' — 15 = 0.
3A-= = i5. .-. X-' = 5, X = V5.
A root which is indicated, but can only be found approximately is
called a surd.
Solve 3 a;^ + 15 = o.
3 .v2 = - 15, .v= = - 5, :.x = \/- 5.
The square root of a negative quantity cannot be found even approxi-
mately, for the square of any number is positive; therefore, a root which
is indicated, but cannot be found approximately is called imaginary.
To Solve an Adfected Quadratic
First. — Carry all the terms invuhini^ the unknown (juantities to one
side of the equation and the known quantities to the other side. Arrange
the unknown quantities in the order of their exjxjnents, changing the
signs of the equation if necessary, so that the sign of the term containing
the square of the unknown quantity shall be positive.
Second. — Divide both terms by the coefficient of the square -of the
unknown quantit}'.
Third. — To complete the square.
Add to both sides of the equation, the square of half the coefficient
of the unknown quantity. The side containing the unknown quantity
will now be a perfect square.
Fourth. — Extract the square root of both sides of the equation and
solve the resulting simple equation.
Example. — x^ -\- 2 x = 35.
.Add the square of half the coefficient of .v, which is i, to both sides;
then A-* + 2 x + I = 35 + I = 36.
Plane Geometry 15
Extracting the square root
X + I = ^36 = ± 6
X = 6 - I = s
a;=— 6 — i = — 7.
• Example: 3 .t^ — 4 .r = 32.
Divide by the coeiEcieat of x-
x^-^ = ^.
3 3
Add the square of half the coefScient of x, which equals (,f)^ = |;
then .i;^-f^ + f = ¥ + !•
Extracting the square root, the equation becomes
1- _ 2 _ -v/100 _ 10
-'- 3 — ^ 9 3
a-— 3-1-3 — 4, or:^-— s^T^a— 3~2 3.
Since the square of a quantity has two roots ±, a quadratic equation
has apparently two solutions. Both solutions may be correct; but in
some cases one may be correct and the other inconsistent with the con-
ditions of the problem.
For the solution of quadratic equations containing two unknown
quantities, or for that of equations of a higher order, a more extended
treatment of the subject is required, than is permissible in a book of this
character.
SECTION III
PLANE GEOMETRY
Problem 1
To Bisect a Straight Line, or an Arc of a Circle
With any radius greater than half AB and with
A and B as centers, describe arcs cutting each other
at C and D. Draw the line CD, which will bisect ^'
the straight line at E and the arc at F.
Problem 2 Fig. i.
To Draw a Perpendicular to a Straight Line, or a Radial Line to the Arc
of a Circle
This is the same as Problem i, Fig. i.
CD is perpendicular to AB, or is radial to the arc.
i6
Plane (Icomctry
Problem 3
To Draw a Perpendicular to a Stritifilil Line, from a Given Point on that
Line
to
U
Fig. 2.
With any convenient radius and the given fxjint C,
as a center, cut the line AB, at A and B. Then
with a radius longer than AC, describe arcs from A
and B intersecting each other at D and E. Draw
DC, perpendicular to AB.
In laying out work on the ground or in places where the straight edge
and dividers are inapplicable:
Set off six feet from .1 to B. Then with .1 , as a cen-
ter and AC = 8' taken on a tape line, describe an arc at
C; with B, as a center and a radius BC = lo', cut the
other arc at C. A line through CA , will be perpendicu-
lar to AB. 3, 4 and s may be used instead of 6, 8 and
lo; or any multiples of 6, 8, lo will serve.
\L '^
Fig. 3.
Problem 4
From a Point at the End of a Given Line lo Draw a Perpendicular
From any point C, above the line, with the radius
AC, describe an arc, cutting the given line at B.
Draw BC, and prolong until it intersects the arc at D.
Then, DA will be perpendicular to .-IB, at .4.
Fig. 4.
Problem 5
From Any Point Without a Given Straight Line, to Draw a Perpendicular
to the Line
Let BC, be the given line; then from any point A,
with any radius AB, describe arcs cutting the line at
B and C. From B and C as centers and any radius
greater than half of BC. describe arcs intersecting at
D. Draw AD, perpendicular to BC. (Fig. 5.)
;:d
Fig. s.
Plane Geometry
17
Problem 6
To Draw a Straight Line Parallel to a Given Line at a Given Distance
from That Line
B D
From any two points on the given line as — -y "y^
centers and the given distance as a radius, I ;
■describe the arcs B and D. Draw BD parallel A. c
to AC. (Fig. 6.) Fig. 6.
Problem 7
To Divide a Given Straight Line into Any Nnnher of Equal Parts
Let AB he the given line. Draw any
— c line AC, intersecting the given line and lay
ofE on it, say, 5 equal parts. Join the last
point 5 with B. Then through each of the
Fig. 7. other divisions on AC, draw lines parallel to
B 5, dividing y4B into 5 equal parts. (Fig. 7.)
Problem 8
To Draw an Angle of 60°, also One of 30°
From A with any radius describe the arc CB, then
with the same radius and 5, as a center, cut the arc at
C. Then the angle CAB = 60°.
From C drop CD perpendicular io AB. The angle
ACD = 30°.
Problem 9
To Draw an Angle of 45°
Draw BC, perpendicular to AB. Make BC = AB,
and draw AC. The angle CAB = 45°. (Fig. 9.)
Fig. 8.
Fig. 9.
Problem 10
To Bisect an Angle
Let ABC be the given angle. With 5 as a center and
any radius, draw the arc AC. Then with A and C as
centers and a radius greater than one-half AC, describe
arcs cutting each other at D. Draw BD, which will
bisect the angle ABC. (Fig, 10.)
Fig. 10.
x8
Plane (icornctry
Problem 11
Through Two Given Points and W ilh a Given Radius Describe I he Arc
of a Circle
Referring to I'ig. lo. Let .1 and C be the given jKiinls and a distance
AB the given radius.
From ,1 and C, with AB as a radius describe arcs cutting each other
at B, then with B as a center strike AC.
All Angles in a semicircle are Kiglit Angles.
Problem 12
An Angle al the Center of a Circle is Twice the Angle at the Circumference
when Both Slatul on the same Arc
C Thus the angle BAC is equal to twice the angle
BDC. (Fig. II.)
Fig. II.
Problem 13
All the Angles Between an Arc and its Chord, the Sides of the Angle Pass-
ing Through the Extremities of t/ie Chord, are Equal. (Fig. 12.)
Thus, the angle EFG = FJIG.
Fig. 12.
Problem 14
To Find the Center of a Circle or of an Arc. (Fig. 13.)
Take an}' three convenient points on the circum-
ference, and with anj' radius greater than half the
distance between any two points, describe arcs cut-
ting each other at d, c, f and g. Through d, f and
e, g, draw the lines df and eg; the center is at their
Fig. 13. intersection H.
Problem 15
To Pass a Circle Through Three Given Points
Referring to Problem 14, let a, b and c be the three given points.
Proceed in the same way as to find the center H.
Plane Geometry
19
Problem 16
To Describe an Arc of a Circle Passing Through Three Given Poitils
when the Center is not Accessible. (Fig. 14.)
Let A , B and C be the three given points.
From A and B as centers and with AB a.s a, radius, describe the arcs
AE and BD.
Draw AD and BE through C. Lay ofi on
the arc AE, any number of equal parts
above E and on BD, the same number be-
low D, numbering the points i, 2, 3, etc., in
the order in which they are taken. Draw
from A, lines through i, 2, 3, etc., on the
arc BD; and from B, lines through i, 2, 3,
etc., on the arc AE. The intersections of
lines having corresponding numbers will be points on the required arc
between C and B.
Proceed in the same manner to find points between C and A. Then
draw the arc through the points.
Fig. 14.
Problem 17
From a Point on the Circumference of a Circle Draw a Tangent to
the Circle. (Fig. 15.)
Through the given point A draw the radial line
AC. Then on AC erect the perpendicular BE, as
in Problem 3.
Fig. is.
Problem 18
From a Point Without a Circle Draw a Tangent to the Circle. (Fig. 16.)
Let A be the center of the circle, and B the
given point. Join A and B, and on the line AB
describe a semicircle, with a radius equal to one-
half oi AB. Through the intersection of the
semicircle and the given circle draw the tangent
BC.
Fig. 16.
20 Plain- (icomclry
Problem 19
Through a Point on a Line, liiurling the Anglf Betwern Two Lines, Draw
a Circle Which Shall be Tangent to the Given Lines. (Fig. 17.)
Fig. 17.
Let A he the point on a line bisect-
ing the angle between BC and DE.
Through .1 draw CVipcrjjendicuIar to
AF. Bisect the angles at C and E.
The intersection G of the bisecting
lines will be on AF and at the center
of the required circle.
Problem 20
Describe an Arc, Tangent to Two Given Arcs and at a Given Point
on one of the Arcs. (Fig. 18.)
Let A and B be the centers of the given arcs
and C the point of tangency on the arc, whose
center is B. Join A and B and draw BC through
the given point. Make CE equal to the radius
AD.
Bisect AE, draw a perpendicular at its middle
point and prolong to intersection with BC at F,
which is the center of the arc required.
Fig. 18.
Problem 21
To Construct a Pentagon having a Given Side AB. (Fig. 19.)
At B erect a perpendicular BC, equal to one-half AB. Draw AC and
make CD equal BC. Then BD is the radius of the
circle circumscribing a pentagon having sides equal
to AB.
The radius of a given circle is the side of an in-
scribed he.xagon.
The radius of a circle circumscribing a hexagon,
is equal to the distance from the center of the hexa-
gon to the e.xtremity of one of its sides.
Fig. 19.
Plane Geometry
21
Problem 22
To Construct an Ellipse ■when the Transverse attd Conjugate Axes
are Given. (Fig. 20.)
Draw the axes AB and CD intersecting at G. From C, with one-
half ^jB as a radius, cut .45 at £ and F. Divide GB into any number
of parts as at i, 2, 3, 4, 5.
With £ as a center and 4 i as a
radius, and with F as a center and
radius B i, strike arcs cutting each
other at i, i, above and below the
transverse axis.
Again with E and F as centers
and A 2 and B 2, respectively as
radii, describe arcs cutting each
other at 2, 2. Find as many points as desired in the same way in both
halves of the ellipse, then trace the curve.
This construction depends on the property of an ellipse; that the sum
of the distances from the foci to any point on the ellipse is equal to the
transverse axis.
Problem 23
To Describe an Ellipse Mechanically when the Transverse and Con-
jugate Axes are Known. (Fig. 21.)
Draw the axes and determine the foci as in Problem 22. Drive two
pins at the foci E and F. Fasten to each of the pins one end of a cord
whose length is equal to that of the
transverse axis.
Then with a pencil, so placed
within the loop of the cord as
always to keep it taut and uniformly
strained, trace one-half of the curve,
from one extremity of the trans-
verse axis to the other. The other
half of the curve is traced by chang-
ing the cord and pencil to the oppo-
site side of the transverse axis. This
method is seldom satisfactory on
account of the unequal stretching
of the cord.
A better mechanical method of describing an ellipse is to place a
straight edge along and above the transverse axis and another along and
1°
0 0" 1
A
B C
Fig. 21.
22 I'laiii- (icomelry
al one side of the ronjunate axis, as at AB and CD (Fig. 21), leaving a
slight o|)cning belwctn llic end of the straightedge CZ^and the transverse
axis.
There must also Lc a tliin strip of wood with a hole for pencil |>oint al
A and small pins at B and C; AB being equal to one-half of the conju-
gate axis; and AC equal to one-half the transverse axis. By moving
this strip so that the pin B is always in contact with AB and the pin C
in like contact with CD the upper half of the ellipse may be de-
scribed.
The straight edges are placed in corresponding positions on the
opposite side of the transverse axis to describe the other half of the
ellipse.
Except where extreme accuracy is required, it is more convenient to
approximate the ellipse with circular arcs.
Thus: Lay off AB and CD (Fig. 22)
equal to the transverse and conjugate axes
respectively. Make Oa and Oc equal to
the difference between the semi-transverse
and semi-conjugate axes, and ad equal to
one-half ac. Set off Oe equal to Od. Draw
di parallel to ac; join e and / and draw the
parallel lines dm and em. From m, with a
radius mC, strike an arc cutting jnd and me. From i, with iD as a
radius, strike an arc cutting id and ie. Then from d and e, with radius
Ad, strike arcs closing the figure.
The Parabola
A parabola is a curve every point of which is equidistant from a line
called the directrix and from a point on its axis called the focus. The
directrix is a line perpendicular to the axis and at the same distance as
the focus from the apex of the curve.
.'\ line perpendicular to the axis, drawn through the focus to the cur\e,
is called the parameter.
If a line be drawn from any point of the curve, perpendicular to the
axis, the distance from the apex to the intersection of the perpendicular
with the axis is called the abscissa of that point and the distance from
the intersection at the axis to the curve is called the ordinate of that
point.
Abscissae of a parabola are as the squares of corresponding ordi-
nates.
The Hyperbola
23
Problem 24
To Construct a Parabola -when the Focus and Directrix
are Given. (Fig. 23.)
Let AB he the directrix, and C the
focus of a parabola. Bisect CD at E, which
point is the apex of the curve.
Then with C as a center and any radii,
as C I, C 2, etc., strike arcs at i, 2 and 3,
etc. From D as a center and with the
radii equal to C i, C 2, C 3, etc., cut the
a.xis at i', 2', 3', etc. Through these points
draw hnes parallel to AB.
The intersection of corresponding parallels and arcs are points on the
required curve.
Problem 25
To Construct a Parabola when an Abscissa and Its Corre-
sponding Ordinate are Given. (Fig. 24.)
Fig. 23.
Fig. 24.
Let BA be the given abscissa and AD
the ordinate.
Bisect AD at E. Draw EB, and EF
perpendicular to EB. Set off BG and BK,
each equal to AF. Then will G be the
focus and LM (through K) perpendicular
to ^B, the directrix. Construct the curve
as in Problem 24.
The Hyperbola
An hyperbola is a cur\'e, such that the difference of the distances from
any point of it to two fixed points is always equal to a given distance.
The two fixed points are called the foci and the given distance is the
transverse axis. The conjugate axis is a line perpendicular to the trans-
verse axis at its middle point; and its length is equal to the side of a
rectangle, of which the transverse axis is the other side and the distance
between the foci, the diagonal.
Problem 26
To Construct an Hyperbola when the Foci and Transverse Axis are Given
Let A and B be the foci and EF the transverse axis. From A set oflf
AG equal to EF. Then, from .4 as a center and with any distance
greater than AF as a radius, strike an arc CD, cutting the transverse
24
Plane CJcomelry
axis (pri)IonKC<l) at //. From ^ as a center and flG as a radius, describe
arcs cutting the arc CD at C and D. C and D will l>e jxjints on the curve;
in like manner any number of (joints arc determined, Uirough which the
curve may be traced.
Proceeding in the same way on the opposite side
of the conjugate axis, the other branch of the curve
is constructed.
The diagonals of a rectangle constructed on the
transverse and conjugate axes are called the
asymptotes and are hnes to which the cur\'e is
tangent at an infinite distance. When the asymp-
totes are at right angles the cur\e is called an equi-
lateral hjTJerbola.
It is a property of the equilateral hyperbola, that if the asymptotes
be taken as the co-ordinate axes the product of the abscissa and ordinate
of an}- point of the curve is equal to the corresponding product of the
co-ordinates at any other point; or that the diagonal of a rectangle con-
structed by the ordinate and abscissa of any point of the curve passes
tlirough the intersection of the axes.
Fig. 25.
Problem 27
Given the Asymptotes and any Point on lite Curve, to Construct
the Curve. (Fig. 26.)
Let AB and AG he. the asymptotes and D the given
point. Multiply AB by AE and divide the product
AB X AE
by any other distance AF; then AG = ' ye '
and the intersection at / of lines through F and G,
parallel to the axes, is another point on the cur\'e.
/
Fig. 26.
Properties of Plane Figures
(i) In a right angle triangle, the square of the hypothenuse is equal
to the sum of the squares of the other two sides.
(2) In an equilateral triangle all the angles are equal.
(3) In an isosceles triangle a line drawn from the vertex perpendicular
to the base bisects the base and also the angle at the vertex.
(4) An exterior angle of a triangle equals the sum of the two opposite
angles.
(s) Similar triangles have equal angles and the sides opposite to
corresponding angles are proportional.
Properties of Plane Figures 25
(6) In any polygon, the sum of all the interior angles is equal to twice
as many right angles as the figure has sides, less four right angles.
(7) In any polygon the sum of all the exterior angles is equal to four
right angles, or 360°.
(S) The diagonals of any regular polygon intersect at the center
of the figure.
(9) A circle may be passed through any three points, not on the same
straight line.
(10) In the same circle, arcs are proportional to the angles at the
center.
(11) Any two arcs having the same angle at the center are propor-
tional to their radii.
(12) Areas of circles are proportional to the squares of their diameters
or the squares of the radii.
(13) A radius perpendicular to the chord of an arc bisects the arc
and its chord.
(14) A straight line tangent to a circle is perpendicular to the radius
at the point of tangency.
(15) An angle at the center of the circle is equal to twice the angle
at the circumference subtended by the same arc.
(16) Angles at the circumference of a circle, standing on the same
arc, are equal.
(17) Any triangle inscribed in a semicircle is a right angled tri-
angle.
(18) In any triangle inscribed in a segment of a circle, the angles at
the circumference are equal.
(19) Parallel chords or a chord and a parallel tangent intercept
equal arcs.
(20) If two chords of a circle intersect, the rectangles made by the
segments of the respective chords are equal.
(21) If one of the chords is a diameter of the circle and the other is
perpendicular to it, then one-half of the chord is a mean proportional
between the segments of the diameter.
(22) In any circle, with the center as the origin of co-ordinates, the
sum of the squares of the abscissa and ordinate of any point is equal to
the square of the radius, or x^ + y^ = I^-
(23) In any ellipse with same origin, the square of the abscissa of any
point multiplied by the square of the semi-conjugate axis plus the square
of the ordinate of same point multiplied by the square of the semi-
transverse a.xis is .equal to the square of the product of the semi-axes.
Thus: 5lv^ 4- A'^'f = A^B'^, where A and B are the semi- transverse
and semi-conjugate axes.
26
Mensuration
(j4) In an ellipse, lines drawn from any j)<)inl to the foci make equal
angles with a LanKcnt at that [Kjint.
(25) The sum of the distances from any f)»jint <jf an ellipse to the foci
is equal to the transverse axis.
(26) If from any point of a parabola a line be drawn to the focus, and
one |)arallcl to the axis, they will make equal angles with the tangent at
that point.
(27) The apex of a parabola bisects the distance on the axis from the
focus to the directrix.
(2S) The angle Ijctween two tangents to a parabola is equal to half
the angle at the focus, subtended by the chord joining the points of
tangency.
(29) The area included between any chord of a parabola and the cur\'e
is equal to two-thirds that of the triangle formed by the chord and
tangents through its extremities.
(30) The difTerence between the focal distances of any point of an
hyperbola is equal to the transverse axis.
(31) The product of the perpendiculars from the foci to any tangent
of an hyperbola is constant.
(32) .\ tangent at any point of an hyperbola makes equal angles with
the focal distances of the point.
SECTION IV
MENSURATION
PL.Wl-: .SUklACKS
Triangles
The area of any triangle is equal to half the
base multiplied by the altitude. (Fig. ^7.)
Area = ^^ X CD.
To solve a triangle, three sides, two angles
and one side or two sides and one angle must
be given.
The area of a parallelogram is equal to the
base multiplied by the perpendicular distance
between the sides = AB X CD. (Fig. 28.)
Fig. 28.
Triangles
27
The area of a trapezoid is equal to half the
sum of the parallel sides multiplied by the per-
pendicular distance between them. (Fig. 29.)
Area =
AB + CD
X CE.
Fig. 29.
is equal
The area of a trapezium is equal to the
diagonal multiphed by half the sum of the
perpendiculars dropped to it from the vertices
of the opposite angles. (Fig. 30.)
^„ AE + DF
Area = CB X
The area of any quadrilateral is found
by multiplying the diagonal by one-half the
sum of the perpendiculars dropped from the
vertices of the opposite angles. (Fig. 31.)
DE + BF
Area = AC X
Fig. 31.
If the diagonal falls without the figure, the
area is equal to the product of the diagonal
by half the difference of the perpendiculars.
(Fig. 32.)
Area =ABCD = AC X ^^ ~ ^^ .
A polygon is a plane figure bounded by three or more straight lines;
it is regular or irregular according as the lines bounding it are equal or
unequal.
If straight lines be drawn from the center of a regular polygon to each
of the vertices of the interior angles, the polygon will be divided into as
many isosceles triangles as it has sides. Each triangle will have for its
base one of the sides of the polygon and for its altitude the perpendicular
distance from the center of the polygon to that side. The area of the
polygon is equal to the sum of the areas of all the triangles, and is
found by multiplying one-half the sum of all the
sides of the polygon by the perpendicular distance
from the center to one of its sides.
To find the area of an irregular polygon, divide
the polygon into triangles and take the sum of
their areas.
!S^D
I !5t56789IO
Fig. 33.
To Find the Area of Any Irregular Plane Figure
Let C D E F G he any irregular figure. Draw any straight line AB
as a base; through the extremities of the figure drop perpendiculars
a3 Mensuration
CA and Fli to the base. Divifle AB into any number of equal parts,
say ID. 'I'hrough llic middle points of each of the equal divisions draw
|)cr|)cndiculars cutting the [boundaries of the figure on opposite sides.
Take the sum of the lengths of all these lines within the figure and divide
such sum by the number of divisions; the quotient is the mean width of
the figure which nuilliplied by its length AB gives the area.
Thus: ab + cd -\- cf etc. = //; then ~ X AB ecjuals the area of
CDEFG.
The Circle
The ratio of the circumference of a circle to its diameter is equal to
3.14159. This is represented by the Greek letter t, pronounced Pi.
Let C = the circumference of any circle.
D = the diameter of any circle,
r = the radius of any circle.
A = area of any circle.
The areas of circles are as the squares of their diameters, or as the
squares of their radii.
C = wD = 3.14159 X D.
C = 2Trr = 6.28318 X r.
A = Trr- = 3.14159 X r^
A = InET- = 0.7854 X Zr-.
CP
A = — = 0.07958 X (?.
47r
A = 0.7854 X 4 r^
A =^ = —
~ 2 4 *
Z? = - = 0.3183 X C.
2 \'— = i.i:
84V/I,
r = — = 0.5642 Va.
2 TV
The Ellipse
29
The Ellipse
The ellipse is a curve formed by the intersection of a plane inclined
to the axis of a cone or cylinder, where the plane does not cut the base.
To Find the Length of any Ordinate, HK or LM, Knowing the Two
Diameters AB and CD, and the Abscisses OK and OM
HK
AB' : CD^ :: AK X KB : HK\
^ J CD' X (AKX KB)
AB^
CD
AB
VaK X KB,
The circumference of an ellipse is found from the formula below,
wherein D = transverse diameter and d = conjugate diameter. C =
d{D - d)
d)-
circumference = 2,-T-A'iS d -\- 2 {D
V 2 8.8
V{D + d)x{D + 2d)
C = 3.1415
These formulas apply where large D is not more than five times as
long as d.
The area of an ellipse is equal to that of an annular ring of which the
siun and difference of the radii of the limiting circles are respectively
equal to the semi-axes of the ellipse.
Thus TT (f2 — r'^) ==Tr{r + r') X {r — r') ; then if (r + r') equals the semi-
transverse axis equals A, and (r — r') equals the semi-conjugate axis
equals S, the area of the ellipse equals tt {AB) or w into the product of
the semi-axes or into the product of the axes, divided by four.
30 Men Ml rat ion
SOLIDS
The Priam
A prism is a solid whose bases or ends arc similar, equal and parallel
polyj^ons and wiiose sides arc parallelograms. The prism is right or
ohli(iuc according as the sides are jK-Tpemlicular to or inclined to the ends;
regular or irregular, as the ends are regular or irregular polygons.
The surface of any prism is the sum of the areas of the sides added to
that of the ends.
To find the surface of a right i)rism, multiply the i>erimeler of its base
liy its altitude; to this i)roduct add the areas of the ends.
The volume of any prism is ecjual to the area of its base multiplied
by its altitude, or perpendicular distance between the ends.
The volume of any fruslum of a prism is equal to the product of the
sum of all the edges (divided by their number;, and the area of the cross
section perpendicular to those edges.
The Pyramid
A pyTamid is a solid having any jjolNgun for its base; and for its sides
triangles, terminating at one point called the apex
The a.xis of a pyramid is a straight line from the ape.x to the center of
gravity of its base.
A pyramid is right or oblique according as the a.xis is perpendicular
or inclined to the base; regular or irregular, as the base is a regular or
irregular figure.
The slant height is the distance from the vertex of any of the tri-
angular sides to the middle point of its base.
The surface of any pjTamid is equal to the sum of the areas of all the
triangles of which it is composed plus the area of the base.
The surface of a right regular pyramid is equal to the perimeter of its
base multiplied by half the slant height plus the area of the base.
The volume of any pyramid is equal to the area of the base multiplictl
by one-third of the altitude; or the perpendicular distance from the apex
to the base. It is also equal to one-third the volume of a cylinder having
the same base and altitude; or to one-half the volume of a hemisphere
having the same base and altitude.
The volumes of a pyramid, hemisphere and cylinder, having the same
base and altitude are to each other as i, 2 and 3.
Frustrum of a Pjrramid
The frustrum of a pyramid is the section between two i)lanes which
may or may not be parallel.
Polyhedra 31
The slant height of any side of a frustrum of a pyramid is measured
from the middle points of the top and bottom sides of the trapezium
forming that side.
To find the surface of any frustrum of apyramid, take the sum of the
areas of all the trapeziums forming the sides, to which add the sum of
the top and base.
The surface of a frustrum of a right regular pyramid, where the top
and base are parallel planes, is equal to one-half the sum of the perimeters
of top and base multiplied by the slant height plus the sum of the areas
of the top and base.
The volume of any frustrum of any pyramid, with top and base
parallel, is equal to one-third the perpendicular distance between top
and base multiplied by the sums of the areas of top and base, and the
square root of the product of those areas.
Thus H, being the perpendicular and A and A' the areas of top and
base, respectively, then the volume equals \ H X {A -\- A' -\- ^ A X A')
or A" being equal to the area of a section midway between and parallel
to base and top, the volume = V = I H {A +A' + 4A").
A prismoid is a solid having six sides, two of which are parallel but
unequal' quadrangles, and the other sides trapeziums.
To find the Volume of a Prismoid
Let A = area of one of the parallel sides.
a — area of the other parallel side.
M = area of cross section midway between and parallel to
the parallel sides.
L = perpendicular distance between the two parallel sides.
Then Volume^ £X ^4 + « + 4^/j.
The Wedge
The wedge is a frustrum of a triangular prism. Its volume is equal
to the area of a right section multiplied by one-third the sum of the
lengths of the three parallel edges.
Let A equal area of section perpendicular to the axis of the prism and
BC, DE and FG, the lengths of the parallel edges respectively.
Then Volume of wedge = A •
3
Polyhedra
A polyhedron is a solid bounded by plane surfaces.
A regular polyhedron is one whose bounding faces are all equal and
regular polygons.
32
Mcii.suratiun
There are five regular polyhcdra as follows:
Name
Bounded by
Surface
" sum of sur-
faces of all the
faces
= square of
the length of
one edg«; by
\'olume
• tof
Kth
,,. by
Tetrahedron
Cube or hexahedron
Octahedron
Dodecahedron
4 Equilateral trianRlcs.. .
6 squares
8 EquiLiteral trianRles..
12 Equilateral pentagons.
20 Equilateral triangles. .
1.7320
6.000
3 4641
20.6458
8.6602
.1178
1.000
.4714
7.6631
2.1817
The Cylinder
A cylinder may be delincd as u pri.-^m, oi which a section perpendicular
to its axis is a circle. It may be right or oblique.
The base of a right cylinder is a circle, that of an oblique cylinder an
ellipse.
The surface of any cylinder is ccjual to the product of the circumference
of a circle whose plane is perpendicular to the axis of the cylinder, by
the length of the axis, plus the area of the ends.
The volume of a cylinder is equal to the area of a circle perpendicular
to the axis multiplied by its altitude.
The Cone
A cone is a pyramid having an infinite number of sides.
Cones are right or oblique according as their axes are perpendicular
or inclined to their bases.
The surface of a right cone is equal to the product of the perimeter
of the base by half the slant height, plus the area of the base.
The surface of an oblique cone, cut from a right cone having a circular
base, is equal to the area of the base, multiplied by the altitude and
divided by the perpendicular distance from the axis at the point where
it pierces the base, to the surface of the cone, plus the area of the base;
AH
or the curv^ed surface of the cone equals -^ • Wherein A is the area
K
of the base, II the altitude and R the perpendicular.
The volume of any cone is equal to the area of the base multiplied by
one-third of the altitude.
The volume of a cone is equal to one-third that of a cylinder, or one-
half that of an hemisphere having same base and altitude.
The Sphere 33
The surface of a right circular frustrum of a cone with top and base
parallel is found by adding together the circumferences of top and base,
multiplying this sum by one-half the slant height; to this product add
the area of top and base to get the total surface.
The volume of a frustrum of any cone, with top and base parallel, is
equal to one-third of the altitude multiplied by the sum of the areas of
top and base plus the square root of the product of those areas, or equals
I the altitude
X (area of top -\- area of base + v area of top X area of base).
The Sphere
A sphere is a solid generated by revolving a semicircle about its
diameter.
The intersection of a sphere with any plane is a circle.
A circle cut by the intersection of the surface of a sphere and a plane
passing through its center is a great circle.
The volume of a sphere is greater than that of any other solid having
an equal-surface.
The surface of a sphere equals that of four great circles.
Surface = ^wr"^.
= ttDK
" = curved surface of a circumscribing cylinder.
" = area of a circle having twice the diameter of the sphere.
The surface of a sphere is equal to that of a circumscribing cube
multiplied by 0.5236.
Surfaces of spheres are to each other as the squares of their diameters.
Volume of a Sphere
Volume = ^irr^ = 4.1888 r''
" = lirD' = 0.5236 D^
" =1 volume of circumscribing cylinder.
" = 0.5236 volume of circumscribing cube.
Volumes of spheres are to each other as the cubes of their diameters.
Radius of a sphere = 0.62035 v volume.
Circumference of sphere = v 59.2176 volume.
= V3.1416 X area of surface.
_ Area of surface
Diameter
34 Mfiisiiniiion
I'hf urea of the rurvwl surface c)f a spherical segment is Cfjual to the
l>r<Kluct of the circumference of a ureal lirclc !)>' the height of the scg-
minl = rrDII , where I) is the diameter of the sjjhere and // the height
of the spherical segment.
The curved surface of a segment of a sphere is to the whole surface
of the sjjhere as the height of the segment is to the diameter of the
s|)heru.
To Find the Volume of a Spherical Segment
Let R = radius of base of segment.
// = height.
Then volume of segment = ^ nil (3 /?^ + //').
To tind the curved surface of a spherical zone, multiply the circum-
ference of the sphere by the height of the zone.
To find the volume of a spherical zone, let A and A' be the radii of
tlic ends of the zone and // be the height and V the volume.
Then K = i t// (jC-F + -'1=') + IP).
Guldin's Theorems
(i) If any plane curve be revolved about any external a.xis situated
in its plane, the surface generated is equal to the product of the perimeter
of the curs'c and the length of the path described by the center of gravity
of that perimeter.
(2) If any plane surface be revolved about any e.\ternal axis situated
in its plane, the volume generated is equal to the area of the revolving
surface multiplied by the path described by its center of gravity.
CHAPTER II
WEIGHTS AND MEASURES
In the United States and Great Britain measures of length and weight
are, for the same denomination, essentially equal; but liquid and dry
measures for same denomination differ widely. The standard measure
of length for both countries is that of the simple seconds pendulum,
at the sea level, in the latitude of Greenwich; in vacuum and at a tem-
perature of 62° F.
The length of such a pendulum is 39.1393 inches; 36 of these inches
constitute the standard British Imperial yard. This is also the stand-
ard in the United States.
The Troy pound at the U. S. Mint of Philadelphia is the legal standard
of weight in the United States.
It contains 5760 grains and is exactly the same as the Imperial Troy
pound of Great Britain.
The avoirdupois pound (commercial) of the United States contains
7000 grains, and agrees with the British avoirdupois pound within o.ooi
of a grain.
The metric system was legalized by the United States in 1866 but its
use is not obligatory.
The metre is the unit of the metric system of lengths and was supposed
to be one ten millionth, , of that portion of a meridian between
10,000,000
either pole and the equator.
The metric measures of surface and volume are the squares and cubes
of the metre, and of its decimal fractions and multiples.
The metric unit of weight is the gramme or grain, which is the weight
of a cubic centimeter of pure water at a temperature of 40° F.
The legal equivalent of the metre as established by Act of Congress
is 39.37 inches = 3.28083 ft. = 1.093611 yards.
The legal equivalent of the gramme is 15.432 grains.
The systems of weights used for commercial purposes in the United
States are as follows:
35
36 Weights aiul Mcxisurcs
Troy Weight
For Gold, Silver, Plalimim and Jewels, except Diamonds and Pearls
24 grains = i (x-nnyweight (dwt.).
20 pennyweights = i ounce = 480 grains.
12 ounces = i pound = 5760 grains.
Apothecaries Weight
{For I'nscriplions only.)
20 grains = i scruple O)
3 scruples = i drachm (3) = 60 grains.
8 drachms = i ounce (5) = 480 "
12 ounces = i pound (lb) = 5760 "
Avoirdupois Weight
For all Malcrials except those above named
16 drachms or 437.5 grains = i ounce (oz.).
16 ounces = i pound (lb.) = 7000 grains.
28 pounds = I quarter (qr.).
4 quarters =. i hundredweight (cwt.) =
112 lbs.
20 hundredweight = i long or gross ton = 2240 lb.
2000 pounds = I short or net ton.
2204.6 pounds = I metric ton.
I stone = 14 pounds.
I quintal = 100 pounds.
The weight of the grain is the same for all systems of weights.
A troy ounce = i .097 avoirdupois ounces.
An avoirdupois ounce = .91146 troy or apoth. ounce.
A troy pound = .822S6 avoirdupois pound.
An avoirdupois pound = i . 21528 troy or apoth. pounds.
The standard avoirdupois pound is equal to the weight of 27.7015 cu.
in. distilled water at 39.2° F., at sea level and at the latitude of Green-
wich.
Long Measure
12 inches = i foot = .3047973 metre.
3 feet = I yard = 36 in. = .9143919 metre.
S§ yards = i rod, pole, perch = i6i feet — 198 in.
40 rods = I furlong = 220 yards = 660 ft.
8 furlongs = i statute mile = 320 rods = 1760 yds. = 5280 ft.
3 miles = I league = 24 furlongs = 960 rods = 5 280 yds.
Square Measure 37
Land Measure
7.92 inches = i Knk; 100 links (66 ft.) = i chain = 4 rods.
10 chains = i furlong; 8 furlongs (80 chains) = i mile.
10 square chains = i acre.
Measures occasionally used
y^5 inch = I point; 6 points-x\ in. = i line.
1000 mils = I inch; 3 in. = i palm; 4 in. = i hand; 9 in. = i span.
2 yards = i fathom = 6 feet; 120 fathoms = i cable length.
A geographical (nautical) mile or knot = 6087.15 ft. = 1855.345
metres = 1.15287 statute miles.
I knot = I minute of longitude or latitude at the equator.
1° latitude at the equator = 68. 70 statute miles.
1° " " latitude 20° =68.78
1° " " " 40° =69.00 "
1° " " " 60° =69.23 "
1° " " " 90° =69.41 " "
Square Measure
144 square inches = i square foot.
9 " feet =1 " yard.
2,o\ " yards =1 " rod, perch or pole = 272^ sq. ft.
40 " rods = I rood = 1210 sq. yds. = 108,908 sq. ft.
4 roods (10 sq. chains) = i acre = 160 sq. rods = 4840 sq. yds =
43,560 sq. ft.
640 acres = i sq. mile = i section.
An acre = a square whose side is 208.71 ft.
A half acre = a square whose side is 147.581 ft.
A quarter acre = a square whose side is 104.355 ^t.
A circular inch is the area of a circle i inch in diameter and = .7854
sq. inches.
I square inch = 1.2732 circular inches.
A circular mil is the area of a circle i mil or .001 in. in diameter.
looo^ mils or 1,000,000 circular mils = i circular inch.
I square inch = 1,273,239 circular mils.
A cylinder, i inch in diameter and i foot high, contains:
1 .3056 U. S. gills.
.2805 U. S. dry pints.
.3246 U. S. liquid pints.
A cylinder, one foot in diameter and i foot high, contains:
1357. 1712 cubic inches. i-8§.oo64 U. S. liquid gills.
.7854 " feet. 47.0016 U.S. " pints.
.02909 " yards. 23.5008 U.S. " quarts.
38
\\ eights and Measures
5.8752 U. S. liquid gallons.
40.3916 U. S. dry pints.
20.1958 U.S. " quarts.
2.5254 U. S. dr)' pecks.
0.63112 U.S. " bushels.
Liquid Measure
[United Stdtrs only)
4 frills = I pint = 28.875 cubic inches.
2 pints = I quart = 57.75 cu. ins. = 8 gills.
4 quarts = 1 gallon = 231 cu. in. = 8 pts. = 32 gills.
T,\\ gallons = I barrel = 126 quarts = 4. 2 11 cu. ft.
63 gallons = 1 hogshead.
2 hogsheads = i pipe or liull.
2 pipes = I tun.
A puncheon contains 84 gallons.
A tierce contains 42 gallons.
A cube 1. 61 5 ft. on edge contains 3.384 U. S. struck bushels; or 31 J
gallons = 1 bbl.; or 4. 211 cu. ft.
Approximate
measure
Diameter
Height
iMiatc
;re
Diameter
Height
I Gill
J Pint
I Pint
I Quart
Inches
1.75
2.25
3.50
3.50
Inches
3
3S
3
6
1 Gallon
2 Gallons
8 Gallons
10 Gallons
Inches
7
7
14
14
Inches
6
12
12
IS
The basis of this measure is the old British wine gallon of 231 cubic
inches; or 8.3388 lbs. of distilled water at 39° F. and 30" barometer.
A cubic foot contains 7.48 gallons.
Apothecaries' or Wine Measure
Measure
Symbol
Pints
Fluid
ounces
Fluid
drachms
Minims
Cubic
inches
Weight of water
Ounces
Grains
I Minim
I fluid drachm.
I fluid ounce. . .
I pint
I gallon
m
0
Cong.
I
8
I
16
138
I
8
128
1034
I
60
480
7680
61440
0.0038
0.2356
1.8047
28.87s
231
I 043
Pounds
avoir.
1.043
8.345
0-95
57.05
456.4
7301.9
S84IS
British Imperial Liquid and Dry Measures
39
Dry Measure
{United Stales only)
2 pints = I quart = 67.2006 cubic inches = 1. 16365 liquid quarts.
4 quarts = i gallon = 8 pints = 268.80 cubic inches = 1. 16365 liq. gal.
2 gallons = I peck = i6 pints = 8 qts. = 537.60 cu. inches.
4 pecks = I struck bu. = 64 pints = 32 qts. = 8 gallons =21 50.42 cu. in.
The old Winchester struck bushel containing 2150.42 cubic inches or
77.627 pounds, avoirdupois, of distilled water at its maximum density
is the basis of this table.
Its legal dimensions are those of a cylinder i8| inches in diameter and
8 inches deep. When heaped, the cone must not be less than 6 inches
high; (the bushel) containing 1.5555 cubic feet and equal to ij struck
bushels.
Miscellaneous Measures
12 pieces = i dozen. 20 pieces = i score.
12 dozen = i gross. 24 sheets = i quire.
T 2 gross = I great gross. 20 quires = i ream.
2 pieces = i pair.
Weights of Given Volumes of Distilled Water at 70° F.
United States Liquid Measure
I gill = . 26005 lt)S.
I pint = 1 . 1402 "
I quart = 2 . 0804 "
I gallon = 8 lbs. 55 oz. = 8.345 lbs.
I barrel = 315 gals. = 262. 1310 lbs.
United States Dry Measure
I pint = I. 2104 lbs.
I quart = 2 . 4208 "
I gallon = 9.6834 "
I peck = 19.3668 "
I bushel (struck) = 77.4670 "
British Imperial Liquid and Dry Measures
Liquid and Dry Measures
31214 lbs. avoir, of distilled water.
24858
I gill
I pint
I quart
I gallon
I peck
= 9
= 19
I bushel = 79
4971S
9772
40
Weights and Measures
This system su|>crse<lcs the uld ones throughout flreat Britain, and
is based on the Imperial gallon of 277.274 cubic inches, ecjual to 10 {X)unds
avoirduiX)is of pure water at 62° I'., 30 in. Har.
Metric Measures
I litre = 2. 1981 lbs. avoir, of pure water.
1 centilitre = .02198 " " " " " = 153,866 gr.
1 decilitre = .2198 " " " " " = 3.516902.
I decalitre = 21.9808 " " " "
I metre or sterc = 2198.0786 " " " " "
Metric Measures of Length in U. S. Standard
Inches
Feet
Yards
Miles
Millimetre*..
Centimetref.
Decimetre —
Metret
Decametre i
Hectometre I
Kilometre f
Myriametre J
.039370
.393704
3 93704
39 3704
393 704
Road
measures
.003281
.032809
.328087
3 28087
32.80869
328 0869
3280.869
32808.69
. 1093623
1.093623
10.93623
109.3623
1093.623
10936.23
■062137s
.6213750
6.213750
• About A of an inch.
t About i of an inch.
t About 3 feet 3g inches.
Metric Square Measure by U. S. Standard
Measures Square inches Square feet 1 Square yards Acres
Square millimetre... . .001550 .00001076
Square centimetre.... .1,^5003 .00107641]
Square decimetre 1 5 5003 .10764101
Square meter or cen
tare 1550.03 10.764101
Square decametre or
aire '1SS003 1076. 4101
Square decare* 10764. loi
Hectare I Square miles 107641 .01
Square kilometre .3861090 10764101
Square myriametre. . 38.61090 1
.0000012
.0001196
.0119601
1.19601
119.6011
1196.011
11960.11
1196011
.000247
.024711
.247110
2.47110
247-110
247110
Seldom used.
Metric Weights, Reduced to Avoirdupois 41
Metric, Cubic or Solid Measure by U. S. Standard
Cubic inches
Millilitre or cubic cen-
. 0610254
Liquid
.0084537 gill.
Dry
.0018162 pint.
.610254
Liquid
.084537 gill.
Dry
.018162 pint.
6.10254
Liquid
.84537 gill.
Dry
.18162 pint.
61.0254
Liquid
1. 05671 quart = 2.1134 pints.
Dry
.11351 peck = .9031 qt. = 1. 816 pts.
610.254
Cubic feet
■353156
Liquid
2.64179 gallons
Dry
.283783 bu. = 1.1351 pks. = 9.081 qts.
3 53156
Liquid
26.4179 gallons.
Dry
2.83783 bushel.
Kilolitre or cubic metre
35.3156
Liquid
264.179 gallons ) ,
Dry
28.3783 bushels )
Myrialitre or decastere.
353.156
Liquid
2641.79 gallons )
Dry
283.78 bushels j
Metric Weights, Reduced to Avoirdupois
Measure
Milligramme
Centigramme
Decigramme
Gramme
Decagramme
Hectogramme
Kilogramme
Myriagramme
Quintal
Tonneau, millier or tonne
Avoirdupois
.015432 grains
.15432
I. 5432
15.432
.022046 lbs.
.22046
2.2046
22.046
220.46
2204.6
The base of the French system of weights is the gramme; which is
the weight of a cubic centimeter of distilled water at maximum density,
at the sea level and at the latitude of Paris, Barometer 29.922 inches.
42
Weights an<l Measures
Mktkic LiNKAi. Mkasuke
Millimetre. .
Centimetre- .
Decimetre. ..
Metre
Decametre . .
Hectometre.
Kilometre. ..
Myriametre.
Metres | Inches
100
1000
lOOOO
.<J.W,»7
3937
3 937
39 368S
Feet
.00328
.0328
.3280
3.2807
32.807
328.07
.^280.7
32807
Yards
.10936
I 0936
10.936
109 36
1093.6
I09,j6
Miloi
.0621347
.621347
6.21347
Metric Square ^^Ieasurz
Measures
Square centimetre
" decimetre.
" centare.. . .
Are
Hectare
Square
metres
Square
inches
■ IS5
155
1.549-88
154.988
Square kilometre
" myriametre .
Square
feet
. 10763
10.763
1.076.3
107,630
Acres
Square
yards
Acres
.01196
1.196 I .00025
TTO <■' .0247
2.47
Square miles
247
24.708
.38607
38.607
Metric, Cubic or Solid Measure
Measures
Cubic centimetre
" decimetres
Centistere
Decimstere
Stere
Decastere
Hectostere
Cubic
metres
.0001
.001
Cubic
inches
.061016s
61.0165
610.16s
6101.6s
Cubic feet
.353105
3 S3I05
35.310S
353. los
3531 .OS
Cubic
yards
.13078
1.3078
13.078
130.78
Circular Measure
43
Metric Weights
Weight
Grammes
Troy grains
Avoirdupois
ounces
Avoirdupois
pounds
.001
.01
.1
I
10
100
1,000
10,000
100,000
1,000,000
.01543
.1543
1.543
15.43316
.03528
.3528
3.52758
35.2758
Decigramme
Gramme
Decagramme
.0022047
.022047
. 2204737
2.204737
22.04737
220.4737
2204 . 737
i
Metric Dry and Liquid Measures
Measures
Litres
Cubic inches
Cubic feet
Millilitre i
.001
.01
.1
I
10
100
1,000
10,000
.061
.61
6.1
61.02
610.16
Litre
3. 531
Kilolitre ... .
35 31
353.1
Circular Measure
60 seconds (") i minute (')•
60 minutes (') i degree (°).
90 degrees (°) i quadrant.
360 degrees (°) circumference.
Time
60 seconds i minute.
60 minutes i hour.
24 hours I day.
7 days I week.
365 days, 5 hours, 48 minutes, 48 seconds = i year.
Every year whose number is divisible by 4 is a leap year and contains
366 days.
The Centismal years are leap years only when the number of the year
is divisible by 400.
44
Weights niid Measures
Board and Timber Measure
The imil of nie;i>iiremeiil i.^ ;i Ixiard i j Iik Ik> s(iii;irc by one inch thick.
To ascertain the number of feel lM)ar(J measure in a plank or piece of
square limber, multiply the length by the breadth in feet and by the
thickness in inches.
To fmd the cubic contents of a stick of limber (all the measurements
beinK reduced to feet), lake one-fourth the product of the mean girth by
the diameter and the length.
To fmd tiie cubic contents of square limber, reduce all measurements
to feel, then the product of the length by the breadth and thickness will
be the volume in cuiiic feel.
Miscellaneous Measures and Weights
1 barrel of 9our weighs 196 pounds.
I barrel of salt weighs 280 "
I barrel of beef or pork weighs 200 "
I bushel of salt (Syracuse) weighs 56 "
Anthracite coal (broken) averages 54 lbs. to the cubic foot.
Bituminous coal (broken) averages 49 " " " '' "
Cement (Portland) weighs 96 lbs. to the bushel.
G\T3sum (ground) " 70 " " "
Lime (loose) " 7° "
Lime (well-shaken) " 80 " " " "
Sand " 98 " " " cubic foot or 1.181 tons
to the cu. yd.
Useful Factors
Inches
X
X
0.08333
0.02778
0 00001578
0.00695
0.0007716
0.00058
0 0000214
0 004.329
0 MM
0.00019
144 0
0 II12
1728
0 03704
7 48
= feet
= vards
.<
X
= miles
Square Inches. . . .
X
. . . . X
= square feet
= square yards
Cubic inches
X
X
= cubic feet
= cubic yards
.<
X
= U. S. gallons
Feet
X
X
= yards
= miles
Square feet
.... X
X
= square inches
= square yards
Cubic feet
.. X
X
= cubic inches
= cubic yards
•.
X
= U. S. gallons
Measures of Work, Power and Duty
45
Useful Factors — {Continued)
Yards X 36 = inches
•• X 3 = feet
" X 0.0005681 = miles
Square yards X i ,296 = square inches
" " X 9 = square feet
Cubic yards X 46,656 = cubic inches
" X 27 = cubic feet
Miles X 63,360 = inches
" ; . . X S ,280 = feet
" X 1,760 = yards
Avoirdupois ounces X .0.0625 = pounds
X 0.00003125 = tons
" pounds X 16 = ounces
" " X .001 = hundredweight
" " X .0005 = tons
" " 27.681 = cubic inches of
water at 39.2° F
" tons X 32,000 = ounces
" " X 2,000 = pounds
Watts X 0.00134 = horse power
Horse power X 746 = watts
Weight of round iron per fool = square of diameter in quarter inches -f- 6.
Weight of flat iron per foot = width X thickness X io-3.
Weight of flat plates per square foot = 5 pounds for each 1-8 inch thickness.
Measures of Work, Power and Duty
Work is the result of expenditure of energy in overcoming resistance.
Tiie unit of work is tiie pressure of one pound exerted through a distance
of one foot and is called one foot pound.
Horse Power. — Term employed to measure the quantity of work.
The unit is one horse power; or the quantity of work performed in
raising 33,000 lbs., one foot in one minute
= 33,000 foot pounds per minute
= 550 foot pounds per second
= 1,980,000 foot pounds per hour.
A heat unit is the amount of heat required to raise one pound of water
at maximum density i° F., or i pound of water from 39° F. to 40° F. =
778 foot pounds.
One horse power = 2545 heat units per hour
33,000
778
= 42.146 heat units per minute
= .7021 heat units per second.
.,6
Mathematical Tables
Tadlk of SguAKKS, CuHKS, Sqi:akk Rocjts and Cube
Ruurs OF Numbers fkou .i to io
No.
Square
CulJc
Square
root
Cube
root
No.
Square
Cube
Square
root
Cube
root
.1
.01
.001
.3163
.4642
4.1
16.81
68 921
3.03S
1. 601
IS
.0225
.0034
.3873
5313
4-2
17 64
74.088
3.049
1. 613
.3
04
.008
.4472
.58.18
4 3
18.49
79 S07
2 074
I 626
.25
.0635
.0156
■ Soo
.6300
4 4
19 36
85 184
2098
1 639
.3
09
•037
.5477
.66<J4
4 5
20 25
91 125
2 121
1 651
.35
.1225
.0429
.5916
.7017
46
21.16
97 336
2 145
1 663
.4
.16
.064
• 652s
.7368
4 7
23.09
J03 833
3.168
I 675
45
.203S
.0911
.6708
.7663
4.8
23.04
110.592
3.191
1 687
5
25
125
• 7071
.7937
4.9
24.01
117 649
2 314
1698
55
3025
.1664
7416
.8193
5
25
125
2 3361
I 710
.6
.36
.316
.7746
• 84.VI
5-1
36.01
132.651
2 358
I 721
.65
■422s
.3746
.8063
.8662
52
37-04
140.608
2.380
I 732
.7
•49
• 343
.8367
.8879
5-3
38.09
148.877
2.302
I 744
.75
.562s
.4219
.8660
.9086
5 4
39.16
157.464
2.324
I 754
.8
.64
■ 512
8944
• 9283
S-5
30.35
»66.375
2 345
I 76s
.85
.7225
.6141
,9219
• 9473
S-6
31.36
175.616
2.366
I 776
.9
.81
•729
.9487
• 9655
5-7
33.49
185.193
2.387
1 786
95
.9025
.8574
9747
.9830
5.8
3364
195- 112
2.408
"797
I
I
I
I
I
5 9
34.81
20s -379
2.429
1.807
I 05
I . 1025
1.158
1.025
1. 016
'•
''^
216
2.4495
1.8171
I.I
I 31
I 331
1.049
1.032
- 21
226.981
2 470
1.837
1.15
I 3225
1. 521
1.072
1.048
-■- 44
238.328
2 490
I 837
1.2
I 44
1 . 728
1.09s
1.063
'■) 3
39.69
250.047
2 sio
1.847
1-25
1.5625
I 953
1. 118
1.077
6-4
40.96
262.144
2 530
I 857
13
1.69
2.197
1. 140
1.091
6-5
42.35
274.625
2.S50
1.866
I 35
1.822s
2.460
I 163
I.ios
6.6
43-56
287.496
2.569
1.876
14
1.96
2.744
1. 183
1.119
6-7
44-89
300.763
2.588
1.885
1 45
2.1025
3.049
1.304
1. 132
6.8
46.34
314-432
2.608
I «9S
1-5
2.25
3.375
1.3247
I. 1447
6-9
47.61
328.509
2.627
1.904
I 55
2.402s
3 724
1.345
1.157
7
49
343
2.6458
I. 9129
16
256
4.096
1.265
1. 170
7.1
SO. 41
357. 9"
2.665
1.923
I 65
2 7225
4.492
1.285
1.183
7.2
51.84
373.248
2 683
I 931
17
2.98
4.913
1.304
I 193
7.3
53.29
389.017
2.702
1.940
1 75
3 062s
5.359
I 323
1.20s
7.4
54-76
405.334
3.730
I 949
1.8
3 24
5.832
I 342
l,3l6
7.5
56.25
431.875
2.739
1.9S7
1.85
3 422s
6.332
1.360
1.338
7-6
57-76
438-976
2.757
1.966
19
361
6.859
I 378
1.339
7.7
59 29
456.533
2.775
1. 975
I 95
3 8025
7.415
I 396
1.349
7.8
60.84
474.553
2.793
1.983
2
4
8
I. 4142
1.2599
7.9
62.41
493.039
2.811
1.992
2.1
4 41
9.26
1.449
1. 281
8
64
513
2.8384
3
33
4.84
10.648
1483
1.301
8.1
65.61
531 -441
2.846
2.008
33
5 29
13.167
I 517
1.330
8.2
67.24
551.368
2.864
3.017
34
5.76
13.824
1.549
1.339
8.3
68.89
571-787
2.881
"2.035
2.5
6.25
IS 625
I.S81
1-357
8.4
70.56
593.704
2.898
3.033
3.6
6.76
17.576
I.6l3
1-375
8.5
72.25
614.135
2.915
3.041
3.7
7.29
19 683
I 643
I 392
8.6
73-96
636.056
2-933
3.049
3.8
7.84
21.952
1.673
1.409
8.7
75.69
658.503
2.950
3.057
2.9
8.41
24.389
1.703
1.426
s s
-7 44
681.473
2.966
3.06s
3
9
27
I 7,?2I
1.442
- f 21
704.969
2.983
3.073
3.1
9 61
29 791
I 761
1-458
729
3
3.081
3.2
10 34
.12 76S
1.789
1 474
".' 1
«2 8l
753-571
3.017
3.088
3 3
10.89
.J5 937
1. 817
I 489
9.2
84.64
778-688
3033
3.09s
3.4
11.56
39 304
I 844
I..S04
9 3
86.49
804.357
3 oso
3.103
3.5
13. 35
42.87s
1. 871
1-518
9.4
88 36
830.584
3-066
3.110
36
13.96
46.656
1.897
1-533
9.5
90.2s
857.3-5
3- 082
3.118
3 7
13 69
50.653
1.924
1-47
9.6
92.16
884.736
3.098
3.135
3.8
14 44
54.872
1.949
I-560
9-7
94-09
912.673
3. 114
2.133
3.9
IS 21
59 319
1.975
1-574
9.8
96.04
941.192
3.130
2.140
4
I6
64
3
I.S874
9.9
98.01
970-399
3.146
2.147
Table of Squares, Cubes, Square Roots and Cube Roots 47
Table of Squares, Cubes, Square Roots and Cube Roots
OF Numbers from i to iooo
Remark on the Following Table. Wherever the effect of a fifth decimal in the
roots would be to add i to the fourth and final decimal in the table, the addition has
been made.
No.
Square
Cube
Square
root
Cube
root
No.
50
Square
Cube
Square
root
Cube
root
I
I
I
2,500
125,000
7.0711
3.6840
2
4
8
I. 4142
1.2599
SI
2,601
132,651
7
1414
3
7084
3
9
27
I . 7321
1.4422
52
2,704
140,608
7
2111
3
7325
4
16
64
2
1.5874
53
2,809
148,877
7
2801
3
7563
5
25
125
2.2361
I. 7100
54
2,916
157,464
7
3485
3
7798
6
36
216
2.4495
1.8171
55
3.025
166,375
7
4162
3
8030
7
49
343
2.645S
I. 9129
56
3.136
175,616
7
4833
3
8259
8
64
512
2.8284
2
57
3.249
185,193
7
5498
3
8485
9
81
729
3
2.0801
58
3.364
195,112
7
6158
3
8709
10
100
1,000
3 1623
2.1544
59
3.481
205,379
7
6811
3
8930
II
121
1. 331
3.3166
2.2240
60
3.600
216,000
7
7460
3
9149
12
144
1,728
3.4641 I2.2894
6i
3.721
226,981
7
8102
3
9365
13
169
2,197
3-6056
2.3513
62
3.844
238,328
7
8740
3
9579
14
196
2,744
3.7417
2.4101
63
3,969
250,047
7
9373
3
9791
15
225
3.375
3.8730
2.4662
64
4,096
262,144
8
4
16
256
4.096
4
2.S198
65
4.225
274,625
8
0623
4
0207
17
289
4,913
4.1231
2.5713
66
4.356
287,496
8
1240
4
0412
18
324
5.832
4.2426
2.6207
67
4.489
300,763
8
i8S4
4
061S
19
361
6,859
4.3.S89
2.6684
68
4,624
314,432
8
2462
4
0817
20
400
8,000
4.4721
2.7144
69
4.761
328,509
8
3066
4
1016
21
441
9.261
4.5826
2.7589
70
4.900
343,000
8
3666
4
1213
22
484
10,648
4.6904
2.8020
71
5.041
357,911
8
4261
4
1408
23
529
12,167
4.7958
2.8439
72
5.184
373,248
8
4853
4
1602
24
576
13.824
4.8990
2.8845
73
5.329
389.017
8
5440
4
1793
25
625
15.625
5
2.9240
74
5.476
405.224
8
6023
4
1983
26
676
17,576
5.0990
2.9625
75
5.62s
421.875
8
6603
4
2172
27
729
19,683
5.1962
3
76
5.776
438.976
8
7178
4
2358
28
784
21,952
5.2915
3.0366
77
5.929
456,533
8
7750
4
2543
29
841
24,389
5.3852
3.0723
78
6,084
474,552
8
88x8
4
2727
30
900
27,000
5.4772
3.1072
79
6,241
493.039
8
8882
4
2908
31
961
29,791
5.5678
3.1414
80
6,400
512,000
8
9443
4
3089
32
1,024
32,768
5.6569
3.1748
81
6,561
531,441
9
4
3267
33
1,089
35,937
5.7446
3.2075
82
6,724
551,368
9
0554
4
3445
34
1,156
39,304
S.8.?io
3.2396
83
6,889
571,787
9
1 104
4
3621
35
1.225
42,875
5.9161
3.2711
84
7.056
592,704
9
1652
4
3795
36
1,296
46.656
6
3.3019
85
7.225
614,125
9
2195
4
3968
37
1,369
50,653
6,0828
3.3322
86
7,396
636,056
9
2736
4
4140
38
1.444
54.872
6.1644
3.3620
87
7,569
658,503
9
3274
4
4310
39
1,521
59.319
6.2450
3.3912
88
7,744
681,472
9
3808
4
4480
40
1,600
64,000
6.3246
3.4200
89
7,921
704,959
9
4340
4
4647
41
1,681
68,921
6.4031
3.4482
90
8,100
729,000
9
4868
4
4814
42
1,764
74.088
6.4807
3.4760
91
8.281
753,571
9
5394
4
4979
43
1,849
79.S07
6.5574
3.5034
92
8,464
778.688
9
5917
4
5144
44
1.936
85,184
6.6332
3.5303
93
8,649
804,357
9
6437
4
5307
45
2,025
91.125
6.7082
3.5569
94
8,836
830,584
9
6954
4
5468
46
2,116
97,336
6.7823
3.5830
95
9.025
857,375
9
7468
4
5629
47
2,209
103,823
6.8557
3.6088
96
9,2l6
884,736
9
7980
4
5789
48
2,304
110,592
6.9282
3.6342
97
9,409
912.673
9
8489
4
5947
49
2,401
117.649
7
3.6593
98
9.604
941.192
9
8995
4
6104
48
Rlallicmalical Tables
Table of Squares, Cubes, Square Roots and Cube Roots
Of Numbers from i i<> iooo — {Continued)
No.
Square
Cube
Square
root
Cube
root
No.
Square
Cube
Square
root
Cube
root
99
9.801
970.299
9 9499
4 6261
152
23.104
3.S11.808
12 3288
5 3J68
loo
10,000
1.000.000
10 4 6416
I. S3
23.409
3.581. 577
>2 3fi<J\
; 34«s
lOI
10,201
I.O.W.IOI
10 0499
4 6570
154
21.716
3.652.264
12.4097
5 3601
I02
10.404
1.061,208
10,0995
4 6723
155
24X325
3.723.87s
12.4499
S.3717
103
10,609
1.092,727
10 1489
4.687s
156
24.336
3.796.416
12.4900
s 38.32
104
10,816
1.124,864
10 1980
4.7027
157
24.649
3.869,893
12 S300
s 3947
los
II. 02s
1. 1 57 .625
10.2470
4.7177
158
24.964
3.944.312
125698
S.4061
io6
11.236
1,191.016
10,2956
4.7326
159
25.281
4.019,679
12 6o9S
S.4I7S
107
11.449
1.225.043
10.3441
4.7475
160
25.600
4.096.000
12.6491
S.4288
108
11.664
1. 259.712
10.3923
4.7622
161
25.921
4. 173. 281 ; 12.6886
S.4401
109
11.881
1,295.029
10.4403
4.7769
162
26.244
4.251.S28
12.7279
5 4514
no
12.100
1. 331. 000
10,4881
4.79U
163
26.569
4.330.747
12.7671
S-4626
III
12.321
1.367.631
10,5357
4.8059
164
26,896
4.410.944
12.8067
5 4737
112
12.S44
1.404,928
10.5830
4.8203
16s
27,225
4.492.12s
12.8452
5 4848
113
12,769
1.442.897
10.6301
4 8346
166
27.556
4.574.296
12.8841
5-4959
114
12.996
1.481.544
10.6771
4.8488
167
27.889
4.657.463
12.9228
5 S069
IIS
13.22s
1.520,87s
10.7238
4.8629
168
28.224
4.741.632
12.961S
S.S178
116
13.456
1,560,896
10.7703
4.8770
169
28.561
4,826.809
13
S.S288
117
13.689
1.601,613
10.8167
4 8910
170
28,900
4.913.000
13.0384
S 5397
118
13.924
1.643.032
10.8628
4 9049
171
29.241
S.OOO,2II
13.0767
S.5505
119
14. 161
1.685.159
10.9087
4.9187
172
29.584
s.088.448
13.1149
s 5613
lao
14.400
1,728.000
10.9545
4.9324
173
29.929
S.I77.717
13.1529
S 5721
121
14.641
1.771,561
II
4.9461
174
30.276
s.268.024
13.1909
5. 5828
122
14.884
1.815.848
II.04S4
4.9597
175
30.625
5.359.375
13-2288
5.5934
123
IS. 129
1,860.867
11.0905
4-9732
176
30.976
5.451.776
13.2665
5 6041
124
IS. 376
1.906.624
II 1355
4.9866
177
31.329
3.545.233
13.3041
5.6147
I2S
15.62s
1.953,125
11.1803
5
178
31.684
5. 639.752
13.3417
5. 6252
126
IS. 876
2.000,376
1 1 . 22SO
5.0133
179
32.041
5.735.339
13.3791
5-6357
127
16.129
2.048.383
11.2694
5.0265
180
32.400
S. 832 .000
13.4164
5-6462
128
16.384
2.097.152
"■3137
5. 0397
181
32.761
5.929.741
13.4536
5-6567
129
16.641
2.146,689
11.3578
5.0528
182
33.124
6.028.568
13.4907
5 -6671
130
16,900
2.197.000
11,4018
5.0658
183
33.489
6,128,487
13 5277
5 -6774
131
17.161
2,248,091
11.4455
5.0788
184
33.856
6,229,504
13.5647
5- 6877
132
17.424
2.299.96S
I I. 4891
S.0916
185
34.225
6.331.625
13 60IS
5.6980
133
17.689
2.352.637
11.5326
S1045
186
34.596
6.4.34,856
13.6382
5-7083
134
17.956
2,406,104
11.5758
5. 1172
187
34.969
6.539.203
13.6748
5.718s
I3S
l8,225
2.460,375
II. 6190
5.1299
188
35.344
6,644,672
13.7113
5. 7287
136
18,496
2.515.456
11.6619
S.1426
189
35.721
6.751,269
13.7477
5.7388
137
18.769
2.S7I.353
11.7047
5.1551
190
36.100
6.859.000
13.7840
5-7489
138
19.044
2.628,072
"7473
5.1676
191
36.481
6.967.871
13.8203
5 7590
139
19.321
2,685.619
11.7898
5.1801
192
36.864
7.077.888
13.8564
S.7690
140
19.600
2.744.000
11.8322
5.1925
193
37.249
7.189.057
13.8924
5 7790
141
19.881
2.803.221
11.8743
5.2048
194
37.636
7.301.384
13.9284
5.7890
142
20.164
2.863.288
11.9164
S.2171
195
38.02s
7.414.875
13.9642
5 7989
143
20.449
2.924.207
11.9583
S 2293
196
38.416
7.529.536
14
5.8088
144
20.736
2. 98s .984
12
5.2415
197
38.809
7.645.373
14.0357
5.8186
MS
21.025
3.048,625
12.0416
5.2536
198
39.204
7.762.392
14.0712
5.828s
146
21.316
3.I12.136
12.0830
5.2656;
199
39.601
7.880.599
14.1067
58383
147
21.609
3.176.523
12.1244
5.2776^
200
40,000
8.000.000
14 1421
5.8480
148
21.904
3.241,792
12.1655
5.2896,
201
40,401
8.120.601
M 1774
).8S78
149
22,201
3.307.949
12 2066
5.3015;
202
40.804
8,242,408
14.2127 .
;867S
ISO
22,500
3.375.000
12.2474
5 3133
203
41,209
8.365.427
14-2478 .
; 8771
151
22.801
3.442.951
12.2882
5 32SI
1
ao4
41.616
8,489.664
14 2829 .
8868
Table of Squares, Cubes, Square Roots and Cube Roots 49
Table of Squares, Cubes, Square Roots and Cube Roots
OF Numbers from i to iooo — (Coniinued)
No.
Square
Cube
Square
root
Cube
root
No.
258
Square
Cube
Square
root
Cube
root
20s
42,02s
8,615,125
14.3178
5. 8964
66,564
17,173,512
16.0624
6 3661
206
42,436
8,741,816
14-3527
5 9059
259
67,081
17,373,979
16.093s
6 3743
207
42,849
8,869,743
14-3875
S-9IS5
260
67,600
17,576,000
16.1245
6.3825
208
43,264
8,998,912
14.4222
5-92.S0
261
68,121
17,779,581
16.1555
6.3907
209
43,681
9,129,329
14-4568
5-9345
262
68,644
17,984,728
16.1864
6.3988
210
44,100
9,261,000
14.4914
S-9439
263
69,169
18,191,447
16.2173
6 4070
211
44.521
9.393.931
14.5258-
5 -9533
264
69,696
18,399,744
16.2481
6 41SI
212
44,944
9,528,128
14-5602
5. 9627
265
70,225
18,609,625
16.2788
6 4232
213
45,369
9,663,597
14-5945
5.9721
266
70,756
18,821,096
16.3095
6 4312
214
45,796
9,800,344
14.6287
5.9814
267
71,289
19,034,163
16.3401
6 4393
215
46,225
9,938,375
14.6629
5 -9907
268
71,824
19,248.832
16.3707
6 4473
216
46,656
10,077,696
14.6969
6
269
72,361
19,465,109
16.4012
6 4553
217
47,089
10,218,313
14.7309
6.0092
270
72,900
19,683,000
16.4317
6 4633
218
47,524
10,360,232
14.7648
6.0185
271
73,441
19,902,511
16.4621
6.4713
219
47,961
10,503,459
14.7986
6.0277
272
73,984
20,123,648
16.4924
6.4792
220
48.400
10,648,000
14.8324
6.0368
273
74.529
20,346,417
16.5227
6.4872
221
48,841
10,793,861.
14.8661
6.0459
274
75,076
20,570,824
16.5529
6.4951
222
49,284
10,941 ,048
14-8997
6.0550
275
75,62s
20,796,875
16.5831
6.5030
223
49.729
11,089,567
14-9.332
6.0641
276
76,176
21,024,576
16.6132
6.5108
224
50,176
11,239,424
14.9666
6.0732
277
76,729
21,253,933
16.6433
6.5187
22s
50,625
11,390,625
IS
6.0822
278
77,284
21,484,952
16.6733
6.5265
226
51,076
II,.543.I76
15.0333
6.0912
279
77,841
21,717,639
16.7033
6-5343
227
51,529
11,697,083
15.0665
6.1002
280
78,400
21,952,00c
16.7332
6-5421
228
51,984
11,852,352
15.0997
6.1091
281
78,961
22,188,041
16.7631
6-5499
229
52,441
12,008,989
15- 1327
6.1180
282
79.524
22,425,768
16.7929
6-5577
230
52,900
12,167,000
15-1658
6.1269
283
80,089
22,665,187
16.8226
6.5654
231
53.361
12,326,391
IS -1987
6.1368
284
80,656
22,906,304
16.8523
6 5731
232
53,824
12,487,168
IS-23IS
6.1446
28s
81,225
23.149,125
16.8819
6.5808
233
54,289
12,649,337
IS -2643
6.1534
286
81,796
23,393,656
16.9115
6.588s
234
S4,7S6
12,812,904
15-2971
6.1622
287
82,369
23,639,903
16.9411
6.5962
235
55,225
12,977,875
15-3297
6.1710
288
82,944
23,887,872
16.9706
6.6039
236
55,696
13,144,256
15.3623
6.1797
289
83,521
24,137,569
17
6-611S
237
56,169
13,312,053
IS. 3948
6. 1885
290
84,100
24,389,000
17.0294
6.6191
238
56,644
13,481,272
15.4272
6.1972
291
84,681
24,642,171
17.0587
6.6267
239
57.121
13,651,919
15.4596
6.2058
292
85,264
24,897,088
17.0880
6.6343
240
57.600
13,824,000
15.4919
6.2145
293
85,849
25,153,757
17.1172
6.6419
241
58,081
13,997,521
15.5242
6.2231
294
86,436
25,412,184
17.1464
6.6494
242
58,564
14.172.488
15.5563
6.2317
29s
87,025
25,672,375
17.1756
6.6569
243
59,049
14.348.907
15.5885
6.2403
296
87,616
25,934,336
17.2047
6.6644
244
59.536
14,526,784
15.6205
6.2488
297
88,209
26,198,073
17.2337
6.6719
245
60,025
14,706,125
15.6525
6.2573
298
88,804
26.463,592
17.2627
6.6794
246
60,516
14,886,936
15.6844
6.2658
299
89,401
26,730,899
17.2916
6.6869
247
61,009
15,069,223
15.7162
6.2743
300
90,000
27,000,000
17. 320s
6.6943
248
61,504
15,252,992
15.7480
6.2828
301
90,601
27,270,901
17.3494
6.7018
249
62,001
15,438,249
15.7797
6.2912
302
91,204
27,543,608
17.3781
6.7092
250
62,500
15,625.000
IS.8II4
6.2936
303
91,809
27,818,127
17.4069
6.7166
251
63,001
15,813,251
15.8430
6,3080
304
92.416
28,094,464
17.4356
6.7240
252
63,504
16,003,008
IS. 8745
6.3164
305
93.025
28,372,62s
17.4642
6.7313
253
64,009
16,194,277
15 - 9060
6.3247
306
93,636
28,652,616
17.4929
6-7387
254
64,516
16,387,064
15-9374
6.3330
.307
94,249
28.934,443
17.5214
6 7460
255
65,025
16,581 ,.375
IS -9687
6.3413
308
94,864
29,218,112
17.5499
6.7533
256
65.536
16,777,216
16
6.3496
309
95,481
29,503,629
17.5784
6 7606
257
66,049
16,974,593
16.0312
6. 3579
310
96,100
29,791,000
17.6068
6.7679
so
Malhcmalicul Tables
Tabix op Squares, Cubes, Square Roots and Cube Roots
OF Numbers from i to looo — (Continued)
Square
96.721
97.344
97.969
98.596
99.225
99.856
100,489
101,124
101,761
102,400
103,041
103,684
104,329
104,976
105,625
106,276
106,929
107,584
108,241
108.900
109,561
110,224
110,889
111.556
112,225
112,896
113.569
114.244
114.921
115.600
116,281
116,964
117.649
118,336
119.02s
119.716
120,409
121,104
121,801
122. soo
123.201
123.904
124.609
125.316
126.025
126,736
127,449
12S.164
128.881
i29.(Joo
130,321
131.044
131,769
Cube
30.371,328
30.664,297
30,959.144
31.255.875
31.554.496
31.855.013
32.157.432
32.461,759
32,768.000
33.076.161
33..i.S6.248
33.698.267
34.012.224
34.328.125
34.645.976
34.965.783
35.287.552
35.611,289
35.937.000
36,264.691
36.594.368
36.926,037
37.259.704
37.595.375
37.933.056
38.272.753
38.614,472
38,958,219
39.304.000
39.651.821
40,001,68s
40,353.607
40,707.584
41.063,625
41.421.736
41.781.923
42.144.192
42.508,549
42.875.000
43.243.551
43.614.208
43.9S6.977
44.361.864
44.738.875
45.118.016
45.499.293
45.882.712
46,268,279
46,656.000
47.045.881
47.4.37.928
47.832.147
Square
Cube
v#*
root
root
.^0.
364
17 6352
6 7752
17663s
6 7824
365
17 6918
6 7897
366
17.7200
6 7969
367
17.7482
6.8041
368
17 7764
6.S113
369
17 804s
6.8185
370
17.8326
6.8256
371
17.8606
6.8328
372
17.888s
6.8399
373
17.9165
6.8470
374
17.9444
6.8541
375
17.9722
6.8612
376
18
6.8683
377
18.0278
6. 8753
378
18.0555
6.8824
379
18.0831
6 8894
380
18.1108
6 8964
381
18.1384
6.9034
382
18.1659
6.9104
383
18.1934
6 9174
384
18.2209
6.9244
385
18.2483
6.9313
386
18.2757
6.9382
387
18.3030
6.9451
388
18.3303
6.9521
389
18.3576
6.9589
390
18.3848
6.9658
391
18.4120
6.9727
392
18.4391
6.979s
393
IS. 4662
6.9864
394
18.4932
6.9932
395
18.5203
7
396
18.5472
7.0068
397
18.5742
7.0136
398
18.6011
7 . 0203
399
18 6279
7.0271
400
18.6548
7.0338
401
18.6815
7.0406
402
18.7083
7.0473
403
18.7350
7.0540
404
18.7617
7.0607
40s
18.7883
7.0674
406
18.8149
7.0740
407
18.8414
7.0807
408
18.8680
7.0873
409
18.8944
7 0940
410
18.9209
7 1006
411
18 9473
7 . 1072
412
18.9737
7.I138
413
19
7.1204
414
19 0263
7.1269
415
19.0526
7.1335
416
Square
132.496
1.33.225
13.5.956
134.689
135.424
136.161
136.900
137.641
138.384
139.129
139.876
140.625
141.376
142.129
142,884
143.641
I44,.»oo
145.161
145.924
146,689
147,456
148.225
148,996
149.769
150.544
151.321
152,100
152,881
153.664
154.449
155.2.56
156,025
156,816
157,609
158.404
159.201
160,000
160,801
161,60.1
162,409
163,216
164,025
164.836
165,649
166.464
167.281
168.100
168.921
169.744
170.569
171.396
172,225
173.056
Cube
48.228,544
48,627,125
49/527,896
49.430.863
49.836/532
So.243,409
50,653.000
51.064,811
51.478.848
51.895,117
52,313.624
52.734.375
53,157.376
53.582.633
54.010,152
54.439.939
54.872.000
55Jo6,34l
55,742,968
56,181,887
56,623,104
57,066,625
57,512,456
57.960,603
58,411,072
58,863,869
59.319.000
59.776.471
60,236,288
60,698,457
61,162,984
61,629,875
62,099.136
62,570,773
63,044.792
63.521.199
64,000.000
64.481.201
64.964.808
65,450.827
65.939.264
66,430.125
66.923,416
67,419.143
67,917.312
68,417.929
68,921,000
69,426,531
69,934,528
70,444.997
70.957.944
71 .473.375
71.991.296
Square
fXX>t
0788
.1050
1311
1572
1833
2094
23S4
2614
2873
3132
3391
3649
3907
416s
4422
4679
4936
5192
5448
9 5704
9 5959
9 6214
9 6469
9 6723
9 6977
19 7231
9 7484
9 7737
9 7990
9 8242
9 8494
9 8746
9 8997
9.9249
9 9499
9 9750
20
20 0250
20.0499
20.0749
20.0998
20.1246
20 1494
20.1742
20. 1990
20.2237
20.2485
20.2731
20.2978
20.3224
20.3470
20 371s
20 3961
Table of Squares, Cubes, Square Roots and Cube Roots 51
Table of Squares, Cubes, Square Roots aistd Cube Roots
OF Numbers from i to iooo — {Continued}
No
Square
Cube
Square
root
Cube
root
No.
Square
Cube
Square
root
Cube
root
417
173.889
72,511.713
20.4206
7.4710
470
220,900
103,823,000
21.679s
7.7750
418
174,724
73,034,632
20.4550
7.4770
471
221,841
104,487,111
21.7025
7.7805
419
175,561
73,560,059
20.4695
7.4829
472
222,784
105,154,048
21.7256
7.7860
420
176,400
74,088,000
20.4939
7.4889
473
223,729
105,823,817
21.7486
7.7915
421
177,241
74,618,461
20.5183
7.4948
474
224,676
106,496,424
21.7715
7-7970
422
178,084
75,151,448
20.5426
7.5007
475
225,625
107,171.875
21.7945
7 8025
423
178,929
75,686,967
20.5670
7 5067
476
226,576
107,850,176
21.8174
7.8079
424
179,776
76,225,024
20.5913
7.5126
477
227.529
108,531,333
21.8403
7-8134
425
180,625
76,765,625
20.6155
7.5185
478
228,484
109,215,352
21.8632
7.8188
426
181,476
77,308,776
20.6398
7.5244
479
229,441
109,902,239
21.8861
7.8243
427
182,329
77,854,483
20.6640
7.5302
480
230,400
110,592,000
21.9089
7-8297
428
183,184
78,402,752
20.6882
7.5361
481
231,361
111,284,641
21.9317
7.8362
429
184,041
78,953,589
20.7123
7.5420
482
232,324
111,980,168
21.9545
7.8406
430
184,900
79,507,000
20.7364
7.5478
483
233,289
112,678,587
21.9773
7.8460
431
185,761
80,062,991
20.7605
7.5537
484
234,256
113,379,904
22
7.8514
432
186,624
80,621,568
20.7846
7.5595
485
235,225
114,084,125
22.0227
7.8568
433
187,489
81,182,737-
20.8087
7.5654
486
236,196
114,791,256
22.0454
7-8622
434
188,356
81,746,504
20.8327
7.5712
487
237.169
115,501,303
22.0681
7.8676
435
189,225
82,312,875
20.8567
7.5770
488
238,144
116,214,272
22.0907
7-8730
436
190,096
82,881,856
20.8806
7.5828
489
2.39,121
116,930,169
22.1133
7.8784
437
190,969
83,453,453
20.9045
7.5886
490
240,100
117,649,000
22.1359
7.8837
438
191,844
84,027,672
20.9284
7.5944
491
241,081
118,370,771
22.1585
7-8891
439
192,721
84,604,519
20.9523
7.6001
492
242,064
119,095,488
22.1811
7.8944
440
193,600
85,184,000
20,9762
7.6059
493
243,049
119,823,157
22.2036
7-8998
441
194,481
85,766,121
21
7.6117
494
244.036
120,553,784
22.2261
7-9051
442
195,364
86,350,888
21.0238
7.6174
495
245,025
121,287,375
22.2486
7 -9105
443
196,249
86,938,307
21.0476
7.6232
496
246,016
122,023,936
22.2711
7-9158
444
197,136
87,528,384
21.0713
7.6289
497
247,009
122,763,473
22.2935
7.9211
445
198,025
88,121,125
21.0950
7.6346
498
248,004
123.505,992
22.3159
7-9264
446
198,916
88,716,536
21.1187
7.6403
499
249,001
124,251,499
22.3383
7.9317
447
199,809
89,314,623
21.1424
7.6460
500
250,000
125,000,000
22.3607
7-9370
448
200,704
89,915,392
21 . 1660
7.6517
501
251,001
125.751,501
22.3830
7.9423
449
201,601
90,518,849
21.1896
7.6574
502
252,004
126,506,008
22.4054
7.9476
450
202,500
91,125,000
21.2132
7.6631
S03
253,009
127,263,527
22.4277
7-9528
451
203,401
91,733,851
21.2368
7.6688
S04
254,016
128,024,064
22.4499
7.9581
452
204,304
92,345,408
21.2603
7.6744
505
255,025
128,787,625
22.4722
7-9634
453
205,209
92,959,677
21.2838
7.6801
506
256,036
129,554,216
22.4944
7.9686
454
206,116
93,576,664
21.3073
7.6857
507
257,049
130,323,843
22.5167
7-9739
455
207,02s
94,196,375
21.3307
7.6914
508
258,064
131,096,512
22.5389
7-9791
456
207,936
94,818,816
21.3542
7.6970
509
259,081
131,872,229
22.5610
7-9843
457
208,849
95,443,993
21.3776
7.7026
510
260,100
132,651,000
22.5832
7-9896
458
209,764
96,071,912
21.4009
7.7082
511
261,121
133,432,831
22.6053
7-9948
459
210,681
96,702,579
21.4243
7.7138
512
262,144
134,217,728
22 . 6274
8
460
211,600
97,336,000
21.4476
7.7194
513
263,169
135,005,697
22.6495
8-0052
461
212,521
97.972,181
21.4709
7 . 72.S0
514
264,196
135,796,744
22.6716
8 0104
462
213,444
98,611,128
21.4942
7.7306
515
265,225
136,590,875
22.6936
8.0156
463
214,369
99,252,847
21.5174
7.7362
516
266,256
137,388,096
22.7156
8.0208
464
215,296
99,897,344
21.5407
7.7418
517
267,289
138,188,413
22 7376
8.0260
465
216,225
100,544,625
21.5639
7.7473
518
268,324
138,991.832
22.7596
8.0311
466
217.156
101,194,696
21.5870
7.7529
519
269,361
139.798.359
22.7816
8.0363
467
218,089
101,847,563
21.6102
7.7584
520
270,400
140,608,000
22.8035
8.0415
468
219,024
102,503,232
21.6,333
7-7639
521
271,441
141,420,761
22.8254
8.0466
469
219,961
103,161,709
21.6564
7.7695
522
272.484
142,236,648
22.8473
8.0S17
52
Matliematical Tables
Table op Squares, Cubes, Square Roots and Cube Roots
OF Numbers from i to iooo — {CotUinucd)
No.
Square
Cube
Square
root
Cube
root
N' .
root
Cube
root
S2i
273.529
143.oss.667
22.869a
8 0569
576
131.776
191,102.976
24
8 3203
524
274.576
143.877.824
22.8910
8 0620
577
332.929
192,100,033
24 oao8
8 3251
S2S
275.625
144.703.12s
22 9129
8.0671
578
334.084
193.100.ss2
24 0416
8 3J00
526
276,676
145.531.576
22 9347
8 0723
579
3.55.241
194.104 .539
24 0624
8 3348
527
277.729
146,363.183
22.9565
8 0774
.SKo
.5.56.400
l9S,ll2/xx>
24 0832
8 .5396
528 278.781
'47.I97.9.S2
22 9783
H 0H25
.581
337.561
196,132,941
24 1039
8 .VW5
529 279.811
148.035.889
2i
8 0876
S82
338.724
197.137368
24 1247
8 .54QI
530 280,900
148.877,000
23.0217
8.0927
S8.»
339.889
198.155.287
24 1454
K .55.19
S3I 281. y6i
119.721,291
23 04.3.J
80978
584
341.056
199.176.704
24 1661
8 .5587
S.?2 2S,<.024
l.W.568,768
23 o''i5l
8.1028
58S
342.22s
200.2OI ,625
24 1868
83634
Si? 284.089
151.419.437
23.0S68
8.1079
586
343.396
201 ,230/556
24 2074
8 .3682
534 285.156
152.273.304
23.1084
8.11.50
587
344.569
202.262.003
24 2281
8 3730
S.V5 286.225
153. 130.375
23.1.501
8.1180
588
345.744
203.297.472
24 2487
8 3777
536 1 2S7.296
153.990.656
23.1517
8.1231
S89
346.921
204.336.469
24 2693
8 382s
537 J 288.369
154.854.153
23.1733
8.1281
590
348,100
20s .379.000
24.2899
8.3872
538 ! 289,441
155.720,872
23.1948
8.1332
591
349.281
206.425,071
24 310s
8 3919
S?9 , 290.521
1.56,590.819
23.2164
8.1382
592
350.464
207.474.688
24 33"
83967
540 291.600
157.464.000
23.2379
8.14.53
593
351.649
208.526.857
24.3516
8.4014
541
2y2.68i
158.3.10,421
23.2594
8.1483
594
352,836
209..584.584
24 3721
8.4061
542
293,764
l59.2JO,o88
23.2809
8. 1533
595
354 .02s
210,644.875
24. 5926
8.4108
543
294.819
160,103.007
23.3024
8.1583
596
355.216
211,708.7,56
24 4131
8 415s
544
295.936
160,989,184
23.3238
8.163.5
597
356.409
212,776,173
24 4536
8 4202
545
297.025
161.878,62s
23.3452
8.1683
598
357.604
213.847.192
24 4540
8 4249
546 298.116
162.771.336
23.3666
8.1733
599
358.801
214.921.799
24 4745
8 4296
547
293.209
163.667,323
23.3880
8.1783
600
360,000
216.000,000
24 4949
8.4343
548
300.304
164.566,592
23.4094
8. 1833
601
361,201
217.081 .801
24 5153
8.4390
549
301,401
165,469.149
23.4307
8.1882
602
362,404
218,167.208
24 5357
8.4437
550
,502.500
166,375,000
23.4521
8.1932
603
363.609
219,256.227
24 5561
8 4484
551
.503.601
167,284,151
23 -4734
8.1982
604
364.816
220,348.864
24 5764
8.4530
552
304,704
168,196.608
23.4947
8 2031
60s
366.02s
221.445.125
24.5967
8.4577
553
305.809
169,112,377
23.5160
8.2081
606
367.236
222,545.016
24.6171
8 4623
554
306.916
I7o.o3l.46»
23.5272
8.2130
607
368.449
223.648,543
24 6374
8.4670
555
30S.025
170,953.875
23.5584
8.2180
608
369.664
224,755.712
24.6577
8.4716
556
.309,136
171,879.616
23.5797
8.2229
609
370.881
225,866,529
24.6779
8.4763
557
310,249
172,808,693
23.600S
8.2278
6io
372,100
226,981 ,000
24.6982
8.4809
558
311.364
173.741. 112
23.6220
8.2327
611
373.321
228.099.131
24.7184
8.4856
559
312.481
174.676,879
23.6432
•*. 2377
612
374.544
229.220,928
24.7386
8 4902
s6o
313.600
175,616,000
23.66.13
S.2426
613
375.769
230,346.397
24.7588
8.4948
561
314.721
176.s58.48l
23.6854
8.247s
614
376,996
231.475.544
24.7790
8.4994
562
315.844
177.504,328
23.7065
S.2524
615
378.22s
232,608,375
24 7992'
8.S040
563
316,969
178,453.547
23.7276
8.2573
616
379.456
233.744.896
24.8193
8 S086
564
318.096
179.406,144
23.7487
S.2621
617
380.689
234.885,113
24.8395
8.S132
565
319.225
180,362,12s
23.7697
8.2670
618
381,924
236,029,032
24.8596
8.5178
S66
320,356
181,321,496
23.7908
8.2719
619
383.161
237.176,659
24.8797
8.5224
567
321.489
182,284,263
23.8118
8.2768
620
384.40c
238.328.000
24.8998
8.5270
568
322,624
183.2.50,432
23.8328
8.2816
621
385.641
239.483.061
24.9199
8.5316
569
323.761
184,220,009
23.85,57
8 2865
622
386.884
240.641,848
24 9399
8.5362
S70
,524.900
185,193.000
23 8747
8.2913
623
,588,129
24 1, 804 .,567
24.9600
8.5408
571
326.041
186. 169.411
23 8956
8 2962
624
389.376
242.970,624
24.9800
8 5453
572
327,184
187,149,248
23 916s
8 3010
625
,590.625
244.140,62s
25
8.5499
573
328.329
188,132.517
23 9374
8 ..5059
626
391.876
245.314.376
25 0200
8 5544
574
329.476
189,119.224
23 95«3 8.3107
627
.593.129
246.491,883
2S 0400
8 5590
575
330,625
190.109.375
23 9792 8.31SS
628
394.384
247.673.152
25.0590
8.5635
Table of Squares, Cubes, Square Roots and Cube Roots 53
Table of Squares, Cubes, Squaije Roots and Cube Roots
OF Numbers from i to iooo — {Continued)
No.
Square
Cube
Square
root
Cube
root
No.
682
Square
Cube
Square
root
Cube
root
629
395,641
248,858,189
25.0799
8.5681
465,124
317,214,568
26.1151
8.8023
630
396,900
250,047.000
25.0998
8.5726
683
466,489
318.611.987
26.1343
8.8066
631
398,161
251.239,591
23.1197
8 5772
684
467,856
320,013,504
26.1534
8.8109
632
399.424
252,435,968
25.1396
8.5817
68s
469,225
321,419,125
26.1725
8.8152
633
400,689
253,636,137
25.1595
8.5862
686
470,596
322,828,856
26.1916
8.8194
634
401,956
254,840,104
25.1794
8.5907
687
471,969
324,242,703
26.2107
8.8237
635
403,225
256,047,875
25.1992
8.5952
688
473.344
325,660,672
26.229S
8.8280
636
404,496
257.259.456
25.2190
8.5997
689
474,721
327,082,769
26.2488
8.8323
637
40s. 769
258.474,853
25.2389
8.6043
690
476,100
328.509.000
26.2679
8.8366
638
407,044
259,694,072
25.2587
8.6088
691
477,481
329,939,371
26.2869
8.8408
639
408,321
260,917,119
25.2784
8.6132
692
478,864
331,373,888
26.3059
8.8451
640
409,600
262,144,000
25.2982
8.6177
693
480,249
332,812,557
26.3249
8.8493
641
410,881
263.374.721
25.3180
8.6222
694
481,636
334,255,384
26.3439
8.8536
642
412,164
264,609.288
25. 3377
8.6267
695
483,025
335.702,37s
26.3629
8.8578
643
413,449
265.847,707
25.3574
8.6312
696
484,416
337.153.536
26.3818
8.8621
644
414,736
267,089,984
25.3772
8.6357
697
485,809
338.608.873
26 . 4008
8.8663
645
416,025
268,336,12s
25.3969
8.6401
698
487,204
340,068.392
26.4197
8.8706
646
417.316
269,586,136
25.4165
8.6446
699
488,601
341. 532.099
26.4386
8.8748
647
418,609
270,840,023
25.4362
8.6490
700
490,000
J43.ooo.ooo
26.4575
8.8790
648
419,904
272,097,792
25.4558
8.65.35
701
491,401
344.472,101
26.4764
8.8833
649
421,201
273,359.449
25 4755
8.6579
702
492,804
345.948,408
26.4953
8,8875
650
422,500
274,625,000
25.4951
8.6624
703
494,209
347.428.927
26.SI41
8.8917
6sr
423,801
275,894.451
25.5147
8.6668
704
495,616
348.913,664
26.5330
8.8959
652
425,104
277,167,808
25-5343
8.6713
70s
497,025
.350.402.625
26.5518
8.9001
653
426,409
278,445,077
25 5539
8.6757
706
498,436
351.895,816
26.5707
8.9043
6S4
427,716
279,726,264
25.57.34
8.6801
707
499.849
353,393,243
26.5895
8.9085
6S5
429,025
281,011,375
25 5930
8.684s
708
501,264
354.894,912
26.6083
8.9127
656
430,336
282,300,416
25.6125
8.6890
709
502,681
356,400,829
26.6271
8.9169
657
431,649
283,593,393
25.6320
8.6934
710
504,100
357 .91 1. 000
26.6438
8.9211
658
432,964
284,890,312
25.6515
8.6978
711
505,521
359.425.431
26.6646
8 925. J
659
434,281
286,191,179
25.6710
8.7022
712
506,944
360.944.128
26.6833
8 9295
660
435,600
287,496,000
25.6905
8.7066
713
508,369
362.467.097
26.7021
8.9337
661
436,921
288,804,781
25.7099
8.7110
714
509,796
363.994.344
26.7208
8.9378
662
438,244
290,117,^28
25.7294
8.7154
715
511,225
365.525.87s
26.7395
8.9420
663
439,569
291,434,247
25.7488
8.7198
716
512,656
367.061,696
26.7582
8.9462
664
440,896
292.754.944
25.76S2
8.7241
717
514,089
368.601.813
26.7769
8.9503
66s
442,225
294,079,62s
25.7876
8.7285
718
515,524
370.146,232
26.7955
8.9545
666
443,556
295,408,296
25.8070
8.7329
719
516,961
371.694.939
26.8142
8.9587
667
444.889
296,740,963
25.8263
8.7373
720
518,400
373.248.000
26.8328
8.9628
668
446,224
298,077,632
25.8457
8.7416
721
519,841
374.805.361
26.8514
8.9670
669
447,561
299,418,309
25.8650
8.7460
722
521,284
375,367,048
26 . 8701
8. 971 I
670
448,900
300,763,000
25.8844
8.7503
723
522,729
377,933,067
26.8887
8.9752
671
450,241
302.111,711
25.9037
8.7547
724
524.176
379,503,424
26 . 9072
8.9794
672
451,584
303,464,448
25.92.50
8.7590
725
525,62s
381.078,12s
26.9258
8.9835
673
452,929
304,821,217
25.9422
8.7634
726
527,076
382,657.176
26.9444
8.9876
674
454,276
306,182.024
25.9615
8.7677
727
528.529
384,240,583
26.9629
8.9918
67s
455.625
307.546.875
25.9808
8.7721
728
529,984
385,828,352
26.981S
8.9959
676
456,976
308.915,776
26
8.7764'
729
531.441
387,420,489
27
9
677
458,329
310,288,733
26.0192
8.78071
730
532.900
389,017,000
27.0185
9.0041
678
459,684
311,6.65.752
26.0384
8.7850!
731
534,361
390,617,891
27.0370
9.0082
679
461,041
313.046.839
26.0576
8.7893'
732
535.824
392,223.168
27.0555
9.0123
680
462,400
314.432.000
26.0768
8. 7937 1
733
537.289
393,832,837
27.0740
9.0164
681
463,761
315.821. 241
26.0960
8.7980
734
1
538,756
395,446,904
27.0924
9.0205
54
Mallu-m;ilit;il luiilcs
Table of Squares, Cubes, Square Roots avd Cube Roots
OF Numbers from i to looo — (CotUinutd)
Squnre
Cube
Square
Cube
No.
Sc|uare
Cube
root
root
No.
S(juarp
Cube
root
root
135
540.225
397,065.375
27.1109
9.0246
788
620.944
489.303.872
28 0713
9 236s
736
541.696
398,688.256
27.1293
9 0287
789
622.521
491.169.069
28 0891
9 2404
737
543.169
400.315.553
27.1477
9 0328
790
624,100
493.039.000
28 1069
9 2443
738
544.644
401.947.272
27.1662
9 0369
791
625,681
494.913.671
28 1247
9 2482
739
546.121
403.583.4 19
27.1846
9 0410
792
627,264
496.793.088
28 142s
9 2521
740
547.600
405.224,0D0
27 . 2029
9 0450
793
628,849
498.677.257
28 1603
9.2560
741
549.081
406,869,021
27.2213
9 0491
794
630,436
500,566,184
28 1780
9 2599
742
550,564
408,518,488
27.2397
9 0532
795
632,025
502,459.875
28 1957
9.2638
743
552.019
410,172,407
27.2580
9 0572
796
63.},6i6
504 ,,3.58,336
28 2135
9 2677
744
553.536
411,8,50.784
27 2764
9 0613
797
6,55,209
506.261,573
28 2312
9 2716
745
555.025
413.493,625
27.2947
90654
798
636,804
508,169.592
28.2489
9 2754
746
556.516
415,160,936
27 31. JO
90694
799
638,401
5 10.082. ,599
28 2666
9 2793
747
558.009
416,832.723
27.3313
9 07.55
800
640,000
512.000.000
28 3843
9 2832
748
559.504
418.508.992
27.3496
9 077s'
801
641,601
513.922,401
28 3019
9.2870
749
561.001
420,189.749
27.3679
9.o8i6|
802
643.204
5iS.849.608
28 3196
9 2909
7SO
562.500
421,875.000
27.3861
9 0856
803
644.809
Si7.78l.627
28 3373
9 2948
751
564.001
423.564,751
27.4044
9.0896' [804
646.416
Si9.718.464
28 3549
9 2986
752
565.504
425.259,008
27.4226
9.0937 805
648,02s
52 1. 660. 125
28 3725
9 3025
753
567.009
426.957.777
27.4408
9.0977I 806
649.636
523.606.616
28 3901
9 3063
754
568.516
428.661.064
27.4591
9.1017 1807
651.249
525. 557. 943
28.4077
9 3102
755
570.025
430.368.875
27.4773
9.1057 1 808
652.864
527.514. 112
28 4253
9 3140
756
571.536
432.081,216
27. 4955
9.1098
809
654.481
529.475,129
28 4429
9 3179
757
573.049
433.798.093
27.5136
9 1 138
810
6.56.100
531.441.000
28 4605
9 3217
758
574.564
435.519.sl2
27.5318
9.1178
811
657.721
53,5,411,731
28.4781
9 32SS
759
576.081
437.245.479
27.5500
9.1218
812
659.344
535,387,328
28 4956
9 3294
760
577.600
438,976.000
27.5681
9.12581
813
660.969
537,-567.797
28 5132
9 3332
761
579.121
440.71 1. 081
27.5862
9.1298;
814
662.596
S.W.353.I44
28.5307
9 3370
762
580.644
442,450,728
27.6043
9.1338I
815
664.225
541.343.375
28.5482
9 3408
763
582.169
444.194,947
27.6225
9- 1378,
816
665.856
S43.338.496
28.5657
9 3447
764
583.696
445.943.744
27.6405
9.i4i8''8i7
667,489
545..538.513
28.5832
9 348s
765
585.225
447.697.125
27.6586
9. 1458'! 818
669,124
547.iJ3.432
28.6007
9 3523
766
586.756
449.455,096
27.6767
9.1498
819
670,761
549.353.259
28.6182
9 3561
767
588.289
451.217,663
27.6948
9-1537
820
672,400
551,368,000
28 6356
9 3599
768
589,824
452,984.832
27.7128
9- 1577
821
674.041
553,387.661
28.6531
9 3637
769
591.361
454.756,609
27.7308
9.1617
822
675.684
555.412.248
28 . 6705
9-3675
770
592,900
456,533.000
27.7489
9- 1657
823
677.329
557.441.767
28.6880
9 3713
771
594.441
458,314.011
27.7669
9.1696
824
678,976
559.476.224
28.7054
9 37SI
772
595.984
460,099,648
27.7849
9-1736
82s
680.625
561.515.625
28.7228
9 3789
773
597.529
461,889.917
27.8029
9-1775
826
682,276
563.5s9.976
28.7402
9 3827
774
599.076
463,684,824
27.8209
9-1815
827
683,929
S65.609.283
28.7576
9 386s
775
600,625
465,484.37s
27.8388
9-1855
828
685.584
!;67.6(>3.552
28.7750
9.3902
776
602,176
467.288.576
27.8568
9.1894
829
687.241
569.722,789
28.7924
9 3940
777
603,729
469.097.4.33
27.8747
9- 1933
830
688.900
571,787.000
28.8097
9 3978
778
605,284
470.910,952
27.8927
9-1973
831
690.561
573,856,191
28.8271
9.4016
779
606,841
472,729,139
27.9106
9.2012
832
692.224
573.930,368
28.8444
9 4053
780
608,400
474.5S2.ooo
27.9285
9-2052
833
693.889
578,009.5.57
28.8617
9 4091
781
609,961
476.379.541
27.9464
9.2091
834
695.556
580,093,704
28 . 8791
9 4129
782
611,524
478.211.768
27.9643
9 2130
835
697,225
582,182,87s
28.8964
9 4166
783
613,089
480.048.687
27.9821
9.2170
836
698,896
584,277,056
28 9137
9 4204
784
614,656
481.890.304
28
9.2209
837
700.569
S86,376,2.S3
28 9310
9 4241
78s
616,225
483.736.625
28.0179
9.2248
838
702.244
588.480.472
28.9482
9 4279
786
617.796
485.587.656
28.0357
9.2287
839
703.921
590.S89.719
28.9655
9 4316
787
619.369
487,443.403
28.0S3S
9.2326
840
705.600
592.704,000
26.9828
9 4354
Table of Squares, Cubes, Square Roots and Cube Roots 55
Table of Squares, Cubes, Square Roots and Cube Roots
OF Numbers from i to iooo — (Continued)
No.
Square
Cube
Square
root
Cube
root
No.
894
Square
Cube
Square
root
Cube
root
841
707,281
594.823,321
29
J.439I
799,236
714.516,984
29.8998
9 6334
842
708,964
596,947,688
29.0172
J.4429
895
801,025
716,917.375
29.9166
9.6370
843
710,649
599,077,107
29-0345
J. 4466
896
802.816
719.323.136
29.9333
9.6406
844
712,336
601,211,584
290517
).4503
897
804,609
721,734,273
29.9500
9.6442
84s
714,025
603,351,125
29.0689
)-454i
898
806,404
724.150.792
29.9666
9.6477
846
715.716
605,495.736
29.0861 (
).4578
899
808,201
726,572,699
29-9833
9.6513
847
717.409
607,645,423
29.1033 <
)-46i5
900
810,000
729,000,000
30
9-6549
848
719.104
609,800,192
29.1204 (
).4652
901
811,801
731,432,701
30.0167
9.658s
849
720,801
611,960,049
29.1376 c
^.4690
902
813,604
733,870,808
30.0333
9.6620
850
722,500
614,125,000
29.1548 c
)-4727
903
815,409
736,314.327
30.0500
9 6656
851
724,201
616,295,051
29.1719 c
)-4764
904
817,216
738,763,264
30 0666
9.6692
852
725,904
618,470,208
29.1890 c
).48oi
905
819,025
741.217.625
30.0832
9.6727
8S3
727.609
620,650,477
29.2062 c
.4838
906
820,836
743.677.416
30.0998
9 6763
8S4
729.316
622,835,864
29,2233 c
.4875
907
822,649
746.142,643
30.1164
9 6799
8SS
731.025
625,026,375
29.2404 c
.4912
908
824,464
748,613,312
30. 1330
9 6834
856
732,736
627,222,016
29.2575 c
-4949
909
826,281
751,089,429
30.1496
9.6870
857
734,449
629,422,793
29.2746 c
.4986
910
828,100
753,571,000
30.1662
9.6905
858
736,164
631,628.712
29.2916 c
■ 5023
911
829,921
756,058,031
30.1828
9 6941
859
737,881
633.839.779
29.30S7 c
.5060
912
831.744
758,550,528
30.1993
9.6976
860
739.600
636.056,000
29 3258 c
-5097
913
833.569
761,048,497
30.2159
9.7012
861
741,321
638,277.381
29.3428 c
■ 5134
914
8.?S.396
763.551,944
30.2324
9.7047
862
743.044
640,503,928
29.3598 c
-5171
915
837.225
766.060,87s
30.2490
9.7082
863
744.769
642,735.647
29.3769 c
-5207
916
8,?9.056
768,575,296
30.2655
9.7118
864
746.496
644,972,544
29-3939 g
.5244
917
840,889
771,095.213
30.2820
9 7153
86s
748.225
647,214,625
29.4109 c
-5281
918
842.724
773 620,632
30.2985
9.7188
866
749.956
649,461,896
29.4279 S
-5317
919
844.561
776,151.559
30.3150
9.7224
867
751.689
651,714.363
29.4449 S
-5354
920
846,400
778,688,000
30.3315
9.7259
868
753.424
653.972.032
29.4618 5
-5391
921
848,241
781,229.961
30.3480
9.7294
869
755.161
656,234.909
29.4788 g
-5427
922
850,084
783.777.448
30.3645
9.7329
870
756,900
658,503.000
29.4958 s
-5464
923
851,929
786,330,467
30.3809
9-7364
871
758,641
660,776,311
29.5127 5
-5501
924
853,776
788.889,024
30.3974
9.7400
872
760,384
663,054.848
29.5296 s
-5537
925
855.625
791,453,125
30.4138
9-7435
873
762,129
665,338,617
29.5466 g
-5574
926
857.476
794,022,776
30.4302
9.7470
874
763.876
667,627,624
29.563s c
.5610
927
859.329
796,597.983
30.4467
9 -7505
875
765.625
669,921,875
29.5804 s
-5647
928
861,184
799.178.752
30.4631
9-7540
876
767,376
672,221,376
29.5973 S
-5683
929
863,041
801,765,089
30.4795
9-7575
877
769.129
674,526,133
29.6142 c
-5719
930
864,900
804,357,000
30.4959
9.7610
878
770.884
676,836,152
29.6311 c
-5756
931
866.761
806,954,491
30.5123
9 7645
879
772,641
679.151.439
29.6479 g
-5792
932
868,624
809,557,568
30.5287
9.7680
880
774.400
681,472,000
29.6648 c
.5828
933
870,489
812,166,237
30.5450
9-771S
881
776.161
683,797.841
29.6816 c
-5865
934
872.356
814,780,504
30.5614
9-77SO
882
777.924
686,128,968
29.6985 g
■ 5901
935
874.225
817,400,375
30.5778
9.7785
883
779.689
688,465,387
29-7153 g
.5937
936
876,096
820,025.856
30.5941
9 7819
884
781,456
690,807,104
29-7321 g
5973
937
877.969
822,656,953
30.6105
9.7854
885
783.225
693.154.125
29.7489 g
.6010
938
879.844
825,293,672
30.6268
9.7889
886
784.996
69s. 506. 456
29.7658 c
.6046
939
881,721
827.936.019
30.6431
9.7924
887
786,769
697.864,103
29.7825 c
.6082
940
883,600
830.584,000
30.6594
9-7959
888
788.544
700,227,072
29-7993 g
.6118
941
885,481
8,«.2.37,62l
30.6757
9.7993
889
790.321
702,595,369
29.8161 c
.6154
942
887,364
8,?5 ,896,888
30 . 6920
9.8028
890
792,100
704,969,000
29.8329 g
.6190
943
889.249
838,561,807
30.7083
9.8063
891
793.881
707,347,971
29.8496 f
).6226
944
891.136
841,232,384
■?o 7246
9.8097
892
795.664
709,732,288
29.8664 c
).6262
945
893.025
843,908,625
30.7409
9.8132
893
797.449
712,121,957
29.8831 Ig
(.6298
946
894,916
846,590,536
30.7571
9.8167
56
Mathcmalical Tal)les
Table of Squares, Ci'bes, Square Roots avd Cube Roots
OF Numbers from i to iooo (Continued)
No.
Square
Cube
Square
root
Cube
root
No.
biiuiirr
Cube
Square
root
Cube
947
8y6.8o9
8.19,278,123
30.7734
9.8201
974
948,676
924/>lo.424
31 2090
9.9126
948
898,704
851,971,392
30.78969 82j6|
975
950,625
926.8s9.375
31 22SO
9.9160
949
900,601
854,670,3.19 30.80589.8270!
976
952.576
929.714.176
31-2410
9 9«94
9SO
902. soo
857,375,000
30.8221 9 830s
977
954.529
932.S74.833
31-2570
9 9227
9SI
904,401
860,085,351
30.83839 8339
978
956.484
935.441.352 31-2730
9 9261
952
906.304
862,801,408
30.85459 8374
979
958.441
938.313.73931-2890
9 929s
953
908,209
865,523,177
30.8707 9.8408
980
960.400
941.192.000 31. 30SO
9 9329
954
910,116
868,250,664
30.88699.8443
981
962.361
944,076, Ul'31. 3309
9 9363
955
912,025
870,983,875
30.9031 9 8477
982
964.324
916,966,168^31.3.369
9 9396
956
9«3.936
873,722,816
30.9192 9. 851!
983
966.289
949.862.087 31.3528
9 9430
957
915,849
876,467,493
30.93549 8546
984
968.256
952.763.904 31 3688
9.9464
9S8
917,764
879.217,912
30.95169.8580
985
970,225
955.671.62s 31.3847
9-9497
959
919.681
881,974,079
30.96779 8614
986
972.196
958.585. 256 31.4006
9 9531
960
921,600
884,736,000
30.98399 86.18
987
974,169
961.504.803 31.4166
9 956s
961
923,521
887.503,681
31 9-8683
988
976,144
964.4.^0,272 31.4.325
9 9598
962
925.444
890,277,128
31.0161 9 8717
989
978,121
967.361,66931.4484
9 9632
963
927,369
893,056,347
31.03229.8751
990
980,100
970.299,00031.4643
9.9666
964
929,296
895.841,344
31.04839 878s
991
982,081
973.242.271 31.4802
9 9699
965
931.22s
898.632.125
31.0644 9.8819
992
984.064
976.191.48831.4960
9-9733
966
933.156
901.428,696
31.0805 9 8854
993
986,049
979.146.657 31 -SI 19
9 9766
967
935.089
904,231,063
31.0966 9.8888
994
988.036
982,107.784 31.5278
9-9800
968
937.024
907.039.232
31.1127 9 8922
995
990.025
985.074,87531-5436
9 9833
969
938.961
909.853.209
31.1288 9 8956
996
992.016
988,047,93631.5595
9.9866
970
940,900
912.673,000
31.14489 8990
997
994,009
991,026,97331.5753
9.9900
971
942,841
915,498,611
31.16099 9024
998
996,004
994,011,99231.5911
9-9933
972
944,784
918,330,048
31.17699 9058
999
998.001
997,002,99931.6070
99967
973
946,729
921,167,317
31.19299-9092
IOOO
1,000,000
1,000,000,000 31.6228
10
To find the square or cube of any whole number ending
with ciphers. First, omit all the final ciphers. Take from the table the
sfiiKirc (ir tul)c (as the case may be) of the rest of the number. To this
square add twice as many ciphers as there were final ciphers in the original
number. To the cube add three times as many as in the original number.
Thus, for 90,500^, 905* = 819,025. Add twice 2 ciphers, obtaining
8,i9o,2So,cxx). For 90,500', 905* = 741,217,625. Add 3 times 2 ci-
phers, obtaining 741,217,625,000,000.
Table of Square Roots and Cube Roots of Numbers 57
Table of Square Roots and Cube Roots of Numbers
FROM 1000 TO 10,000
No errors
No.
Sq.
Cube
No.
Sq.
Cube
No.
Sq.
Cube
No.
Sq.
Cube
root
root
root
root
root
root
root
root
IOCS
31-70
10.02
1270
35-64
10.83
1535
39-18
11.54
1 1800
42.43
12.16
lOIO
31.78
10.03
1275
35-71
10.84
1540
39-24
II. 55
180S
42
49
12.18
1015
31.86
10.05
1280
35-78
10.86
1545
39-31
11-56
1810
42
-54
12.19
1020
31.94
10.07
128S
35-85
10-87
1550
39-37
II. 57
181S
42
60
12.20
1025
32.02
10.08
1290
35-92
10.89
1555
39-43
11-59
1820
42
66
12.21
1030
32.09
10.10
1295
35-99
10.90
1560
39-50
II -60
1825
42
72
12.22
I03S
32.17
10.12
1300
36.06
10.91
1565
39-56
II. 61
1830
42
78
12.23
1040
32.25
10.13
1305
36.12
10.93
1570
29.62
11.62
1835
42
84
12.24
104s
32.33
10. IS
1310
36.19
10.94
1575
39.69
11.63
1840
42
90
12.25
1050
32.40
10.16
1315
36.26
10.96
1580
39.75
11-65
1845
42
95
12.26
1055
32.48
10.18
1320
36.33
10.97
158s
39-81
11.66
1850
43
01
12.28
1060
32.56
I0.20
1325
36.40
10.98
1590
39-87
11.67
i8S5
43
07
12.29
1065
32.63
10.21
1330
36.47
II
1595
39-94
11.68
i860
43
13
12.30
1070
32.71
10.23
1335
36.54
II. 01
1600
40
11-70
1865
43
19
12.31
1075
32.79
10.24
1340
36,61
11.02
160S
40.06
II. 71
1870
43
24
12.32
1080
32.86
10.26
1345
36.67
11.04
1610
40.12
11.72
187s
43
30
12,33
1085
32.94
10.28
1350
36.74
11.05
161S
40.19
11-73
1880
43
36
12.34
1090
33 02
10.29
1355
36.81
11.07
1620
40.25
11-74
188s
43
42
12 -3S
1095
33.09
10.31
1360
36.88
11.08
1625
40.31
11.76
1890
43
47
12-36
1 100
33.17
10.32
1365
36.95
11.09
1630
40.37
11.77
1895
43
53
12-37
1 105
33.24
10.34
1370
37.01
II. II
163s
40.44
11.78
1900
43
59
12.39
mo
33.32
10.35
1375
37.08
II. 12
1640
40.50
11-79
190S
43
65
12.40
iiiS
33.39
10.37
13S0
37.15
II. 13
164s
40.56
11.80
1910
43
70
12.41
1 120
33.47
10.38
1385
37.22
II. IS
1650
40.62
11.82
191S
43
76
12.42
II2S
33. 54
10.40
1390
37-28
II. 16
1655
40.68
11.83
1920
43
82
12-43
1 130
33.62
10.42
1395
37. 35
II. 17
1660
40.74
11.84
1925
43
87
12.44
1 135
33.69
10.43
1400
37.42
II. 19
1665
40.80
11.85
1930
43
93
12. 4S
1 140
33.76
10.45
1405
37.48
11. 20
1670
40.87
11.86
1935
43
99
12.46
1 145
33.84
10.46
1410
37-55
II. 21
167s
40.93
11.88
1940
44
OS
12.47
I ISO
33.91
10.48
1415
37-62
II -23
1680
40.99
11.89
1945
44
10
12.48
"55
33.99
10.49
1420
37-68
11-24
168S
41-05
11.90
1950
44
16
12.49
1 160
34.06
10.51
1425
37-75
II -25
1690
4I-II
II. 91
I9S5
44
22
12.50
1165
34.13
10.52
1430
37-82
11.27
1695
4I-17
11.92
i960
44
27
12.51
1 170
34.21
10.54
1435
37-88
11.28
1700
41-23
11.93
1965
44
33
12.53
1175
34.28
10. 55
1440
37-95
11.29
170S
41-29
11-95
1970
44
38
12.54
1180
34.35
10.57
1445
38.01
II. 31
1710
41-35
11-96
1975
44-
44
12.55
1 185
34.42
10. sS
1450
38.08
11.32
1715
41-41
11-97
1980
44
SO
12.56
1190
34.50
10.60
I4SS
38.14
11-33
1720
41.47
11.98
1985
44-
55
12.57
1 195
34.57
10.61
1460
38.21
11-34
1725
41.53
11.99
1990
44
61
12.58
1200
34.64
10.63
146s
38.28
II -36
1730
41.59
12
199s
44
67
12.59
1 20s
34.71
10.64
1470
38.34
11-37
1735
41.6s
12.02
2000
44-
72
12.60
1210
34.79
10.66
1475
38.41
11-38
1740
41-71
12.03
200s
44-
78
12.61
1215
34.86
10.67
1480
38.47
11.40
•1745
41-77
12. 04
2010
44
83
12.62
1220
34.93
10.69
1485
38.54
II-4I
1750
41-83
12.05
201s
44
89
12.63
1225
35
10.70
1490
38.60
1I-42
1755
41-89
12.06
2020
44
94
12.64
1230
35.07
10.71
149s
38.67
11-43
1760
41.95
12.07
2025
45
12.65
1235
35.14
10-73
1500
38.73
11-45
1765
42.01
12.09
2030
45
06
12.66
1240
35.21
10.74
IS05
38.79
11.46
1770
42.07
12.10
2035
45
II
12.67
1245
35.28
10.76
1510
38.86
11-47
1775
42.13
12. II
2040
45
17
12.68
1250
35.36
10.77
1515
38.92
11-49
1780
42-19
12.12
2045
45
22
12.69
I2SS
35-43
10.79
1520
38.99
11-50
1785
42.25
12.13
2050
45
28
12.70
1260
35-50
10.80
1525
39.05
11-51
1790
42-31
12.14
2055
45
33
12.71
126s
35-57
10.82
1530
39-12
II-S2
1795
42-37
12.15
2060
45
39
12.72
S8
Mathematical Tallies
Table of Square Roots and Cube Roots of Numbers from
looo to io,(x>o — {Conliitued)
No.
Sq.
Cut*
No.
Sq.
Cube
No.
Sq.
Cube
No.
Sq.
Cube
root
root
root
root
root
root
root
root
3o6s
45 44
13.73
2330
48.27
13.26
2740
52. 35
1399
3270
57 i«
14.84
3070
45.50
12.74
2335
48.32
13 27
2750
52.44
14 01
3280
57-27
14.86
ao7S
45 55
12.75
2340
48.37
13.28
2760
52.54
14 03
3290
57 36
14.87
3n8o
45 61
12.77
2345
48.43
13 29
2770
52 63
14 04
3300
57-45
14.89
ao8s
45.66
12.78
i 23SO
48,48
13.30
2780
52,73
14 06
3310
57-53
14.90
ao9o
45.72
12.79
2.555
48.53
13 30
2790
52.82
14.08
3330
57-62
14.93
2095
45.77
12.80
2j6o
48.58
13.31
2800
52,92
14.09
3330
57.71
14.93
3 100
45 83
12. 8i
236s
48.63
13 32
2810
S3. 01
14 11
3340
57-79
14 95
3I05
45.88
12.82
2370
48.68
13.33
2820
S3, 10
14.13
3.M0
57.88
14 96
31 10
45. 93
12.83
2375
48.73
13.34
2830
S3. 20
14 14
3360
57 97
14 98
3IIS
45.99
12.84
2380
48.79] 13 35
2840
53.29
14.16
3370
58.05
14.99
2120
46.04
12.8s
238s
48.84I 13.36
28,50
53 39
14.18
3380
58.14
15 01
21 25
46.10
12.86
2390
48.89
13.37
2860
53-48
14.19
3390
58.23
15.02
2130
46.15
12.87
2395
48.94
13.38
2870
53. 57
14.21
3400
58.31
15 C4
3135
46.21
12.88
2400
48.99
13.39
2880
53 67
14.23
ilio
58.40
IS 05
3140
46.26
12.89
2405
49 04
13 40
2890
53.76
14.24
3420
58.48
15.07
3I4S
46.31
12.90
2410
49.09
13 41
2900
S3 85
14.26
3430
58.57
15.08
3150
46.37
12.91
2415
49.14
13.42
2910
S3 94
14 28
3440
58.65
15.10
3ISS
46.42
12.92
2420
49.19
13 43
2920
54.04
14-29
3450
58.74
15.11
3i6o
46.48
12.93
3425
49.24
13.43
2930
54.13
14-31
3460
58.82
15.12
2i6s
46.53
12.94
2430
49.30
13.44
2940
54.22
14-33
3470
58.91
IS. 14
2170
46.58
12.95
2435
49.35
13.45
2950
54.31
14-34
3480
58.99
15 15
2175
46.64
12.96
2440
49.40
13.46
2960
54. 41
14 36
3490
59 08
IS. 17
3i8o
46.69
12.97
2445
49-45
13.47
2970
54.50
14-37
3500
59.16
IS 18
2185
46.74
12.98
24SO
49.50
13.48
2980
54. 59
14-39
3510
59.25
15.20
2190
46.80
12.99
2460
49.60
13.50
2990
54.68
14-41
3S20
59. 33
IS. 21
2195
46.8s
13
2470
49.70
13.52
3000
54. 77
14-42
3530
5941 15.23
2200
46.90
13 01
3480
49.80
13. 54
3010
54.86
14-44
3S40
5950 15.24
2205
46.96
13 02
2.190
49.90
13 55
3020
54. 95
14 45
35SO
59.58
15.25
2210
47.01
13.03
2500
50
13 57
3030
SS. 05
14.47
3560
59.67
15.27
22IS
47.06
13.04
1 2510
50- 10
13.59
3040
55.14
14.49
3570
59.75
15.28
2220
47.12
13 05
2520
SO. 20
13 61
3050
55.23
14 SO
3580
59.83
IS-30
2225
47.17
13 05
2530
50.30
13.63
3060
55 32
14. 52
3590
5992
IS. 31
2230
47.22
1306
2540
50.40
13 64
3070
55. 41
14.53
3600
60
IS 33
3235
47.28
13.07
2550
SO. 50
13.66
3080
55. SO
14 55
3610
60 08] 15.34
2240
47.33
13. oS
2.i6o
SO. 60
13.68
3090
55.59
14,57
3620
60.17
15.35
3245
47.38
13.09
2570
SO. 70
13.70
3100
55.68
14 S8
3630
60.2s
15.37
3250
47.43
13 10
2580
SO. 79
13.72
3110
55-77
14 60
3640
60.33
15.38
2255
47-49
13.11
2590
50.89
13.73
3120
55-86
14.61
3650
60,42
15.40
2260
47.54
13.12
2600
50.99
13.75
3130
55.95
14,63
3660
60. so
15.41
2265
47.59
13 13
2610
SI. 09
13.77
3140
56,04
14.64
3670
60.58
15.42
3270
47.64
13.14
2620
SI. 19
13.79
3150
S6,l2
14.66
3680
60.66
15.44
3275
47.70
13.15
26.30 SI. 28
13.80
3160
56.21
14-67
3690
60.75
15.45
238o
47.75
13.16
2640
51.38
13.82
3170
56.30
14 69
3700
60.83
15.47
328s
47.80
13.17
2650
51.48
13.84
3180
56.39
14.71
3710
60.91
15.48
2290
47.85
13 18
2660
51.58 13.86
3190
56,48
14.72
3720
60.99
15.49
339s
47.91
13.19
2670
51.67 13.87
3200
S6,S7
14.74
3730
61.07
15.51
2300
47.96
13.20
2680
51.77 1389
3210
56.66
14.75
3740
61.16
15.52
2305
48.01
13.31
2690
SI. 87 13.91
3220
56.75
14.77
3750
61.24
15. 54
3310
48.06
13 22
2700
SI. 96 13 92
3230
56.83
14.78
3760
61.32
15-55
3315
48.11
13.23
2710
52.06 13.94
3240
56.92
14.80
3770
61.40
15.56
3330
48.17
13.24
2720
S2.I5 13.96
3250
57.01
14 81
3780
61.48
15 58
232s
48.22
13.25
3730
S2.2S 13.98
3260
57.10
14-83
3790
61.56
15. 59
Table of Square Roots and Cube Roots
59
Table of Square Roots and Cube Roots of Numbers from
looo TO 10,000 — {Continued)
No.
Sq.
root
Cube
root
IS. 60
No.
Sq.
root
Cube
root
No.
Sq.
root
Cube
root
No.
Sq.
root
Cube
root
•3800
61.64
4330
65.80
16.30
4860
69.71
16-94
S390
73-42
17 -S3
3810
61.73
15.62
4340
65.88
16.31
4870
69.79
16.95
5400
73-48
17.54
3820
61.81
15.63
4350
65-95
16.32
4880
69.86
16.96
5410
73 -SS
17-55
3830
61.89
IS. 65
4360
66.03
16.34
4890
69.93
16-97
5420
73-62
17-57
3840
61.97
15.66
4370
66.11
16.35
4900
70
16.98
S430
73.69
17-58
3850
62.05
15.67
43S0
66.18
16.36
4910
70.07
17
5440
73-76
17-59
3860
62.13
15.69
4390
66.26
16.37
4920
70.14
I7-OI
S450
73-82
17-60
3870
62.21
15.70
4400
66.33
16.39
4930
70.21
17.02
5460
73-89
17-61
3880
62.29
15.71
4410
66.41
16.40
4940
70.29
17-03
5470
73.96
17-62
3890
62.37
15-73
4420
66.48
16.41
49SO
70.36
17.04
5480
74-03
17-63
3900
62.45
15.74
4430
66.56
16.42
4960
70.43
17.05
S490
74-09
17-64
3910
62.53
15.75
4440
66.63
16.44
4970
70.50
17.07
SSoo
74-16
17-65
3920
62.61
15.77
44SO
66.71
16.45
4980
70.57
17.08
55 10
74-23
17-66
3930
62.69
15.78
4460
66.78
16.46
4990
70.64
17.09
5520
74.30
17-67
3940
62.77
IS. 79
4470
66.86
-16.47
Sooo
70.71
17.10
5530
74-36
17-68
3950
62.8s
15.81
4480
66.93
16.49
5010
70.78
17-11
S540
74-43
17-69
3960
62.93
15.82
4490
67.01
16.50
5020
70.85
17.12
5S50
74-50
17.71
3970
63.01
15.83
4500
67.08
16.51
5030
70.92
17.13
5560
74-57
17.72
3980
63.09
IS. 85
4510
67.16
16.52
5040
70.99
17 -IS
S570
74-63
17.73
3990
63. 17
15.86
4520
67-23
16.53
S050
71.06
17- 16
5580
74-70
17-74
4000
63.2s
15.87
4530
67-31
16.5s
5060
71.13
17.17
5590
74-77
17-75
4010
63 32
IS. 89
4S40
67.38
16.56
5070
71.20
17.18
5600
74-83
17.76
4020
63.40
15.90
4S50
67.4s
16.57
5080
71.27
17-19
5610
74-90
17-77
4030
63.48
15.91
4560
67.53
16.58
5090
71.34
17 -20
5620
74-97
17.78
4040
63.56
15-93
4S70
67.60
16.59
5100
71.41
17-21
5630
75-03
17-79
4050
63.64
IS. 94
4580
67.68
16.61
Siio
71.48
17.22
5640
75-10
17.80
4060
63.72
15 -9S
4590
67 -75
16.62
5120
71-55
17.24
5650
75-17
17.81
4070
63.80
IS- 97
4600
67.82
16.63
5130
71.62
17.25
5660
75-23
17.82
4080
63.87
IS -98
4610
67.90
16.64
S140
71.69
17.26
5670
75.30
17.83
4090
63.95
15.99
4620
67.97
16.66
51S0
71.76
17.27
5680
75-37
17.84
4100
64.03
16.01
4630
68.04
16.67
5160
71.83
17.28
5690
75-43
17-85
41T0
64.11
16.02
4640
68.12
16.68
S170
71.90
17.29
5700
75.50
17.86
4I20
64.19
16.03
4650
68.19
16.69
S180
71-97
17.30
S7IO
75-56
17.87
4130
64.27
16.04
4660
68.26
16.70
S190
72-04
17. 31
5720
75-63
17-88
4140
64.34
16.06
4670
68.34
16.71
5200
72.11
17.32
5730
75-70
17-89
4150
64.42
16.07
4680
68.41
16.73
5210
72.18
17.34
5740
75.76
17-90
4160
64.50
16.08
4690
68.. 48
16.74
5220
72.25
17. 35
S750
75.83
17-92
4170
64.58
16.10
4700
68.56
16.7s
5230
72.32
17 36
5760
75-89
17.93
4180
64.65
16. II
4710
68.63
16.76
5240
72-39
17.37
S770
75-96
17-94
4190
64.73
16.12
4720
68.70
16.77
5250
72.46
17.38
5780
76.03
17 -9S
4200
64.81
16.13
4730
68.77
16.79
5260
72.53
17.39
5790
76.09
17-96
4210
64.88
16. IS
4740
68.85
16.80
5270
72.59
17.40
5800
76.16
17.97
4220
64.96
16.16
4750
68.92
16.81
5280
72.66
17.41
5810
76.22
17-98
4230
65.04
16.17
4760
68.99
16.82
5290
72.73
17.42
5820
76.29
17.99
4240
65.12
16.19
4770
69.07
16.83
5300
72.80
17-44
S830
76.35
18
4250
65.19
16.20
4780
69.14
16. 85
5310
72.87
17-45
5840
76.42
18.01
4260
65.27
16.21
4790
69.21
16.86
S320
72.94
17.46
5850
76.49
18.02
4270
6S.35
16.22
4800
69.28
16.87
5330
73.01
17-47
5860
76. 55
18.03
4280
65.42
16.24
4810
69.35
16.88
5340
73.08
17 -48
5870
76.62
18.04
4290
65.50
16.25
4820
69.43
16.89
S3SO
73-14
17-49
5880
76.68
18. OS
4300
65.57
16.26
4830
69.50
16.90
5360
73-21
17 -SO
5890
76.75
18.06
4310
65.65
16.27
4840
69.57
16.92
5370
73-28
17. SI
5900
76.81
18.07
4320
65.73
16.29
4850
69.64
16.93
5380
73-35
17-52
S9IO
76.88
18.08
6o
Malhcmaticjil Tables
Table of Square Roots ajo) Cuue Roots of Numbers from
looo TO 10,000 — (CotUinued)
Sq.
Cube
root
root
76,94
18.09
77.01
18.10
77.07
18.11
77.14
18.12
77.20
18 13
77.27
18.14
77.. W
18. IS
77.40
18.16
77.46
18.17
77.52
18.18
77.59
18.19
77.65
18.20
77.72
18.21
77.78
18.22
77.85
18.23
77.91
18.24
77.97
18.2s
78.04
18.26
78.10
18.27
78.17
18.28
78.23
18.29
78.29
18.30
78.36
18.31
78.42
18.32
78.49
18.33
78.55
18.34
78.61
18.3s
78.68
18.36
78.74
18.37
78.80
18.38
78.87
18.39
78.93
18.40
78.99
18.41
79.06
18.42
79 12
18.43
79-18
18.44
79.25
18.45
79.31
18.46
79.37
18.47
79 44
18.48
79 50
18.49
79 56
18. so
79.62
18. SI
79- 69
18.52
79.75
18. S3
79.81
18.54
79.87
18. SS
79 94
18.56
80
18 .S7
80.06
18.58
80.12
18.59
80.19
18.60
80.2s
18.60
No.
6450
6460
6470
6480
6490
6500
6s«o
6520
6530
6540
6550
6560
6570
6580
6590
6600
66io
6620
6630
6640
6650
6660
6670
6680
6690
6700
6710
6720
6730
6740
6750
6760
6770
6780
6790
6800
6810
6820
6830
6840
6850
6860
6870
6880
6890
6900
6910
6920
6930
6940
6950
6960
6970
Sq.
Cube
root
root
80.31
18 61
80.37
18 62
80.44
18 63
80.50
18 64
80.56
18.65
80.62
18.66
80. 68
18.67
80. 75
18.68
80.81
18.69
80.87
18.70
80.93
18.71
80.99
18.72
81.06
18.73
81.12
18.74
81.18
18.7s
81.24
18.76
81.30
18.77
81.36
18.78
81.42
18.79
81.49
18.80
81.55
18.81
81.61
18.81
81.67
18.82
81.73
18.83
81.79
18.84
81.85
18.8s
81.91
18.86
81.98
18.87
82.04
18.88
82.10
18.89
82.16
18.90
82.22
18.91
82.28
18.92
82.34
18.93
82.40
18.94
82.46
18.95
82.52
18.95
82.58
18.96
82.64
18.97
82.70
18.98
82.76
18.99
82.83
19
82.89
19.01
82.95
19.02
83.01
19.03
83.07
19.04
83.13
19.0s
83.19
19.06
83.25
19.07
83.31
19.07
83.37
19.08
83 43
19.09
83.49
19.10
No.
6980
6990
7000
7010
7020
70.50
7040
7050
7060
7070
7080
7090
7100
71 10
7120
7130
7140
7150
7160
7170
7180
7190
7200
7210
7220
7230
7240
7250
7260
7270
7280
7290
7300
7310
7320
7330
7340
73SO
7360
7370
7380
7390
7400
7410
7420
7430
7440
7450
7460
7470
7480
7490
7SOO
Sq.
root
Cube
root
83. SS
83.61
83.67
83 .73
83.79
83.85
83 90
83.96
84.02
84.08
84.14
84.20
84.26
84.32
84.38
84.44
84.50
84.56
84.62
84.68
84.73
84.79
84.85
84.91J
84.97
85.03'
85.09!
85.15;
85.21]
85.26;
85.32]
85.38'
85.44
85.S0I
85.56]
85.62
85.67
85.73
85.79J
85. 85 I
85.911
85.97
86.02
86.08
86.14
86.20
86.29
86.31
86.37
86.43
86.49
86.54
86.60
No.
7SIO
7S»
7S*>
7540
7SSO
7S6o
7S70
7580
759°
7600
7610
7620
7630
7640
7650
7660
7670
7680
7690
7700
7710
7720
7730
7740
7750
7760
7770
7780
7790
7800
7810
7820
7830
7840
7850
7860
7870
7880
7890
7900
7910
7920
7930
7940
7950
7960
7970
7980
7990
8000
8010
8020
8030
Sq.
root
Cube
root
86.66
86.7a
86.78
86 83
86 89
869s
87.01
87.06
87.12
87.18
87.24
87.29
87.3s
87.41
87.46
87. S2
87.58
87.64
87.69
87.7s
87.81
87.86
87 92
87.98
88.03
88.09
88. IS
88.20
88.26
88.32
88.37
88.43
88.49
88.S4
88.60
88.66
88.71
88.77
88.83
88.88
88.94
88.99
89.0s
89.11
89.16
89.22
89.27
89 33
89 39
89.44
89. SO
89.55
89.61
Table of Square Roots and Cube Roots
6i
Table of Square Roots and Cube Roots of Numbers from
looo TO 10,000 — {Continued)
No.
Sq.
root
Cube
root
No.
Sq.
root
Cube
root
No.
Sq.
root
Cube
root
No.
Sq.
root
Cube
root
8040
89.67
20.03
8540
92.41
20.44
9040
95.08
20.83
9540
97.67
21.21
80S0
89
72
20.04
8550
92
47
20. 45
9050
95
14
20.84
9S50
97
72
21.22
8060
89
78
20.05
8560
92
52
20.46
9060
95
18
20.85
9560
97
78
21.22
8070
89
83
20.06
8570
92
57
20.46
9070
95
24
20.8s
9S70
97
83
21.23
8080
89
89
20.07
8580
92
63
20.47
9080
95
29
20.86
9580
97
88
21.24
8090
89
94
20.07
8590
92
68
20.48
9090
95
34
20,87
9590
97
93
21.25
8100
90
20.08
8600
92
74
20.49
9100
95
39
20.88
9600
97
98
21.25
81 10
90
06
20.09
8610
92
79
20.50
91 10
95
45
20.89
9610
98
03
21.26
8120
90
II
20.10
8620
92
84
20.50
9120
95
50
20.89
9620
98
08
21.27
8130
90
17
20.11
8630
92
90
20.51
9130
95
55
20.90
9630
98
13
21.28
8140
90
22
20.12
8640
92
95
20.52
9140
95
60
20.91
9640
98
18
21.28
8150
90
28
20.12
8650
93
01
20.53
9150
95
66
20.92
9650
98
23
21.29
8l6o
90
33
20.13
8660
93
06
20.54
9160
95
71
20.92
9660
98
29
21.30
8170
90
39
20.14
8670
93
II
20.54
9170
95
76
20.93
9670
98
34
21.30
8l8o
90
44
20.15
8680
93
17
20. 55
9180
95
81
20.94
9680
98
39
21.31
8190
90
SO
20.16
8690
93
22
20.56
9190
95
86
20.95
9690
98
44
21.32
8200
90
55
20.17
8700
93
27
20.57
9200
95
92
20.95
9700
98
49
21.33
8210
90
61
20.17
8710
93
33
20.57
9210
95
97
20.96
9710
98
54
21.33
8220
90
66
20.18
8720
93
38
20.58
9220
96
02
20.97
9720
98
59
21.34
8230
90
72
20.19
8730
93
43
20.59
9230
96
07
20.98
9730
98
64
21.3s
8240
90
77
20.20
8740
93
49
20.60
9240
96
12
20.98
9740
98
69
21.36
8250
90
83
20.21
8750
93
54
20.61
9250
96
18
20.99
9750
98
74
21.36
8260
90
88
20.21
8760
93
59
20.61
9260
96
23
21
9760
98
79
21.37
8270
90
94
20.22
8770
93
65
20.62
9270
96
28
21.01
9770
98
84
21.38
8280
90
99
20.23
8780
93
70
20.63
9280
96
33
21.01
9780
98
89
21.39
8290
91
OS
20.24
8790
93
75
20.64
9290
96
38
21.02
9790
98
94
21.39
8300
91
10
20.25
8800
93
81
20.65
9300
96
44
21.03
9800
98
99
21.40
8310
91
16
20.26
8810
93
86
20.65
9310
96
49
21.04
9810
99
05
21.41
8320
91
21
20.26
8820
93
91
20.66
9320
96
54
21.04
9820
99
10
21.41
8330
91
27
20.27
8830
93
97
20.67
9330
96
59
21.05
9830
99
IS
21.42
8340
91
32
20.28
8840
94
02
20.68
9340
96
64
21.06
9840
99
20
21.43
8350
91
38
20.29
8850
94
07
20.68
9350
96
70
21.07
9850
99
25
21.44
8360
91
43
20.30
8860
94
13
20.69
9360
96
75
21.07
9860
99
30
21.44
8370
91
49
20.30
8870
94
18
20.70
9370
96
80
21.08
9870
99
35
21.45
8380
91
54
20.31
8880
94
23
20.71
9380
96
85
21.09
9880
99
40
21.46
8390
91
60
20.32
8890
94
29
20.72
9390
96
90
21.10
9890
99
45
21.47
8400
91
6S
20.33
8900
94
34
20.72
9400
96
95
21.10
9900
99
50
21.47
8410
91
71
20.34
8910
94
39
20.73
9410
97
01
21. II
9910
99
55
21.48
8420
91
76
20.34
8920
94
45
20.74
9420
97
06
21.12
9920
99
60
21.49
8430
91
82
20. 35
8930
94
50
20.75
9430
97
II
21.13
9930
99
65
21.49
8440
91
87
20.36
8940
94
55
20.75
9440
97
16
21.13
9940
99
70
21.50
8450
91
92
20.37
8950
94
60
20.76
9450
97
21
21.14
9950
99
75
21.51
8460
91
98
20.38
8960
94
66
20.77
9460
97
26
21.15
9960
99
80
21.52
8470
92
03
20.38
8970
94
71
20.78
9470
97
31
21.16
9970
99
85
21.52
8480
92
09
20.39
8980
94
76
20.79
9480
97
37
21.16
9980
99 90
21.53
8490
92
14
20.40
8990
94
82
20.79
9490
97
42
21.17
9990
99-95
21.54
8500
92
20
20.41
9000
94
87
20. So
9500
97
47
21.18
lOOOO
100 1
21.54
8510
92
25
20.42
9010
94
92
20.81
9SIO
97
52
21.19
8520
92
30
20.42
9020
94
97
20.82
9520
97
57
21.19
8530
92
36
20.43
9030
95
03
20.82
9S30
97
62
21.20
'>2 iMalhciiKilicil I'aliles
To find Square or Cube Roots of large numbers not con-
tained in the column of numbers of the table
Sinli routs may sDniclimcs Ijc taken at. ontc from llic taljlc, by mtrtly
rcf^ardin^ ihc columns of |K)\vers as bfing columns of numbers; and tliosc
of numljcrs as bein^ those of roots. Thus, if ihe si/iiiirc root of 25281
is required, first find thai number in the column of squares; and opix>silc
to it, in the column of numbers, is its square root 159. For the cube root
of 857375, find that number in the column of cubes; and opposite to it,
ill the column of numbers, is its cube root 95. When the exact number
is not contained in the column of squares, or cubes, as the case may be,
\vc may use instead the number nearest to it, if no great accuracy is
required. But when a considerable degree of accuracy is necessary, the
following very correct methods ma>' be used.
For the square root
This rule applies both to whole numbers and to those which are parlly
(not wholly) decimal. First, in the foregoing manner, take out the
tabular nunil)cr, wliich is nearest to the gi\-en one; and also its tabular
square root. Multiply this tabular numl)cr b}' 3; to the product add
the given number. Call the sum A. Then multiply the given number
l)y 3; to the product add the tabular number. Call the sum />. Then
A : B :: Tabular root : Required root.
Example. — Let the given number be 946.53. Here we find the nearest
tabular number to be 947; and its tabular square root 30.7734. Hence,
947 = tabular numl)cr
3
2841
946.53 = given number
3787-53 = -•!•
and
94*'^-53 = given number
3
2839-59
947 = tabular number
I 3786.59 = B.
A B Tab. root Req'd root
Then 3787-53 : 3786.59 :: 30-7734 : 30-7657+-
The root as found by actual matliematical process is also 30.76574-.
For the cube root
This rule api)lics lioth to wiiole nunil)crs and to those whicli are parlly
decimal. First take out the tabular number which is nearest to the given
one; and also its tabular cul)e root. ^lultiply this tabular number by
2; and to the product add the given number. Call the siun A. Then
Cube Root
63
multiply the given number by 2; and to the product add the tabular
number. Call the sum B. Then
A : B :: Tabular root : Required root.
Example. — Let the given number be 7368. Here we find the nearest
tabular number (in the column of cubes) to be 6859; and its tabular cube
root 19. Hence,
6859 = tabular number
13718
7368 = given number
21086 = A.
and
7368 = given number
14736
6859 = tabular number
I 21595 = B.
B Tab. root Req'd root
Then 21086 : 21595 " ^9 : I94585.
The root as found by correct mathematical process is 19.4588.
A
21086
64
Mallienuitical Tallies
Areas and Circuukkkknces ok Circles for Diaueteks in
Units and Eiciiths, etc., from ^4« to ioo.
Uiam-
Circum-
Area
Diam-
Circum-
Area
Diam-
Circum-
itLT
ference
eter
2H
ference
elcr
ference
Area
<B4
.049087
.00019
7.068S8
3 9761
S«6
I7.47SI
24.301
•42
.09817s
.00077
c>1.
7 26493
4 2000
H
17 671S
24 850
H«
.147J62
.00173
H
7.46128
4 4.V3I
'M«
17 8678
25 406
M.
.1963S0
.00307
lit
7.65763
46664
H
18 0642
25 967
9)3
.294524
.00690
W
7.85398
4.9087
'»i«
18. 260s
26 S3S
^
.392699
.01227
Wo
8 0S0.33
S-1S72
H
18.4.569
27 109
Ma
.490874
.01917
H
8.2466K
S.411 .
18 6532
27 688
^0
•589049
.02761
'!ir>
« 41P3
567.:
18 8496
28 274
li2
.687223
.03758
^4
8.63938
5 g-v''
19 2423
29 465
M
.785398
.04909
'■dfl
8.83573
6 2126
1 ^*
19.6.V50
JO 680
Wj
.883573
.06213
li
9 03208
6.4918
\ H
ao.0277
31.919
M.
.981748
.07670
'■''is
9 22843
6.7771
' .
20.4204
33 183
>Hj
1.07992
.09281
3
9 42478
7.o«.-
20.8131
34 472
^6
1.17810
.11045
Mo
9 62113
7-3'"-
21.2058
35 78s
'?42
1.27627
.12962
'6
9 81748
7-6699
>H
21.5984
.37 122
?<«
I. 37445
.15033
9io
10.0138
7-9798
7
21.9911
38.48S
'Hi
1.47262
. 17257
M
10.2102
8,2958
yi
22.3838
39 871
)i
1.57080
. 1963.1
v'io
10.406s
8.6179
M
22.776s
41 282
'"^fc
1.66897
.22166
%
10.6029
8 01*^2
H
23.1692
42.718
9i«
1.7671S
.24850
?i»
10.7992
'•J
23 5619
44 179
>%•.■
1.86532
.27688
!i
10.9956
■4
23 9546
45664
H
1.96350
.30680
?lo
11.1919
■'•4
24 3473
47 173
2J.42
2.06167
.33824
56
11.3683
10.321
yi
24.7400
48.707
«H«
2.15984
.37122
'Ho
11.5846
10.680
8
25.1327
50.265
2^2
2.25802
.40574
?1
I I. 7810
1I.04S
W
25 5254
51 849
^4
2. 35619
.44179
'?i6
11 9773
11.416
M
25.9'8i
S3 4S6
*542
2.454.37
.47937
H
12.1737
11-793
94
26 3108
SS .088
'^6
2.55254
.51849
'■?io
12.3700
12.177
W
26.703s
56.745
"/42
2.65072
.55914
4
12.5664
12.566
94
27.0962
S8.426
%
2.74889
.60132
'io
12.7627
12.962
•M
27.4889
60.132
»H2
2.84707
.64504
'H
12.9591
13 364
;8
27.8816
61.862
'^fl
2.94524
.69029
r»s
13 1554
13.772
9
28.2743
63 617
3)42
3.04342
.73708
H
13.3518
14.186
%
28.6670
65.397
I
3.14159
.78540
5ia
13.5481
14.607
li
290597
67.201
Mfl
3 33794
.88664
H
13-7445
15 0.33
9s
29.4524
69 039
!-4
3 53429
.99402
1U
13.9408
15466
^4
29 8451
70.882
?(«
3 7,?o64
I . 1075
H
14.1372
IS 904
H
30 2378
72.760
U
3.92699
I . 2272
?1a
14.3335
16.349
94
30.6305
74662
''10
4.12334
1.3530
5(i
14-5299
16.800
'A
31.0232
76589
■'4
4.31969
1.4849
"16
14.7262
17.257 1
10
31.4159
78.540
^io
4.S1604
1.6230
•M
14.9226
17.721 '
H
31.8086
80.SI6
^^
4-712.39
1.7671
';'ifl
15-1189
18'. 190
M
32.2013
82.516
»io
4.90874
1.9175
H
IS.3153
18.665
96
32.5940
84 -541
H
5.10509
2.07.39
'Mo
15.5116.
19 147
H
32.9867
86.590
'!i»
5.30144
2.236s
S
IS.70S0
19 63s
96
33 3794
88.664
^4
5.49779
2.4053
Mo
15.9043
20.129
94
33 7721
90.763
'^i8
S. 69414
2.5802
H
16.1007
20.629
li
34.1648
92.886
^/6
5.89049
2.7612
9io
16.2970
21. 135
II
34.5575
95 033
'Mo
6.08684
2.9483
M
l6.49.i4
21.648
H
34 9.502
97.20s
2
6.28319
3.1416
■Mo
16.6897
22.166
M
35.3429
99.402
H»
6.47953
3.3410
H
l6.885l
22.691
96
35-7356
101.62
^
6.67588
3 5466
■/i«
17.0824
23.221
W
36.1283 103.87
^0
6.87223
3.7583
!'i
17.2788
23 758
H
36.5210 106.14
Areas and Circumferences of Circles
6S
Areas and Circxjmterences of Circles for Diameters in
Units and Eighths, etc. — {Continued)
Diam-
Circum-
Area
Diam-
Circum-
Area
Diam-
Circum-
Area
eter
ference
eter
ference
eter
ference
iiH
36.9137
108.43
l8?i
57-7268
265.18
25
78.5398
490-87
'A
37.3064
no. 75
Vi
58.1195
268.80
A
78-9323
495.79
12
37.6991
113. 10
5i
58-5122
272.45
Vi
79.3252
500.74
H
38.0918
115.47
Vi
58.9049
276.12
■H
79.7179
50s. 71
M
38.484s
117.86
li
59 2976
279.81
A
80.1106
510.71
%
38.8772
120.28
19
59-6903
283.53
H
80.5033
515.72
H
39.2699
122.72
H
60.0830
287.27
%
80.8960
520.77
•>i
39.6626
125.19
M
60.4757
291.04
A
81.2887
525-84
H
40.0553
127.68
5i
60.8684
294.83
26
81.6814
530.93
T^
40.4480
130.19
Vi
61.2611
298.65
A
82.0741
536.0s
13
40.8407
132.73
%
61.6538
302.49
H
82.4668
541-19
H
41.2334
133.30
H
62.0465
306.35
%
82.8595
546.35
Vi
41.6261
137.89
'A
62.4392
310-24
A
83.2522
551-55
%
42.0188
140.50
20
62.8319
314.- 16
H
83.6449
556.76
'/^
42.411S
143.14
A
63.2246
318.10
H
84.0376
562.00
%
42.8042
143.80
M
63.6173
322.06
A
84.4303
567.27
?4
43.1969
148.49
%
64.0100
326.05
27
84.8230
572.56
'A
43.5896
151 . 20
M
64 . 4026
330.06
A
85.2157
577.87
14
43.9823
153.94
%
64.7953
334.10
H
85.6084
583.21
W
44.37SO
156.70
94
6S-1880
338.16
H
86.0011
588.57
Vi
44.7677
159.48
Ji
65-5807
342.2s
A
86.3938
593 96
H
4S.1604
162.30
21
65-9734
346.36
^A
86.7865
599.37
H
4S.5S3I
165.13
A
66.3661
350.50
%
87.1792
604.81
H
4S.94S8
167.99
\i
66.7588
354.66
A
87.5719
610.27
Vi
46.338s
170.87
H
67.151S
358.84
28
87.9646
615-75
•A
46.7312
173.78
\'i
67.5442
363.05
A
88.3573
621.26
IS
47.1239
176.71
H
67-9369
367.28
H
88.7500
626.80
H
47.S166
179.67
%
68.3296
371.54
H
89.1427
632.36
H
47-9093
182.6s
'A
68.7223
375.83
A
89-5354
637-94
%
48.3020
185-66
22
69.1150
380.13
H
89.9281
643-55
^
48.6947
188.69
A
69.5077
384.46
%
90.3208
649 18
^6
49-0874
191-75
M
69.9004
388.82
A
90.713s
654.84
%
49-4801
194.83
?i
70.2931
393-20
29
91 . 1062
660.52
-A
49.8728
197-93
y2
70.6858
397-61
A
91.4989
666.23
16
50.2655
201.06
A
71.0785
402.04
H
91.8916
671.96
H
50.6582
204.22
%
71.4712
406.49
H
92.2843
677.71
W
51-0509
207.39
A
71-8639
410.97
A
92.6770
683.49
?i
51.4436
210.60
23
72.2566
415-48
H
93-0697
689.30
'/i
51.8363
213.82
A
72.6493
420.00
?4
93-4624
695.13
5/i
52.2290
217.08
H
73.0420
424.56
A
93-8551
700.98
%
52.6217
220.3s
%
73.4347
429.13
30
94.2478
706.86
?6
53.0144
223.65
A
73-8274
433-74
A
94.6405
712.76
17
53.4071
226.98
A
74.2261
438.36
A
95-0332
718.69
A
53-7998
230.33
U
74-6128
443 01
3i
95-4259
724.64
H
54-1925
233.71
A
75.005s
447.69
A
95 -8186
730.62
^
54-5852
237.10
24
75.3982
452.39
^A
96.2113
736.62
H
54-9779
240.53
A
75-7909
457.11
H
96.6040
742.64
H
55-3706
243.98
Vi
76-1836
461.86
A
96.9967
748.69
M
55-7633
247.45
H
76.5763
466.64
31
97-3894
754-77
5i
56.1560
250-95
A
76.9690
471.44
H
97-7821
760.87
18
56.5487
254-47
H
77.3617
476-26
H
98.1748
766.99
V6
56.9414
258.02
H
77-7544
481. II
H
98.567s
773- 14
H
57-3341
261.59
A
78.1471
485.98
A
98.9602
779-31
60
Malhcm.ilic;il T.ildes
ArF.AS and CiRClTMFERKNCKS OF CIRCLES FOR DIAMETERS IN
Units and Kichtus, etc. — {Continued)
Diam-
Circuit
IJiam-
Circum-
Area
Diam-
Circum-
Area
cUt
fcrcnu.
ctcr
ference
eter
ference
31H
99 3S29
785.51
H
120.166
"49 I
aaH
140.979
1581.6
94
99 7456
791 73
H
120 559
1156.6
4S
141
372
1590
4
Th
100 1.38
797 98
W
120.951
1164.3
M
141
764
1599
3
32
100 531
804.2s
H
121.344
"71. 7
M
142
157
i6og
3
H
100.924
810 54
94
121.737
"79 3
96
142
SSO
1617
0
U
101.316
816.86
J6
122.129
1186.9
^6
142
942
1626
0
H
loi . 709
823 21
39
122.522
1194.6
96
143
33S
1634
9
H
102.102
829.58
H
122.915
1202.3
94
143
728
1643
9
5i
102.494
83s 97
M
123. yjs
1210.0
H
144
121
1652
9
H
102.887
842.39
96
123 700
1217.7
46
144
S13
1661
9
%
103.280
848.83
H
124.093
1225.4
H
144
906
1670
9
33
103 673
855.30
96
124 486
1233.2
M
145
299
1680
0
H
10.J.065
861.79
94
124.878
1241.0
96
I4S
691
1689
I
y*
104.458
868.31
Zi.
125.271
1248 8
W
146
084
1698
3
96
104.851
874.85
40
12s 664
1256.6
96
146
477
1707
4
H
105.243
881.41
H
126 056
1264.5
94
146
869
1716
5
fi
105.636
888.00
H
126 449
1272.4
"^6
147
262
1725
7
94
106.029
894.62
96
126.842
1280 3
47
147
65s
1734
9
^
106.421
901.26
V6
127.235
1288.2
H
148
048
1744
3
34
106.814
907.92
96
127.627
1296.2
H
148
440
1753
S
H
107 . 207
914-61
94
128 020
1304.2
96
148 833
1762
7
y*
107.600
921.32
H
128.413
1312.2
'/4
149 226
1772
I
96
107.992
928.06
41
128. 80s
1320.3
H
149 618
1781
4
H
108.385
934-82
H
129.198
1328.3
94
150.011
1790
8
96
10S.778
941-61
H
129.591
1336.4
J6
150.404
1800
I
94
103.170
948-42
96
129.983
1344-S
48
ISO 796
1809
6
•yi
109.563
955-25
H
130.376
1352.7
W
ISI 189
1819
0
35
109.956
962.11
96
130.769
1360.8
H
151 582
1828
S
^6
no. 348
969-00
94
131. 161
1369 0
96
151 975
1837
9
K4
no. 741
975-91
li
131 554
1377.2
H
152 367
1847
S
96
III. 134
982.84
42
131 947
1385.4
96
152 760
1857
0
H
111.527
989.80
^6
132.340
1393 7
94
153 153
1866
s
96
111.919
996.78
H
132.732
1402.0
J6
153 545
1876
I
94
112.312
1003.8
96
133 125
1410.3
49
153 938
18S5
7
^
112.705
1010.8
\i
133 -Si8
1418.6
H
154.331
189s
4
36
113.097
1017-9
96
I33-9IO
1427.0
y*
154-723
190S
0
H
113.490
1025.0
94
134-303
1435 4
96
ISS "6
1914
7
H
113.883
1032.1
?6
134-696
1443 8
H
155-509
1924
4
96
114.275
1039.2
43
135 088
1452.2
96
155 902
f934
3
«
114.668
1046.3
H
135-481
1460.7
94
156.294
1943
9
96
115 061
IOS3-S
H
135-874
1469.1
J6
156.687
1953
7
94
115.454
1060.7
96
136-267
1477.6
so
157 080
1963
S
J6
US 846
1068.0
H
136.659
1486.2
H
157 472
1973
3
37
1 16. 2,39
1075.2
96
I37-OS2
1494.7
M
IS7 86s
1983
3
H
116 632
1082.5
94
137-445
1503.3
^8
158 258
1993
I
M
117 024
1089.8
J6
137 837
15". 9
!4
158.650
2003
0
96
117.417
1097. I
44
138 230
1520.5
96
159 043
2012
9
H
117.810
II04.5
V6
138 623
1529-2
94
159 436
2022
8
96
118 202
nil. 8
H
139 ois
1537-9
//6
159 829
2032
8
94
118.596
1119.2
96
139 408
1546.6
SI
160.221
2042
8
J6
118.988
1126.7
H
139 801
I55S-3
M
160 614
2052
8
38
119 381
"34-1
96
140.194
1564 0
y*
161.007
2062
9
yi
119-773
1141 6
94
140 586
1572-8
96
161.399
3073.O
Areas and Circumferences of Circles
67
Areas and Circumferences of Circles for Diameters in
Units and Eighths, etc — {Continued)
Diam-
Circum-
Area
Diam-
Circum-
Area
Diam-
Circum-
Area
eter
ference
eter
ference
eter
ference
Si!-^
161.792
2083.1
58'/^
182.605
2653.5
64?i
203.418
3292.8
H
162.185
2093.2
w
182.998
2664.9
%
203.811
3305.6
%
162.577
2103.3
3^
183.390
2676.4
65
204 . 204
3318 3
?i
162 970
2113 5
1 2
183.783
2687.8
M
204 596
3331 I
52
163 363
2123.7
5^
184 . 176
2699.3
H
204.989
3343.9
M
163.756
2133 9
H
184.569
2710.9
H
205.382
3356 7
H
164.148
2144,2
k
184.961
2722.4
H
205.774
3369 6
?i
164 541
2154-5
59
185.354
2734.0
H
206.167
3382.4
^^
164 934
2164.8
M
185.747
2745.6
H
206 . 560
3395 3
5i
i6s 326
2I7S.I
U
186.139
2757.2
I'i
206 . 952
3408.2
H
165.719
2185.4
%
186.532
2768.8
66
207.345
3421.2
li
166. 112
219s -8
H
186.925
2780.5
H
207.738
3434.2
53
166 504
2206.2
%
187.317
2792.2
H
208.131
3447.2
H
166 897
2216.6
Vi
187.710
2803.9
H
208.523
3460.2
H
167.290
2227.0
^/i
188.103
281S.7
\i
208.916
3473.3
%
167.683
2237-5
60
188.496
2827.4
5i
209.309
3486.3
54
168.075
2248.0
H
188.888
2839.2
%
209.701
3499-4
^i
168.468
2258.5
H
189.281
2851.0
'yi
210.094
3512. S
H
168.861
2269.1
?i
189.674
2862.9
67
210.487
3525.7
^
169.253
2279.6
I'i
190.066
2874.8
H
210.879
3538.8
54
169.646
2290.2
H
190.459
2886.6
H
211.272
3552. 0
Iri
170.039
2300.8
%
190.852
2898.6
H
211.665
3565.2
H
170.431
2311.5
li
191.244
2910.5
H
212.058
3578. S
H
170.824
2322.1
61
191.637
2922.5
H
212.450
3591. 7
H
171. 217
2332.8
H
192.030
2934.5
%
212.843
3605.0
%
171.609
2343 5
U
192.423
2946. 5
%
213.236
3618.3
%
172.002
2354. 3
H
192. 81S
2958.5
68
213.628
3631.7
%
172.395
2365.0
H
193.208
2970.6
H
214.021
3645.0
55
172.788
2375.8
H
193.601
2982.7
w
214.414
3658.4
H
173.180
2386.6
H
193.993
2994.8
H
214.806
3671.8
H
173-573
2397.5
~A
194.386
3006.9
\i
215.199
3685.3
H
173.966
2408.3
62
194.779
3019. I
H
215.592
3698.7
Vi
174.358
2419.2
H
195. 171
3031.3
H
215.984
3712.2
^
174.751
2430.1
M
195.564
3043.5
%
216.377
3725.7
H
175.144
2441. 1
%
195-957
3055.7
69
216.770
3739.3
■'A
175.536
2452 0
\i
196.350
3068.0
M
217.163
3752.8
56
175.929
2463.0
^A
196.742
3080.3
M
217.555
3766.4
H
176.322
2474.0
H
197.13s
3092.6
^i
217.948
3780.0
H
176.715
2485.0
li
197.528
3104.9
^^
218.341
3793.7
H
177.107
2496.1
63
197.920
3117.2
H
218.733
3807.3
H
177. Soo
2507.2
H
198.313
3129.6
?4
219.126
3821.0
5i
177.893
2518.3
H
198.706
3142.0
'A
219.519
3834.7
H
178.285
2529.4
%
199.098 ■
3154.5
70
219.911
3848. 5
li
178.678
2540.6
Vi
199.491
3166.9
'/i
220.304
3862.2
57
179 071
2551. 8
r&
199.884
3179.4
M
220.697
3876.0
H
179.463
2563.0
H
200.277
3191.9
H
221.090
3889.8
H
179.856
2574.2
li
200.669
3204.4
'A
221.482
3903.6
%
180.249
2585.4
64
201.062
3217.0
^A
221.875
3917. S
V^
180.642
2596.7
H
201.455
3229.6
¥i
222 . 268
3931.4
H
181 .034
2608.0
H
201.847
3242.2
%
222 . 660
394S.3
?4
181.427
2619.4
H
202.240
3254.8
71
223.053
3959.2
H
181.820
2630.7
Vi
202.633
3267.5
A
223.446
3973.1
58
182.212
2642 . I
•>6
203.025
3280.1
Vi
223.838
3987.1
68
Mullu'malii;il Tables
Areas and Circumferences of Circles for Diaueters in
Units and Kighths, etc. — {Conlimud)
Diam-
Circum-
Area
Diam-
Circum-
Area
Diam-
Circum-
elor
ference
eter
ference
eter
ference
Areft
7iH
224.231
4001. I
78
245 044
4778 4
84H
265.857
5634.5
W
224.624
4015.2
^6
245 437
4793.7
?4
266.350
5641 2
94
22S.OI7
4029.2
H
245 830
4809 0
56
266.643
56.57.8
94
225 409
4043.3
H
246 222
4824.4
85
267.03s
5674 5
J6
225.802
4057.4
M
246.615
4839 .8
H
367.438
S691 3
7a
226.195
4071.5
56
247.008
4855.2
5i
367.831
5707 9
^6
226.587
4085.7
94
247 400
4870.7
96
368 213
5724 7
\i
226.980
4099 8
J6
247.793
4886.2
H
368 606
5741 5
9*
227.373
4114 0
79
248.186
4901.7
96
268.999
5758 3
W
227.76s
4128.2
H
248.579
4917.2
94
269.393
5775.1
H
228.158
4142.5
y*
248.971
4932.7
56
269.784
579« 9
94
228.551
4156.8
H
249 364
4948.3
86
270.177
5808.8
Ji
228.944
4171 1
M
249-757
4963.9
H
270 570
582s 7
73
229.336
4185.4
•?6
250.149
4979.5
y*
270.962
58.J2 6
'/6
229.729
4199 7
94
250.542
4995.2
H
271.355
5859 6
H
230.122
4214. I
56
250.935
5010.9
H
271.748
5876 5
%
230. SI4
4228,5
80
251 327
5026. 5
96
272.140
5893 5
Vi
230.907
4242.9
^6
251.720
S042.3
94
272.533
59«o 6
56
231.300
4257.4
H
252.113
5058.0
56
272.926
5927 6
94
231.692
4271.8
96
252.506
5073-8
87
273 319
5944 7
56
232.08s
4286.3
H
252.898
5089.6
56
273.711
5961 8
74
232.478
4300.8
96
253.291
S105.4
y*
274.104
5978.9
yi
232.871
4315.4
94
253.684
5121.2
96
274.497
5996.0
M
233 263
4329.9
56
254.076
5137. I
H
274.889
6013 2
9i
233.656
4344.5
8l
254.469
5153- 0
96
275.282
6030.4
^
234.049
4359.2
56
254.862
S168.9
94
275.675
6047.6
96
234 441
4373 8
54
255.254
S184.9
56
276.067
6064.9
94
234.834
4388.5
96
255.647
5200.8
88
276.460
6082 I
J6
235.227
4403.1
^
256.040
5216.8
56
276.853
6099.4
75
235.619
4417.9
H
256.433
5232.8
H
277.246
6116.7
>6
236.012
4432.6
54
256.825
5248.9
96
277-638
6134-I
M
236.40s
4447.4
",
2=57.218
5264.9
H
278.031
615I-4
96
236.798
4462.2
S7.611
5281.0
96
278.424
6168.8
!^
237.190
4477.0
..-,8.003
5297.1
H
278.816
6186.2
96
237.583
4491.8
■ 1
258.396
5313-3
56
279-209
6203-7
94
237.976
4506.7
H
258.789
5329.4
89
279.602
6221 . I
T6
238.368
4S2I.S
}4
259.181
5345.6
H
279.994
6238 6
76
238.761
4536. 5
H
259 574
5361.8
H
280.387
6256.1
!^
239 154
4SSI.4
?4
259.967
5378 -I
96
280.780
6273 7
5-4
239.546
4566.4
56
260.359
5394-3
H
281.173
6291.2
96
239-939
4581.3
83
260.752
5410.6
56
281.565
6308.8
«
240.332
4596.3
56
261 . 145
5426.9
94
281.958
6326.4
96
240.725
4611.4
'4
261.538
5443-3
56
282.351
6344. 1
94
241. 117
4626.4
1 H
261.930
5459-6
90
282.743
6361 . 7
56
241. Sio
4641.5
M'
262.323
5476.0
56
283.136
6379 4
77
241.903
4656.6
'•i
262.716
5492-4
54
283.529
6397.1
M
242.29s
4671.8 1
•?4
263.108
5508.8
96
283.921
6414.9
H
242.688
4686.9
56
263.501
5525-3
5i
284.314
6432.6
96
243081
4702.1
84
263.894
5541-8
96
284.707
6450.4
H
243.473
4717.3
56
264.286
5558.3
94
285.100
6468.2
96
243.866
4732.5
n
264.679
5574.8
56
285.492
6486.0
94
244.259
4747.8
H
265.072
5591 4
91
285.885
6503.9
56
244.652
4763.1 1
54
265.465
5607.9
56
286.278
6521.8
Areas and Circumferences of Circles
69
Areas and Circumferences of Circles for*Diameters in
Units and Eighths, etc. — {Concluded)
Diam-
eter
91 54
Circum-
ference
286 . 670
287.063
287.456
287.848
288.241
288.634
289.027
289.419
289.812
290.205
290.597
290.990
291.383
291.775
292 . 168
292 . 561
292.954
293 346
293 -739
294.132
294.524
294.917
295 -310
295.702
Area
6539.7
6557.6
6575.5
6593.5
6611.5
6629.6
6647.6
6665.7
6683.8
6701.9
6720.1
6738.2
6756.4
6774.7
6792.9
6811.2
6829.5
6847.8
6866.1
6884.5
6902.9
6921.3
6939.8
6958.2
Diam-
eter
94'/4
96
Circum.
ference
296.095
296.488
296.881
297.273
297 . 666
298.059
298.451
298.844
299 .237
299.629
300.022
300. 41S
300.807
301 . 200
301.593
301.986
302.378
302.771
303.164
303.556
303.949
304 -342
304.734
305.127
Area
6976.7
6995.3
7013 8
7032.4
7051.0
7069 . 6
7088.2
7106.9
7125.6
7144.3
7163.0
7181.8
7200.6
7219.4
7238.2
7257.1
7276.0
7294.9
7313.8
7332.8
7351.8
7370.8
7389.8
7408.9
Diam-
Circum-
eter
ference
97W
305.520
H
305.913
H
306.305
%
306.698
H
307.091
I'i
307.483
98
307.876
yi
308.269
H
308.661
%
309 054
Vi
309.447
%
309.840
?i
310.232
■A
310.625
99
311. 018
M
311. 410
H
311.803
H
312.196
H
312.588
54
312.981
?i
313.374
5i
313.767
100
314.159
Area
7428.0
7447.1
7466.2
7485.3
7504. S
7523.7
7543.0
7562.2
7581. 5
7600.8
7620.1
7639.5
7658.9
7678.3
7697.7
7717. I
7736.6
7756.1
7775.6
7795.2
7814.8
7834.4
7854.0
70
Mathematical TaMcs
Areas and CiRciTMFERENrES of Circles for Diameters
PROM !io TO loo Advancing by Tenths
Diameter
Area
Circumfcrcnccll Diar
netcr
3
Area
Circumference
0 0
S
32.0618
16.6S04
.1
.007854
.31416
4
22.9022
16.9646
.3
.031416
.62832
S
23 7583
17.3788
.3
.070686
.94248
.6
24.6301
17 S929
.4
.12566
1.2566
.7
25.5176
17 9071
.5
.196.JS
1.5708
8
26.4208
18 2313
.6
.2«27.»
1.8850
.9
27 3397
18 5354
.7
.38485
2.1991 6
0
28.2743
18.8496
.8
.50266
2.S133
I
29.2247
19 1637
•9
.63617
2.8274
.2
30.1907
19 4779
l.o
.7854
3.1416
.3
31.172s
19.7920
.1
.9503
3 4558
4
32.1699
20 1062
.3
I.I3IO
3 7699
S
33.1831
30. 4204
3
I 3273
4.0841
6
34.2119
20.734S
• 4
I. 5394
4.3982
7
35.2565
21.0487
.5
1-7671
4.7124
8
36.3168
31 3628
.6
2.0106
S.0265
9
37.3928
21 6770
• 7
2.2698
5.3407 7
0
38.4845
21 9911
.8
2.5447
5.6549
I
39 5919
22.3053
•9
2.8353
5.9690
2
40.7150
22.6195
2.0
3.1416
6.3832
•3
41.8539
22.9336
.1
3.4636
6.5973
4
43.0084
23 2478
.2
3.8013
6.911S
5
44.17S6
23 5619
•3
4.1548
7.2257
6
45.3646
23 8761
• 4
4 5239
7.5398
7
46.5663
24 1903
■5
4.9087
7.8540
8
47.7836
24.5044
.6
5.3093
8.i68i
9
49.0167
24.8186
• 7
5. 7256
8.4823 8
0
50.2655
25.1327
.8
6.IS75
8.7965
I
SI. 5300
25 4469
•9
6.6052
9.1106
2
52.8102
25.7611
3.0
7.0686
9.4248
3
54.1061
26.0752
.1
7.5477
9.7389 .
4
55.4177
26.3894
.3
8.042s
10.0531
5
56.7450
26.703s
• 3
8.S530
10.3673
6
58.0880
27.0177
•4
9.0792
10.6814
7
59.4468
27.3319
.5
9.6211
10.9956
8
60.8212
27.6460
.6
10.1788
11.3097
9
62.2114
27.9602
.7
10.7521
11 6239 9
0
63.6173
28.2743
.8
11.3411
II. 9381
I
65.0388
28.5885
•9
11.9459
12.2522
2
66.4761
28.9027
4.0
12.5664
12.5664
3
67.9291
29.2168
.1
13.2025
12.8805
4
69.3978
29.5310
.2
13.8.S44
13.1947
5
70.8822
29.84SI
.3
14 5220
13.5088
6
72.3823
30.1593
• 4
15 2053
13.8230
7
73.8981
30.4734
.5
15 9043
14.1372
8
75.4296
30.7876
.6
16.6190
14.4513
9
76.9769
31 . IOI8
.7
17.3494
14.7655 10
0
78.5398
31.4159
.8
18.0956
15.0796 j
I
80.1185
31.7301
• 9
18.8574
IS. 3938
2
81.7128
32.0442
so
19.6350
15.7080
3
83.3229
32.3584
.1
20.4282
16.0221 |j
4
84.9487
32.6726
.2
21.2372
i6.,w63 1
5
86.5901
32.9867
Areas and Circumferences of Circles
71
Areas and Circumferences of Circles for Diameters
FROM Mo TO 100 Advancing by Tenths — {Continued)
Diameter
Area
Circumference
Diameter
Area
Circumference
10.6
88.2473
33.3009
15.9
198.5565
49. 9513
.7
89 . 9202
33.6150
16.0
201.0619
50.2655
.8
91.6088
33.9292
.1
203.5831
50.5796
•9
93 3132
34.2434
.2
206.1199
so. 8938
II. 0
95.0332
34.5575
.3
208,6724
51.2080
.1
96.7689
34.8717
.4
211.2407
51 5221
.2
98.5203
35.1858
.5
213.8246
51.8363
• 3
100.287s
35.5000
.6
216.4243
52.1504
.4
102.0703
35.8142
■ 7
219.0397
52.4646
• 5
103.8689
36.1283
.8
221.670S
52 . 7788
.6
10S.6832
36.4425
.9
224.3176
53 0929
.7
107.5132
36.7566
17.0
226.9801
53.4071
.8
109.3588
37.0708
.1
229.6583
53.7212
.9
III. 2202
37.3850
.2
232.3522
54.0354
12.0
113.0973
37.6991
.3
235.0618
54.3496
.1
I 14. 9901
38.0133
.4
237.7871
54 6637
.2
116.8987
38.3274
.5
240.5282
54.9779
.3
118.8229
38.6416
.6
243.2849
55 . 2920
• 4
120.7628
38.9557
.7
246.0574
55.6062
.5
122.7183
39.2699
.8
248.8456
55.9203
.6
124.6898
39.5841
.9
251.6494
56.234s
• 7
126.6769
39.8982
18.0
254.4690
56.5486
.8
128.6796
40.2124
.1
257.3043
56.8628
.9
130.6981
40.5265
.2
260.1553
57.1770
13.0
132.7323
40.8407
.3
263.0220
57.4911
.1
134.7822
41 . 1549
.4
265.9044
57.8053
.2
136.8478
41.4690
.5
268.8025
58.119s
.3
138.9291
41.7832
.6
271.7164
58.4336
• 4
141. 0261
42.0973
■ 7
274.6459
58.7478
.5
143.1388
42.411S
.8
277.5911
59.0619
.6
145.2672
42.7257
■9
280.5521
59.3761
.7
147. 41 14
43.0398
19.0
283.5287
59.6903
.8
149.5712
43-3540
.1
286.52x1
60.0044
•9
151.7468
43.6681
.2
289.5292
60.3186
I4-0
153.9380
43.9823
.3
292.5530
60.6327
.1
156.1450
44.2965
.4
295.592s
60.9469
.2
158.3677
44.6106
.5
298.6477
61.2611
.•3
160.6061
44.9248
.6
301.7186
61.5752
.4
162.8602
45.2389
.7
304.8052
61.8894
•5
i6s . 1300
45.5531
.8
307.9075
62.2035
.6
167.4155
45.8673
.9
311.0255
62.5177
.7
169.7167
46.1814
20.0
314.1593
62.8319
.8
172.0336
46.4956
.1
317.3087 ■
63.1460
•9
174.3662
46.8097
.2
320.4739
63.4602
iS.o
176.7146
47.1239
.3
323.6547
63.7743
.1
179 0786
47.4380
.4
326.8513
64.088s
.2
181.4584
47.7522
.5
330.0636
64.4026
.3
183.8539
48.0664
.6
333.2916
64.7168
.4
186.2650
48.3805
.7
336.5353
65.0310
■ 5
188.6919
48.6947
.8
339.7947
65.3451
.6
191 . 1345
49.0088
•9
343.0698
65.6593
.7
193.5928
49.3230
21.0
346.3606
65.9734
.8
196.0668
49.6372
.1
349.6671
66.2876
72
Muthcmalical Tallies
Areas and Circumferences of Circles for Diameters
FROM Ho Tu loo Advancing by Tenths — (Contimud)
Diameter
Area
Circumference IJiair
cler
5
Area
Circumference
21 .
■■ ' i.s 36
5SX.S4S9
83.3522
.3
350.3^73
06 y I 59
6
sss 7163
83
5664
4
3S9 6809
-67.2301
7
559 902s
83
880s
5
363 OS03
67.5442
8
564.1044
84
1947
6
366 43S4
67.8S84
9
S68 3220
84
S088
7
369 8361
68.1726 ' 27
0
572. 5553
84
8230
8
373 252C
68.4«''7
1
576 8043
85
1372
9
376 6848
68 80V
581.0690
8S
4513
23
o
.^.1327
69.1150
i
585.3494
8s
765s
I
383 S963
69.4292
4
589.6455
86
0796
2
387.0756
69 74.«
5
593 9574
86
.W38
3
390.5707
70.0575
6
598.2849
86
7080
4
394 0814
70.3717
7
602.6282
87
032I
S
397.6078
70.6858
8
606 9871
87
3363
6
401 . 1500
71.0000 1
9
611. 3618
87
6504
7
404 . 7078
71.3142 28
0
615.7522
87
9646
8
408.2814
71.6283
I
620.1582
88
2788
9
411.8707
71.9425
2
624 5800
88
5929
23
o
415.4756
72.2566
3
629 017s
88
9071
I
419.0963
72.5708
4
633.4707
89
3212
.2
422.7327
72.8849
• 5
637 9397
89
5354
.3
426.3848
73.1991
.6
642.4243
89
849s
.4
430.0526
73 5133
• 7
646 . 9246
90
1637
• S
433.7361
73.8274
.8
651.4407
90
4779
.6
437.4354
74.1416
9
655 9724
90
7930
•7
441.1503
74.4557 29
0
660.5199
91
1063
8
444.SR0O
74.7699
.1
665.0830
91
4303
9
44S 'i.-:-;
75.0841
.2
669.6619
91
734S
24
o
452 . .y^.l i
75.3892
■ 3
674 256s
92
0487
I
456.1671
75.7124
4
678.8668
92
3628
2
459 9606
76.0265
5
683.4928
92
6770
3
463.7698
76.3407
6
688.1345
92
991 1
4
467.5947
76.6549
7
692.7919
93
3053
S
471.4352
76.9690
8
697.4650
93
619s
6
475.2916
77.2832 1
9
702.1538
93
9336
7
479 1636
77.5973 1 30
0
706.8583
94
2478
8
483.0513
77. 91 IS
I
711.5786
94
5619
9
486.9547
78.2257
2
716.3145
94
8761
25
o
490.8739
78.5398
3
721 .0662
95
1903
I
494.8087
78.8540
4
725.8336
95
S044
2
498.7592
79.1681
5
730.6167
9S
8186
3
502,7255
79 4823
6
735.4154
96
1327
4
506.7075
79.7965
7
740.2299
96
4469
S
510.7052
80.1106
8
745.0601
96
761 1
6
514.7185
80.4248
9
749 9060
97
0752
7
518.7476
80.7389 ; 31
0
754 7676
97
3894
8
522.7924
81.0531
I
759 6450
97
703S
9
526.8529
81.3672
2
764..^38o
98
0177
26
o
530.9292
81.6814
3
769.4467
98
3319
I
535.0211
81.9956
4
774.3712
98
6460
2
539.1287
82.3097
5
779-3113
98
9602
3
543.2521
82.6239
6
784.2672
99
2743
4
547-39"
82.9380
7
789.2388
99
S88s
Areas and Circumferences of Circles
73
Areas and Circumferences of Circles for Diameters
FROM Ho TO loo Advancing by Tenths — {Continued)
Diameter
Area
Circumference Diair
leter
Area
Circumference
. 31.8
794 2260
99.9026 37
I
1081.0299
116.5531
9
799-2290
100.2168
2
1086.8654
116.8672
32
o
804.2477
100.5310
3
1092 . 7166
117.1814
I
809.2821
100.8451
4
1098.5835
117.4956
2
814 3322
101 . 1593
5
I 104. 4662
117.8097
3
819.3980
101.4734
6
I no. 3645
118.1239
4
824.4796
101.7876
7
1116.2786
118.4380
S
829.3768
102.1018
8
1122.2083
118.7522
6
834.6898
102.4159
9
1128. 1538
119.0664
7
839.8185
102.7301 38
0
1134.1149
119.3805
8
844 . 9628
103.0442
I
1140.0918
119.6947
9
850.1229
103.3584
2
1146.0844
120 0088
33
o
855.2986
103.6726
3
1152.0927
120.3230
I
860.4902
103.9867
4
I 158. 1167
120.6372
2
865.6973
104.3009
5
1164.1564
120.9313
3
870 , 9202
104 . 6150
6
1170.2118
121.2653
4
876.1588
104.9292
7
I I 76. 2830
121.5796
5
881.4131
105 . 2434
8
1182.3698
121.8938
6
886 6831
105.5575
9
1188.4724
122 . 2080
7
891.9688
105.8717 39
0
1194.5906
122.5221
8
897.2703
106.1838
I
1200.7246
122.8363
9
902.5874
106 . 5000
2
1206.8742
123. 1504
34
o
907 . 9203
106.8142
3
1213.0396
123.4646
I
913.2688
107.1283
4
1219.2207
123.7788
2
918.6331
107 . 4425
5
1225. 4175
124.0929
3
924.0131
107 . 7566
6
1231.6300
124.4071
4
929.4088
108.0708
7
1237.8382
124.7212
5
934.8202
108 , 3849
8
1244. 1021
125.0354
6
940.2473
108 . 6991
9
1250.3617
125.3495
7
945.6901
109.0133 40
0
1256.6371
125.6637
8
951 . i486
109.3274
I
1262.9281
125.9779
9
956.6228
109.6416
2
1269.2348
126.2920
3S
o
962.1128
109.9557
3
1275.5573
126.6062
1
967 . 6184
110.2699
4
1281.8955
126.9203
2
973.1397
110.5841
5
1288.2493
127.2345
3
978.6768
110.8982
6
1294.6189
127.5487
4
984 . 2296
111.2124
7
1301.0042
127.8628
S
989.7980
111.5265
8
1307.4052
128.1770
6
995 3822
111.8407
9
1313.8219
128.4911
7
1000. 9821
112.1349 41
0
1320.2543
128.8053
8
1006.5977
112.4690
I
1326.7024
129.1195
9
1012.2290
112.7832
2
1333. 1663
129.4336
36
o
1017.8760
113.0973
3
1339 6458
129.7478
I
1023.5387
113.4115
4
1346. 1410
130.0619
2
1029. 2172
113.7257
5
1352.6520
130.3761
3
1034. 91 13
114.0398
6
1359. 1786
130.6903
4
1040. 6212
114.3540
7
1365 . 7210
131.0044
S
1046.3467
114.6681
8
1372.2791
131. 3186
6
1052.0880
114.9823
9
1378.8529
131.6327
7
1057.8449
113.2965 42
0
1385.4424
131.9469
8
1063. 6176
115.6106
1
1392.0476
132.2611
9
1069 . 4060
115.9248
2
1398.6685
132.5752
37.0
1075. 2101
116.2389
3
1405. 3051
132.8894
74
Mallicmalical laljlcs
Akeas and Circumferences of Circles for IJiameters
FROM Ho TO loo Advancing by Tenths — {Continued)
Diameter
Area
Circumference Diair
ictcr
Area
Circumference
42.4
I4II.9S74
i33.ao3S 47
7
1787.0086
149 8540
S
1418.6254
Ii3.S«77
8
1794. S091
l.So itXl
.6
1425.3092
133.8318
9
I802 02S4
ISO iHiJ
.7
1432.0086
13.1.1460 48
0
1809 5574
ISO -,'/h
.8
1438.7238
134.4602
I
1817.1050
ISI 1106
•9
I44S 4546
134 7743
2
1824.6684
IS« 4248
43 o
1452.2012
135.0885 '
3
1832 2475
151 7389
.1
1458.9635
135 4026
4
1839 8423
152 0531
.2
1465.7415
135.7168 ,
5
1847.4528
152 3672
■ 3
1472.5352
136.0310 i
6
1855.0790
152 6814
■4
1479 3446
136 3451 1
7
1862. 7210
152 9956
.5
i486. 1697
1366593
8
1870.3786
153 3097
.6
1493.0105
136.9734
9
1878.0519
153 6239
• 7
1499 8670
137.2876 49
0
1885.7409
153 9380
.8
1506.7393
137 6018
I
1893 4457
154 2S22
-9
1513 6272
137 9159
2
1901 1662
154 5664
440
1520.5308
138.2301
3
1908.9024
154 8805
.1
1527.4502
138.5442
4
1916.6543
155 1947
.2
1534.3853
138.8584
5
1924.4218
155 .5088
.3
1541.3360
139 1726 [
6
1932.2051
155 8230
.4
1548.3025
139.4867 I
7
1940.0042
156.1372
• S
1555.2847
139 8009
8
1947.8189
156 4513
.6
1562.2826
140.1153
9
1955.6493
156 7653
.7
1569.2962
140.4292 50
0
1963 4954
157 0796
.8
1576.3255
140.7434
I
1971.3572
157 3938
•9
1583.3706
141.0575
2
1979 2348
157 7080
45. o
1590.4313
141. 3717
3
1987.1280
158 0221
.1
1597.5077
141.6858
4
1995.0370
IS8 3363
.2
1604.5999
142.0000
S
2002.9617
158.6504
• 3
161 I. 7077
142.3142
6
2010.9020
158.9646
4
1618. 8313
142.6283
7
2018.8581
159 2787
• 5
1625.9705
142.9425
8
2026.8299
159 5929
.6
1633. 1255
143.2566
9
2034.8174
159 9071
• 7
1640.2962
143.5708 51
0
2042.8206
160.2212
.8
1647.4826
143.8849
I
2050.8395
160 5354
9
1654.6847
144.1991
2
2058.8743
160 849s
46.0
1661.9025
144.5133
3
2066.924s
161 . 1637
.1
1669. 1360
144.8274
4
2074.9905
161.4779
.2
1676.3853
145.1416
S
2083.0723
161 . 7920
.3
1683.6502
145. 4557
6
2091.1697
162 . 1062
.4
1690.9308
145.7699
7
2099.2829
162.4203
• 5
1698.2272
146.0841
8
2107.4118
162.734s
.6
1705.5392
146.3982
9
2115.5563
163.0487
.7
1712.8670
146.7124 52
0
2123. 7166
163.3628
.8
1720.2105
147.0265
I
2131.8926
163.6770
•9
1727.5697
147.3407
3
2140.0843
163.9911
47.0
1734.9445
147.6550
3
2148.2917
164.3053
.1
1742. 3351
147.9690
4
2156.5149
164.6195
.2
1749.7414
148.2832
5
2164.7537
164.9336
.3
1757.1635
148.5973
6
2173.0082
165.2479
• 4
1764.6012
148.9115
7
2181.2785
165.5619
• S
1772.0546
149.2257 1
8
2189.5644
165.8761
.6
1779.5237
149.. 5398 !
1
9
2197. 8661
166.1903
Areas and Circumferences of Circles
75
Areas and Circumferences of Circles for Diameters
FROM i-io to ioo .\dvancing BY TENTHS — {Continued)
Diameter
Area
Circumference
Diameter
Area
Circumference
S3.0
2206.1834
166.5044
58.3
2669 . 4820
183.5914
.1
2214.516s
166.8186
.4
2678.6476
183.4690
.2
2222.8653
167.1327
.5
2687.8289
183.7832
.3
2231 . 2298
167.4469
6
2697.0259
184.0973
• 4
2239 . 6100
167.7610
.7
2706 . 2386
184. 41 IS
.5
2248.0059
168.0752
.8
2715.4670
184.7256
.6
2256.417s
168.3894
• 9
2724. 7112
185.0398
• 7
2264.8448
168.7035
59.0
2733.9710
185.3540
.8
2273.2879
169.0177
.1
2743.2466
185.6681
•9
2281.7466
169.3318
.2
2752.5378
185.9823
540
2290.2210
169.6460
.3
2761.8448
186 . 2964
.1
2298. 7112
169 . 9602
.4
2771.167s
186.6106
.2
2307. 2171
170.2743
•5
2780.5058
186.9248
.3
2315.7386
170.5885
.6
2789.8599
187.2389
.4
2324.2759
170.9026
.7
2799.2297
187.5531
• 5
2332.8289
171. 2168
.8
2808.6152
187.8672
.6
2341-3976
171. 5310
.9
2818.016s
188.1814
• 7
2349.9820
171. 8451
60.0
2827.4334
188.4956
.8
2358.5821
172.1593
.1
2836.8660
188 . 8097
■9
2367 . 1979
172.4735
.2
2846.3144
189.1239
55. o
2375.8294
172.7876
•3
2855.7784
189.4380
.1
2384.4767
173.1017
.4
2865.2582
189.7522
.2
2393.1396
173.4159
• 5
2874.7536
190.0664
■ 3
2401. 8183
173.7301
.6
2884.2648
190.3805
■ 4
2410. 5126
174.0442
.7
2893.7917
190.6947
• S
2419.2227
174.3584
.8
2903.3343
191.0088
.6
2427.9485
174.6726
.9
2912.8926
191.3230
■ 7
2436.6899
174.9867
61.0
2922.4666
191.6372
.8
2445.4471
175.3009
.1
2932.0563
191. 9513
■9
2454.2200
175.6150
.2
2941.6617
192.265s
56.0
2463.0086
175.9292
3
2931.2828
192.5796
.1
2471. 8130
176.2433
4
2960.9197
192.8938
.2
2480.6330
176.5575
5
2970.5722
193.2079
.3
2489.4687
176.8717
6
2980.2405
193 5221
.4
2498.3201
177.1858
.7
2989.9244
193.8363
• 5
2507.1873
_ 177.5000
.8
2999.6241
194.1504
.6
2516.0701
177.8141
.9
3009.3395
194.4646
■ 7
2524.9687
178.1283
62.0
3019. 070s
194.7787
.8
2533.8830
178.4425
.1
3028.8173
195.0929
.9
2542.8129
178.7566
.2
3038.5798
195.4071
S7.0
2551.7586
179 0708
• 3
3048.3580
195.7212
.1
2560.7200
179.3849
.4
3058 . 1520
196.0354
.2
2569.6971
179.6991
.5
3067.9616
196.349s
.3
2578.6899
180.0133
.6
3077.7869
196.6637
.4
2587.6985
180.3274
.7
3087.6279
196.9779
.5
2596.7227
180.6416
.8
3097.4847
197.2920
.6
2605.7626
180.9557
• 9
3107.3571
197.6062
■ 7
2614. 8183
181.2699
63.0
3117.2453
197.9203
.8
2623.8896
181.5841
.1
3127.1492
198.234s
.9
2632.9767
181 8982
.2
3x37.0688
198.5487
58.0
2642.0794
182.2124
.3
3147.0040
198.8628
.1
2651. 1979
182.526s
.4
3156.9550
199.1770
•2
2660.3321
182.8407
.5
3166.9217
199. 49"
76
M.ithem:ili< :il 'I'aliles
AkEAS ANU (.JKC TMl-KKKNCKS OV CiRCI-ES FOR DlAMl M
FROM !io TO lOO AUVANI l\G HY TKNTHS — (Co////'
Diiimetcr
An-.-x
Circumference
Diameter
Area
CircumUTi-ncc
63.6
3176.9043
199 8oS3
68.9
3728. 4SC»
216.4556
.7
3186 9033
300 119s '
69.0
3739
3807
216 7699
.8
3196.9161
aoo.4336 !
.1
37SO
1270
217 0841
■ 9
3206 94S6
200.7478
.2
3760
9891
217 398»
64.0
3216.9909
201.0620
• 3
3771
8668
217 7124
.1
3227 651 »
201.3761
.4
3782
7603
218 0265
.2
3237 128s
201.6902
5
3793
669s
218 3407
■ 3
3247 2222
202.0044
.6
3804
5944
318 6548
.4
3257 3289
202.3186
•7
3Sts
S350
318 9690
S
3267.4527
202.6327
.8
3826
4913
219 2832
.6
3277.5922
202 . 9469
.9
3837
4633
219 5973
■ 7
3287.7474
203.2610
70.0
,3848
4510
219 9H 5
.8
3297 9183
203.5752
.1
.3859
4544
220 2256
•9
3308.1049
203.R894
.2
3870
4736
220 5398
6s.o
3318.3072
204 2035
• 3
3881
5084
220 8540
.1
3328.5253
204.5176
.4
3892
5S90
221.1581
.2
3338.7590
204.8318
■ 5
3903
6252
221.4823
.3
3349 008s
205.1460
.6
3914
7072
221.7964
.4
3359.2736
205.4602
■ 7
3925
8049
222.1106
• S
3369 5545
20s. 7743 1
.8
3936
9182
222 4248
.6
3379 8510
206.0S85
• 9
3948
0473
222 7389
.7
3390.1633
206.4026
71.0
3959
1921
223.0531
.8
3400.4913
206.7168
.1
3970
3526
223.3672
• 9
3410.8350
207.0310
.2
3981
5289
223.6814
66.0
3421. 1944
207.3451
.3
3992
7208
223 9956
.1
3431.5695
207.6593
.4
4003
9284
224 3097
.2
3441.9603
207.9734
•5
4015
1518
224.6239
.3
3452.3669
208.2876
.6
4026
3908
224 9380
.4
3462.7891
208.6017
.7
4037
6456
225 . 2522
.5
3473.2270
208.9159
.8
4048
9160
225.5664
.6
3483.6807
209.2301
•9
4060
2022
225 880s
.7
3494.1500
209.5442
72.0
4071
5041
226 1947
.8
3504.6351
209.8584
.1
4082
8217
226 S088
•9
3515. 1359
210.1725
.2
1094
ISSO
226.8230
67.0
3525.6524
210.4867
.3
4105
5040
227.1371
.1
3536.1845
210.8009
■4
4116
8687
227.4513
.2
3546.7324
211.1150
5
4128
2491
227.7655
.3
35S7 . 2960
211.4292
.6
4139
6452
228 0796
.4
3567.8754
211.7433
• 7
4151
0571
2?8 3938
.S
3578.4704
212.0575
.8
4162
4846
228.7079
.6
3589. 081 I
212.3717
• 9
4173
9279
229.0221
■ 7
3599 7075
212.6858
73 0
4185
3868
229.3363
.8
3610.3497
213.0000
.1
4196
861S
229.6504
•9
3621 .0075
213.3141
.2
4208
3519
229.9646
68.0
3631. 681 I
213.6283
.3
4219
8579
230.3787
.1
3642.3704
213 9^25
.4
4231
3797
230.5929
.2
3653.0754
214.2566
.5
4242
9172
230.9071
.3
3663.7960
214 5708
1 -^
4254
4704
231.2213
■4
3674.5324
214.8849
1 .7
4266
0394
23I.S354
• S
3685.2845
215.1991
i •*
4277
6240
231.8495
.6
3696.0523
215 51.3.5
1 -9
4289
2243
232.1637
.7
3706.8359
215.8274
74.0
4300
8403
232.4779
.8
3717. 6.351
216.1416
i •*
4312
4721
232.7920
Areas and Circumferences of Circles
77
Areas and Circumferences of Circles for Diameters
FROM Ho TO loo Advancing by Tenths — {Continued)
Diameter
Area
Circumference Dian
leter
Area
Circumference
74.2
4324 I 195
233.1062 79
5
4963.9127
249.7566
3
4335.7827
J33.4203
6
4976.4084
250.0708
4
4347.4616
233.7345
7
4988.9198
250.3850
5
4359 1562
234.0487
8
5001 . 4469
250.6991
6
4370.8664
234.3628
9
5013 . 9897
251 0133
7
4382.5924
234.6770 80
0
.S026.5482
251.3274
8
4394 3341
234.9911
I
5039.1225
251.6416
9
4406.0916
235.3053
2
5051. 7124
251.9557
75
o
4417.8647
235.6194
3
S064 . 3180
252 . 2699
I
4429.653s
235 9336
4
5076.9394
252 . 5840
2
4441.4580
236.2478
S
5089.5764
252.8982
3
4453.2783
236.5619
6
5102 . 2292
253.2124
4
4465.1142
236.8761
7
5114.8977
253 5265
5
4476.9659
237 . 1902
8
5127. 5819
253.8407
6
4488.8332
237.5044
9
5140. 2818
254.1548
7
4500.7163
237.8186 81
0
S152.9973
254 . 4690
8
4512.6151
238.1327
I
5165.7287
254.7832
9
4524 . 5296
238 . 4469
2
5178.4757
255.0973
76
o
4536.4598
238.7610
3
5191.2384
255.4115
I
4548.4057
239.0752
4
5204 0168
255 . 7256
2
4560.3673
239.3894
5
5216. 8110
256 0398
3
4572.3446
239.7035
6
5229 6208
256 . 3540
4
4584.3377
240.0177
7
5242.4463
256.6681
5
4596.3464
240.3318
8
5255 . 2876
256.9823
6
4608.3708
240.6460
9
5268.1446
257 . 2966
7
4620. 41 10
240.9602 82
0
5281. 0173
257 6106
8
4632 . 4669
241.2743
I
5293.9056
257.9247
9
4644.5384
241.588s
2
5306.8097
258.2389
77
o
4656.6257
241.9026
3
5319.729s
2S8 5531
I
4668.7287
242.2168
4
5332.6650
258 . 8672
2
4680.8474
242.5310
5
5345 . 6162
259.1814
3
4692 . 9818
242.8451
6
5358.5832
259.4956
4
4705. 1319
243.1592
7
5371.5658
259.8097
5
4717.2977
243.4734
8
5384 . 5641
260.1239
6
4729.4792
243.7876
9
5397.5782
260 4380
7
4741.6756
244.1017 83
0
5410.6079
260.7522
8
4753.8894
244.4159
I
5423.6534
261.0663
9
4766. 1181
244.7301
2
5436.7146
261 . 380s
78
o
4778.3624
245.0442
3
5449. 7915
261 . 6947
I
4790.6225
245.3584
4
5462.8840
262.0088
2
4802.8983
245.672s
5
5475.9923
262.3230
3
481S.1897
245.9867
6
5489. I 163
262.6371
4
4827.4969
246.3009
7
5502.2561
262.9513
5
4839.8198
246.6150
8
5515. 4115
263.265s
6
4852.1584
246.9292
9
5528.5826
263.5796
7
4864.5128
247.2433 84
0
5.S41.7694
263 8938
8
4876.8828
247.5575
I
55,54.9720
264.2079
9
4889.2685
247.8717
2
5568 . 1902
264 . 5221
79
o
4901.6699
248.1858
3
5581.4242
264.8363
I
4914. 0871
248.5000
4
5594.6739
265.1414
2
4926.5199
248.8141
5
5607.9392
265.4646
3
4938.9685
249.1283
6
5621 . 2203
265.7787
4
4951.4328
249.442s
7
5634.5171
266.0929
78
Matluinalical Tables
Akkas and Circumferences of Cfrcles for Diameters
FROM Ho TO loo Advancing by Tenths — (Continued)
Diamt'tLT
Area
Circumference
Diameter
Area
Circtimfcrcnco
84.8
S647.8.'.
'. 4071
90.1
637s 8701
283.0575
9
seeiisTf^
.•'!<>. 7212
■2
6390
0309
283 3717
85
0
5674 SOI?
267 03.54
3
6404
2073
283 6858
I
5687 8614
267.3495
.4
6418
3995
284 0000
3
5701 2367
267 6637
5
6432
6073
284 3«4I
3
S7«4 6277
267.9779
.6
6446
8309
284 6283
4
5728. oi4S
268 2920
7
6461
0701
284 9425
5
S741.4569
268.6062
6475
3251
285 2566
6
S7S4.89SI
268.9203
'.(
6489 5958
28s S7o8
7
5768.3490
269.2345
91.0
6503 8822
285 8849
8
5781 8l8s
269.5486
.1
6518 1843
386.1991
9
5795.3038
269.8628
.2
6532.5021
286 513.3
86
0
S808.8048
270.1770
.3
6546 8356
286.8274
I
5822.3215
270.4911
.4
656J . 1848
287.1416
3
583s 8539
. 270.8053
.5
6575.5498
287 4557
3
5849.4020
27I.II94
.6
6589 9304
287.7699
4
5862 9659
271.4336
.7
6604 3268
288 0840
S
5876.5454
271.7478
.8
6618.7388
288 3982
6
5890.1407
272.0619
■ 9
6633.1666
288 7124
7
5903.7516
272.3761
92.0
6647. 6101
289.0265
8
5917 3783
272.6902
.1
6662.0692
289 3407
9
5931 0206
273.0044
.2
6676 5441
289.6548
87
0
5944 6787
273 3186
•3
6691.0347
289.9690
I
5958.352s
273.6327
.4
6705 5410
290.2832
3
5972.0420
273.9469
•5
6720.0630
290 5973
3
5985.7472
274 2610
.6
67^4.6008
290 9115
4
5999 4681
274.5752
.7
6749.1542
291.2256
5
6013.2047
274.8894
.8
6763 7233
291 5398
6
6026.9570
275.2035
• 9
6778.3082
291.8540
7
6040.7250
275.5177
93.0
6792.9087
292.1681
8
6054.5088
275.8318
.1
6807.5250
292 4823
9
6068.3082
276.1460
.2
6822.1569
292 7964
88
0
6082.1234
276.4602
•3
6836 8046
293.IT06
I
6095 9542
276.7743
• 4
6851.4680
293.4248
2
6109.8008
277.0885
5
6866.1471
293.7389
3
6123,6631
277.4026
6
6S80.8419
294.0531
4
6137. 54"
277.7168
■ 7
6895.5524
294.3672
S
6151.4348
278.0309
.8
6910 2786
294.6814
6
6165.3442
278.3451
• 9
6925 020s
294.9956
7
6179.2693
278.6593
94.0
6939.7782
295 3097
8
6193. 2101
278.9740
.1
6954 5SI5
295.6239
9
6207.1666
279.2876
.2
6969.3106
295.9380
89
0
6221. 1389
279.6017
.3
6984.1453
296.2522
1
6235.1268
279 9159
4
6998.9658
296.5663
2
6249.1304
280.2301
5
7013. 8019
296.8805
3
6263.1498
280.5442
.6
7028.6538
297.1947
4
6277.1849
280.8584
.7
7043.5214
297.5088
S
6291 . 2356
281.1725
.8
7058.4047
297.8230
6
6305.3021
281.4867
.9
7073.3033
298.1371
7
6319.3843
281.8009
95. 0
7088 . 2184
298.4513
8
6333.4822 .
282. 1 ISO
.1
7103.1488
298.7655
9
6347.5958
282.4292
.2
7118.1950
299 0796
90
0
6361. 7251
282.7433
1 ■'
7133.0568
299 3938
Areas and Circumferences of Circles
79
Areas and Circumperences of Circles for Diameters
FROM Ho TO loo Advancing by Tenths — {Concluded)
Diameter
Area
Circumference Diair
later
Area
Circumference
95. 4
7148.0343
2997079 97
8
7512.2078
307.2478
• 5
7163
0276
300.0221
9
7527.5780
307.5619
.6
7178
0366
300.3363 98
0
7542.9640
307.8761
■ 7
7193
0612
300.6504
I
7558.3656
308.1902
.8
7208
1016
300.9646
2
7573.7830
308.5044
•9
7223
1577
301.2787
3
7589. 2161
308.8186
96.0
723S
2295
301.5929
4
7604.6648
309.1327
.1
7253
3170
301.9071
5
7620.1293
309.4469
.2
7268
4202
302.2212
6
7635.6095
309.7610
.3
7283
5391
302.5354
7
7651 . 1054
310.0752
.4
7298
6737
302.8405
8
7666.6170
310.3894
•S
7313
8240
303.1637
9
7682.1444
310.7035
.G
7328
9901
303.4779 99
0
7697.6893
311. 0177
.7
7344
1718
303.7920
I
7713 2461
311. 3318
.8
73S9
3693
304 . 1062
2
7728.8206
311.6460
•9
7374
5824
304.4203
3
7744.4107
311.9602
97.0
7389
8113
304.7345
4
7760.0166
312.2743
.1
740s
0559
305.0486
5
7775.6382
312.5885
.2
7420
3162
305.3628
6
7791.2764
312.9026
.3
7435
5922
303.6770
7
7806.9284
313.2168
■ 4
74SO
8839
305.9911
8
7822.5971
313.5309
.5
7466
1913
306.3053
9
7838. 281S
313.8451
.6
74S1
5144
306.6194 100
0
7853.9816
314.1593
.7
7496
8532
306.9336
To compute the area or circumference of a circle of a diameter greater than
100 and less than looi;
Take out the area or circumference from table as though the number
had one decimal, and move the decimal point two places to the right for
the area, and one place for the circumference.
Example. — Wanted the area and circumference of 567. The tabular
area for 56.7 is 2524.9687, and circumference 178.1283. Therefore area
for 567 = 252496.87 and circumference = 1781.283.
To compute the area or circumference of a circle of a diameter greater than
1000,
Di\ide by a factor, as 2, 3, 4, 5, etc., if practicable, that will leave a
quotient to be found in table, then multiply the tabular area of the
quotient by the square of the factor, or the tabular circumference by the
factor.
£a;am/>/e. — Wanted the area and circumference of 2109. Dividing
by 3, the quotient is 703, for which the area is 388150.84 and the circum-
ference 2208.54. Therefore area of 2109 = 388150.84 X 9 = 3493357-56
and circumference = 2208.54 X 3 = 6625.62.
8o
Malhcmulical Tablci
Table df CiRCirtAR Arcs
Lenflli of circular arcs when the ihord and ihc heithi of the arc are [hen.
Divide the hciKht by the chord. Find in the cfilumn of Heights the number
equal to this quotient.
Take out the correspondinR number from the column of IcnRtii
Multiply this luit numlier by the length of the given chord.
Heights
Lengths
Heights
Lengths
Heigh'
HeighU Li
•ngths
.001
I.O0OO3
.049
1.00638
•097
I. 02491
US I
05516
.002
1.00002
.050
1.00665
.098
I.02S42
146 I
OSS9I
.003
I 00003
•OS I
1.00692
•099
I 02593
147 I
05667
.004
1.00004
.052
1.00720
.100
1.02646
148 1
OS743
.00s
1.00007
.053
1.00748
.101
1 .02698
149 »
05819
.006
i.oooto
.054
1.00776
.102
1.02752
150 1
05896
.007
I. 00013
.05s
1.0080s
.103
1 .02806
ISI 1
OS97.J
.008
1.00017
.056
1.00834
.104
1 02860
152 I
06031
.009
1.00022
.057
1.00864
.105
1.02914
IS3 I
06130
.010
1.00027
.058
1.00895
.106
1.02970 1
IS4 I
06209
.011
1.00032
.059
1.00926
.107
1.03026 ll
ISS 1
0628S
.012
1 .00038
.060
1.00957
.loS
I 03082
156 1
06368
.013
I. 0004s
.061
1.00989
.109
I 031.39
IS7 »
06449
.014
1.00053
.062
1.01021
.110
1.03196
158 1
06530
.ois
I. 00061
.063
1.01054
.111
I 03254
159 I
0661 1
.016
1.00069
.064
1.01088
.112
I. 03312
160 1
06693
.017
1.00078
.065
1.01123
.113
1.03371
161 1
06775
.018
1.00087
.066
1.01158
.114
1 03430
163 1
06858
.019
1.00097
.067
I. 01 103
.115
1.03490
163 1
06941
.020
1.00107
1 r l.'j-,
.116
I. 03551
164 1
07025
.021
1.00117
1 I ■ :
.117
1.03611
l6s I
07109
.022
1.00128
.-7-
1 .iij-J
.113
1.03672
166 I
07194
•023
I. 00140
.071
1.01338
.119
1.03734
167 I
07279
.024
I. 00153
.072
I .01376
.120
1.03797
168 I
07365
.025
1.00167
.073
I.01414
.121
1.03860
169 1
074SI
.026
I .00182
.074
I. 01453
.122
I 03923
170 I
07537
.027
I. 00196
■075
I. 01493
.123
1.03987
171 1
07624
.028
I. 00210
.076
I 01533
.124
1.640SI
172 1
07711
.029
1.00225
■077
1 01573
•125
I. 04116
173 I
07799
.030
I .00240
.078
I.01614
.126
I .04181
174 I
07888
■031
1 .00256
.079
I .01656
.127
I .04247
173 I
07977
.032
I .00272
.080
1.01698
.128
I. 04313
176 1
08066
■033
1.00289
.081
1.01741
.129
1.04380
177 I
08156
■034
1.00307
.082
I. 01784
.130
1.04447
178 .1
08246
.035
1 .00327
.0S3
1 .01828
.131
I 04SIS
179 1
08337
.036
i.oo,W5
.0S4
I. 01872
.132
1.045S4
180 I
0847a
■037
I .00364
.085
I. 01916
.133
1 .04652
181 1
08519
.038
1.00384
.086
1.01961
.134
1 .04722
182 I
08611
.039
1.0040s
.087
1.02006
.13s
I .04792
183 1
08704
.040
1.00426
.088
1 .02052
.136
I .04862
184 I
08797
.041
I 00447
.089
1.02098
.137
I 049.32
185 1
08890
.042
I .00469
.090
1.02146
.138
1.05003
186 I
08984
•043
1 .00492
.091
1 .02192
■139
I 0507s
187 1
09079
.044
1.0051S
.092
1.02240
.140
1.0S147
188 1
09174
■04S
I .00539
.093
1.0x189
.141
1.05220
189 1
09269
.046
1 00563
.094
I 02339
.I.U
1.05293
190 I
09363
.047
1.00587
.095
I .02389
.143
1.05367
191 1
09461
.048
1.00612
.096
1 .02440
.144
I. 05441
192 I
09SS7
Table of Circular Arcs
Table of Circular Arcs — {Continued)
8i
Heights
Lengths
Heights
Lengths
Heights
Lengths He
ights L
engths
.193
1.09654
.24S
1 . 15670
.303
1 . 22920
358 1
31276
■ .194
1.09752
.249
I . 15791
304
1 . 23063
359 1
31437
.195
1.09850
.250
1.15912
.305
1 . 23206
360 I
31599
.196
1.09949
.251
1.16034 \
.306
1 ■ 23349
361 1
31761
.197
I . 10048
.252
1.16156
• 307
1.23492
362 I
31923
.198
1.10147
.253
1 . 16279
.308
1.23636
363 1
32086
• 199
I. 10247
.254
1 . 16402
.309
1.23781
364 I
32249
.200
I. 10347
.255
1 . 16526
.310
I . 23926
365 1
32413
.201
I . 10447
.256
1 . 16650
.311
1 . 24070
366 1
32577
.202
I. 10548
.257
1.16774
.312
1.24216
357 1
32741
.203
I . 10650
.258
I . 16899
.313
1 . 24361
368 1
32905
.204
I. 10752
.259
1.17024
.314
1.24507
369 1
33069
.205
1.10855
.260
I. 17150
.315
1.24654
370 1
33234
.206
I. 10958
.261
I . 17276
.316
1 24801
371 I
33399
.207
1.11062
.262
1 . 17403
.317
I . 24948
372 1
33564
.20S
1.1116s
.263
1.17530
.318
1.25095
373 1
33730
.209
1.11269
.264
1.17657
.319
1 . 25243
374 1
33896
.210
I. 11374
.265
1.17784
.320
I. 25391
375 1
34063
.211
1.11479
.266
1.17912
.321
I 25540
376 1
34229
.212
I. I 1584
.267
1 . 18040
.322
I . 25689
377 1
34396
■ 213
1.11690
.268
1.18169
.323
1.25838
378 1
34563
.214
1.11796
.269
1.18299
■ 324
1.25988
379 I
34731
.215
1.11904
.270
1.18429
.325
I . 26138
380 1
34899
.216
1.12011
.271
I. 18559
.326
I . 26288
381 1
35068
.217
1.12118
.272
1 . 18689
• 327
1.26437
382 1
35237
.218
1.12225
.273
1 . 18820
.32S
I . 26588
383 1
35406
.219
1- 12334
.274
1 . 18951
.329
1 . 26740
384 I
35575
.220
1 . 12444
.275
1 . 19082
.330
1 . 26892
385 I
35744
.221
I. 12554
.276
1.19214
.331
1.27044
386 I
35914
.222
I . 12664
.277
1.19346
.332
1.37196
387 1
36084
.223
I. 12774
.278
1.19479
.333
1.27349
388 I
36254
.224
1 . 12885
.279
1.19612
• 334
1.27502
389 1
3642s
.225
I. 12997
.280
I . 19746
.335
1.27656
390 1
36596
.226
1.13108
.281
1 . 19880
.336
1.27810
391 I
36767
.227
I. 13219
.282
1.20014
.337
1.27964
392 1
36939
.228
1.13331
.283
1.20149
.338
1.28118
393 I
37111
.229
I • 13444
.284
1.202S4
.339
1 . 28273
394 I
37283
.230
1.13557
.285
I. 20419
.340
1.28428
395 1
37455
.231
1.13671
.286
1.20555
.341
1.28583
396 1
37628
.232
1.13785
.287
1.20691
.342
1.28739
397 I
37801
■ 233
1.13900
.288
1.20827
.343
1.28895
398 I
37974
.234
1 14015
.279
1.20964
.344
1.29052
399 I
38148
.235
1.14131
.290
1.21102
.345
1.29209
400 I
38322
.236
1.14247
.291
1 . 21239
.346
1.29366
401 1
38496
.237
1.14363
.292
1.21377
.347
1.29523
402 1
38671
.238
I . 14480
.293
1.2151S
.348
1.29681
403 1
38846
.239
1.14597
.294
1.21654
.349
1.29839
404 1
39021
.240
I . 14714
.295
1.21794
.350
1.29997
40s I
39196
.241
1.14832
.296
1.21933
.351
1.30156
406 1
39372
.242
I . 149SI
.297
1.22073
.352
I. 3031s
407 I
39548
.243
1.15070
.298
1.22213
.353
1.30474
408 I
39724
.244
1.15189
.299
1.22354
.354
1.30634
409 1
39900
.245
I. 15308
.300
1.22495
• 355
1.30794
410 1
40077
.246
1.15428
.301
1.22636
.356
1.30954
411 I
402S4
.247
I. 15549
.302
1.22778
.357
I.3111S
412 I
40432
Mallicm;ilic;il Tables
Table op Circular Arcs — (Concluded)
HeighU
Lengthn
t. 40610
Heights
Lengths
.457
'hs Heights Lengths
.413
.435
1.44589
479 «
S2931
.414
I. 40788 '
'.•>'
I 44773 '
.458
480 1
53126
.41S
1.40966
I 449.S7
459
1.49079
481 1
53322
.416
1.41145
1 45142
.460
1.49269
482 I
53SI8
.417
1. 41324
, -M'J
1.45327
.461
1.49460
483 I
53714
.418
1.41S03
.440
I.4SSI2
.462
1.49651
484 I
53910
.419
1.41682
.441
1.45697
.463
1.49842
48s I
54106
.430
1.41861
.442
1.45883
.464
I S0033
486 I
S4.*)2
.421
I. 42041
.443
1.46069
.46s
1.50224
487 «
54499
.422
1 .42221
.444
I.462SS
.466
1.S0416
488 I
54696
.423
I . 42402
.445
I. 46441
.467
1.S0608
489 I
54893
.424
1.42583
.446
1.46628 !
.468
1.50800
490 1
55091
.42s
1.42764
.447
I. 46815
.469
1.50992
491 I
55289
.426
1.4294s
.448
I . 47002
1 .470
1.51185
492 1
55487
.427
1. 431 27
.449
I. 47189
{ .471
I S1378
493 1
55685
.428
1.43309
.450
1-47377
.472
ISIS7I
494 I
55884
.429
I. 43491
.451
1.47565
.473
I. 51764
49S I
56083
.430
1.43673
.452
1.47753
.474
1.51958
496 I
S6282
.431
1.438S6
.453
1.47912
• 475
I. 52152
497 1
56481
.432
1.44039
.454
1.48131
.476
1.52346
498 I
56681
.433
1.44222
.455
1.48320
' .477
1.52541
499 I
56881
.'434
I. 4440s
.456
1.48509
.478
1.52736
500 I
57080
Lengths of Circular Arcs to Radius 1
To find the length of a circular arc by the following table
Knowing the radius of the circle and the measure of the arc in deg.,
min., etc.
Rule. — Add together the lengths in the table found respectively
opposite to the deg., min., etc., of the arc. Multiply the sum by the
radius of the circle.
Example. — In a circle of 1 2.43 feet radius, is an arc of 13 deg., 27 min.,
8 sec. How long is the arc?
Here, opposite 13 deg. in the table, we find .2268928
" 27 min. " " " " .0078540
" 8 sec. " " " " .0000388
Sum = . 2347856
And .2347856 X 12.43, or radius = 2.918385 feet, the required length
of arc.
Lengths of Circular Arcs to Radius i 83
Lengths of Circular Arcs to Radius i
Deg.
Length
Deg.
Length
Deg.
Length
Deg.
Length
I
.0174533
46
.8028515
91
1.5882496
136
2.3736478
2
.0349066
47
.8203047
92
1.6057029
137
2. 391 101 I
3
.0523599
48
.8377580
93
I. 6231562
138
2.4085544
4
.0698132
49
.8552113
94
1.6406095
139
2 . 4260077
5
0872665
50
.872664()
95
1.6580628
140
2 . 4434610
6
.1047198
51
.8901179
96
1.6755161
141
2 . 4609142
7
.1221730
52
.9075712
97
I . 6929694
142
2 . 478367s
8
.1396263
53
.9250245
98
1.7104227
143
2 . 4958208
9
.1570796
54
.9424778
99
1.7278760
144
2.5132741
10
. 1745.329
55
.9593911
100
1.7453293
145
2 . 5307274
II
. 1919862
56
9773844
lOI
I . 7627825
146
2.5481807
12
.2094395
57
.9948377
102
1.7802358
147
2.5656340
13
. 2268928
58
1.0122910
103
I. 797689 I
148
2.5830873
14
.2443461
59
1.0297443
104
1.8151424
149
2 . 6005406
15
.2617994
60
I. 0471976
105
1.8325957
150
2.6179939
16
■ 2792527
61
1.0646508
106
1.8500490
151
2.6354472
17
. 2967060
62
1.0821041
107
1.8675023
152
2 . 652900s
18
.3141593
63
I.0995S74
108
1.8849556
153
2.6703538
19
.3316126
64
1.1170107
109
1.9024089
154
2 . 6878070
20
.3490659
65
I. 1344640
no
1.9198622
155
2 . 7052603
21
.3665191
66
1.1519173
III
I. 9373155
156
2.7227136
22
.3839724
67
I . 1693706
112
1.9547688
157
2.7401669
23
.4014257
68
I . 1868239
113
I. 9722221
158
2.7576202
24
.4188790
69
I . 2042772
114
1.9896753
159
2.7750735
25
■4363323
70
I. 2217305
115
2.0071286
160
2.7925268
26
.4537856
71
I . 2391838
116
2.0245819
161
2.8099801
27
.4712389
72
1.2566371
117
2.0420352
162
2.8274334
28
.4886922
73
I . 2740904
118
2.0594885
163
2 . 8448867
29
.5061455
74
1.2915436
119
2.0769418
164
2 . 8623400
30
.5235988
75
1.3089969
120
2.0943951
165
2.8797933
31
.5410521
76
1.3264502
121
2. I I 18484
166
2.8972466
32
.5585054
77
1.3439035
122
2.1293017
167
2.9146999
33
.5759587
78
I. 3613568
123
2.1467550
168
2 932IS3I
34
.5934119
79
1.3788101
124
2 . 1642083
169
2.9496064
35
.6108652
80
1.3962634
125
2.1816616
170
2.9670597
36
.6283185
81
1.4137167
126
2.1991149
171
2.9845130
37
.6457718
82
1.4311700
127
2.2165682
172
3.0019663
38
.6632251
83
1,4486233
128
2.2340214
173
3.0194196
39
.6806784
84
I . 4660766
129
2.2514747
174
3.0368729
40
.6981317
85
1.4835299
130
2.2689280
175
3.0543262
41
.7155850
86
I . S009832
131
2.2863813
176
3.0717795
42
.7330383
87
I. 5 184364
132
2.3038346
177
3.0892328
43
.7504916
88
1.5358897
133
2.3212879
178
3.1066861
44
.7679449
89
1.5533430
134
2.3387412
179
3.1241394
45
.7853982
90
1.5707963
135
2.3561945
180
3.1415927
Min.
Length
Min.
Length
Min.
Length
Min.
Length
I
.0002909
6
.0017453
II
.0031998
16
.0046542
2
.0005818
7
.0020362
12
.0034907
17
.0049451
3
.0008727
8
.0023271
13
.0037815
18
.0052360
4
.0011636
9
.0026180
14
.0040724
19
.0055269
S
■0014544
10
.0029089
15
.0043633
20
.0058x78
84 Malhem.ilical Tallies
Lkngths of Cikcular Arcs to Radius i — (Continued)
Min.
Length
Min.
1
Length
Min.
Length
Min.
Length
21
.0061087
31
.009017s
0119264 1
SI
0148353
22
006399.';
33
.009J084
0122173
S3
0151262
23
.0066904
33
.0095993
.0125082
53
0154171
34
0069813
34
.0098902
.0127991
54
0157080
2S
0072722
3S
.0101811
.0130900
SS
.0159989
36
0075631
36
.01047-^
013.3809
S6
.0162897
27
0078540
37
.oioT'i-' 1
oi.}67l7
57
.0165806
38
00S1449
38
.01 lo.s c
0139626
S8
.016871S
29
.00S4.358
39
.01 1314''
014253s
59
.0171624
30
.0087266
40
.OIl6.5Si
0145444
60
017453.3
Sec.
Length
Sec.
Length
Sec.
Len^:: '.
Length
I
.0000048
16
.0000776
31
0001503
46
.0002230
2
.0000097
17
.0000824
32
.0001 S51
47
.0002279
3
.0000145
18
.0000873
33
.0001600
48
.00O2,V7
4
.0000194
19
.0000921
34
.0001648
49
.0002376
S
.0000242
20
.0000970
33
.0001697 :
SO
.0002424
6
.0000291
21
.0001018
36
.0001745 I
SI
.0002473
7
.0000339
22
.0001067
37
.0001794
52
.0002521
8
.0000388
23
.0001115
38
.0001842 1
S3
.0002570
9
.0000430
34
.0001164
39
.0001891
54
.0002618
10
.0000485
35
.0001212
40
.0001939
55
.0002666
II
.0000533
36
.0001261
41
.0001988
56
.0002715
12
.0000582
27
.0001309
42
.0002036
57
.0002763
13
.0000630
38
.OOOI3S7
43
.0002085
S8
.0002812
14
.0000679
29
.0001406
44
.0002133
59
.0002860
IS
.0000727
30
.00014.54
45
.0002182
60
.0002909
Table of Areas of Circular Segments
If the segment exceeds a semicircle, its area = area of circle — area of a segment
whose rise = (diam. of circle — rise of given segment). Diam. of circle = (square
of half chord ^ rise) + rise, whether the segment exceeds a semicircle or not.
Rise
divided
Vjy diam.
of circle
Area =
(square
of diam.)
multi-
plied by
Rise
divided
by diam.
of circle
Area =
(square
of diam.)
multi-
plied by
.001329
.001533
.001746
.001969
.002199
.002438
.002685
.002940
.003202
Rise
divided
by diam.
of circle
Area =
(square
of diam.)
multi-
plied by
Rise
divided
by diam.
of circle
Area =
(square
o/diam.)
muki-
plicd by
.001
.002
.003
.004
• 005
.006
007
.008
.009
.000042
.000119
.000219
.000337
.000471
.000619
.000779
.000952
.001135
.010
.on
.012
.013
.014
.015
.016
.017
.018
.019
.020
.021
.022
.023
.024
.025
.026
.027
.003472
.003749
.004032
.004322
.004619
.004922
.005231
.005546
.005867
.028
.029
.030
.031
.032
.033
.034
.035
.036
.006194
.006527
.006866
.007209
.007SS9
.007913
.008273
.008638
.009008
Table of Areas of Circular Segments
8S
Table of
Areas
OF Circular Segments —
{Continued)
Rise
divided
by diam
of circle
Area =
(square
of diam.)
multi-
plied by
Rise
divided
by diam
of circle
Area =
(square
of diam.)
multi-
plied by
Rise
divided
by diam
of circle
Area =
(square
of diam.)
multi-
plied by
Rise
divided
by diam
of circle
Area=
(square
of diam.)
multi-
plied by
• 037
.009383
.087
.033308
• 137
.064761
.187
.101553
.038
.009764
.088
•033873
.138
.065449
.188
102334
.039
,010148
.089
•034441
• 139
.066140
.189
103116
.040
.010538
.090
.035012
.140
.066833
.190
.103900
.041
.010932
.091
.035586
.141
.067528
.191
• 104686
.042
.011331
.092
• 036162'
.142
,068225
.192
• 105472
•043
.011734
• 093
•036742
• 143
,068924
.193
, 106261
.044
.012142
• 094
•037324
.144
,069626
.194
• 10705 1
• 045
•012555
• 09s
•037909
.145
•070329
■195
• 107843
.046
.012971
.096
•03S497
.146
.071034
.196
• 108636
• 047
.013393
• 097
.039087
■ 147
•071741
■197
• 109431
.048
.013818
.098
.039681
.148
•072450
.198
.110227
.049
.014248
•099
.040277
.149
•073162
■199
.III02S
.050
.014681
• loo
.040875
• ISO
•073875
.200
.111824
.051
.015119
.101
•041477
.151
•074590
.201
.112625
.052
.015561
.102
.042081
.152
•075307
.202
•I 13427
■OS3
.016008
.103
.042687
.153
.076026
.203
•II423I
.054
.016458
.104
.043296
.154
•076747
.204
•I 15036
■ 055
.016912
.105
.043908
.155
•077470
.205
.115842
■ 056
.017369
.106
•044523
.156
.078194
.206
.116651
•057
.017831
.107
.045140
.157
.078921
.207
.117460
058
.018297
.108
•04S759
.158
•079650
.208
.118271
059
.018766
.109
.046381
•159
.080380
.209
.119084
.060
.019239
.110
.047006
.160
.081112
.210
.119898
.061
.019716
.III
•047633
.161
,081847
.211
.120713
.062
.020197
.112
.048262
.162
,082582
.212
■ I2I530
.063
.020681
■ 113
.048894
.163
.083320
.213
.122348
.064
.021168
.114
.049529
.164
.084060
.214
.123167
.065
.021660
• 115
.050165
.165
.084801
.215
. 123988
.066
.022155
.116
• 050805
.166
•085545
.216
.124811
.067
•033653
.117
.051446
.167
.086290
,217
• 125634
.068
.023155
.118
.052090
.168
•087037
.218
• 126459
.069
.023660
.119
.0527.37
.169
•087785
.219
. 127286
.070
.024168
.120
•053385
.170
•088536
.220
.128114
071
.024680
.121
•054037
.171
.089288
.221
.128943
.072
.025196
.122
.054690
.172
.090042
.222
• 129773
073
.025714
.123
.055346
.173
•090797
.223
• 130605
074
.026236
.124
.056004
.174
•091555
.224
• I31438
.075
.026761
.125
.056664
.175
.092314
.225
• 132273
.076
.027290
.126
.057327
.176
.093074
.226
•I33I09
.077
.027821
.127
.057991
.177
•093837
.227
.133946
.078
.028,356
.128
.058658
.178
• 094601
.228
.134784
.079
.028894
.129
.059328
.179
.095367
.229
• 135624
.080
.029435
■ 130
•059999
.180
•096135
.230
. 13646s
081
.029979
.131
.060673
.181
.096904
• 231
.137307
.082
.030526
.132
.061349
.182
.097675
• 232
• I3815I
.083
■031077
.133
.062027
.183
.098447
.233
•138996
.084
.031630
.134
.062707
.184
.099221
.234
• 139842
.085
.032186
.1.35
.063389
.185
•099997
• 235
. 140689
.086
.032746
.136
.064074
.186
.100774
.236
• I4I538
86
Mallunialiial 'I'alilcs
Table of
Areas
OF CiRCULAK SeCUENTS —
(Coniinwd)
Rise
divided
by diam.
Area ■•
(square
of diam.)
multi*
Rise
divided
by diam.
Area —
(sfiuarc
of dium.)
Rise
divided
by diam.
Area —
(sc)uarc
of diam.)
Rise
divided
by diam.
Area-
(square
of diam.)
multi-
plied by
of circle
plied by
.I42.V--
of circle
plied by
of circle
plied by
of circle
.237
.186339
.337
.232634
.387
.280669
.aj8
.143239
.jh-s
.18723s
.338
.233580
.388
.281643
.239
.144091
.289
.188141
.339
.234526
.389
.283618
.240
.144945
.290
.189048
.340
.235473
.390
283593
.a4i
.145800
•291
.189956
.341
.236421
.391
•284569
.242
.146656
.292
.190865
.342
.237369
.392
•285545
.243
147513
.293
.191774
.343
.238319
.393
.286521
.244
.148371
.294
.192685
.344
.239268
.394
.287499
.245
.149231
1 .295
.193597
.345
.240219
.395
.288476
.246
.150091
: .296
.194509
.346
.241170
.396
.289454
.247
. 150953
.297
. 195423
.347
.243132
.397
.290432
.248
.151816
.298
.196337
.348
.343074
.398
291411
.249
.152681
.299
. 197252
.349
.344037
.399
.292390
.250
.153546
.300
.198168
.350
.244980
.400
.293370
.251
• 154413
.301
.199085
.351
.245935 !
.401
.294350
.253
.155281
.302
.200003
.352
.246890
.402
.295330
.253
.156149
.303
.200922
.353
.247845
.403
.296311
.254
.157019
.304
.201841
.354
.248801
.404
•297292
.255
. 157891
.305
.203762
.355
.249758
.405
.298274
.256
. 158763
.306
.203683
.356
.250715
.406
.299256
.257
.159636
.307
.204605
.357
.251673
.407
.300238
.258
.160511
.308
.205528
.358
.353632
.408
.301331
.259
.161386 I
.309
.206452
.359
.253591
.409
.302304
.260
.162263
.310
.207376
.360
.254551
.410
.303187
.261
.163141 '
3"
.208302
1 .361
.255511
.411
.304171
.262
. 164020
.312
.209228
.362
.256472
.412
.305156
.263
.164900
.313
.210I5S
.363
.257433
.413
.306140
.264
.165781
.314
.211083
.364
.258395
.414
.307125
.26s
.166663
.31S
.212011
.36s
.259358
.415
.308110
.266
.167546
.316
.212941
.366
.260321
.416
.309096
.267
. 168431
.317
.213871
.367
.261285
.417
.310082
.268
. 169316
.318
.214802
.368
.262249
.418
.311068
.269
. 170202
.319
.215734
■.369
.263214
.419
.312055
.270
.171090
.320
.216666
.370
.264179
.420
.313042
.271
.171978
• 321
.217600
.371
.265145
.421
.314029
.272
.172868
.322
.218534
.372
.266111
.422
.315017
.273
•173758
.323
.219469
.373
.267078
.423
.316005
.274
. 174650
.324
. 220404
.374
.268046
.424
.316993
.275
.175542
.325
.221341
.375
.269014
.425
.317981
.276
.176436
.326
.222278
.376
.269982
.426
.318970
.277
.177330
.327
.223216
.377
.270951
.427
.319959
.278
.178226
.328
.224154
.378
.271921
.428
.320949
.279
.179122
.329
.225094
.379
. 272891
.429
.321938
.280
.180020
.330
. 226o,i4
.380
.273861
.430
.322928
.281
.180918
.331
.226974
.381
.274832
.431
.323919
.282
.181818
.332
.227916
.382
.275804
.432
.324909
.283
.182718
.333
.228858
.383
.276776
.433
.325900
.284
.183619
.334
.229801
.384
.277748
.434
.326891
.285
. 184522
.335
.230745
.385
.278721
.435
.327883
.286
.185425
.336
.231689
.386
.279695
.436
.328874
Table of Areas of Circular Segments 87
Table of Areas of Circular Segments — (Continued)
Rise
Area =
Rise
Area= j
.ise
Area= j^;^^
Area =
divided
(square
divided
(square ^j^
^ided
(square ^^^-^^^^
(square
by diam.
of circle
of diam.)
multi-
by diam.
of circle
of diam.) .
multi- „t
,. , , 01
diam.
::ircle
of diam.) by diam.
,n^"'*^- of circle
of diam.)
multi-
plied by
plied by
plied by
plied by
.437
.329866
.453
.345768
469
.361719
485
.377701
.438
.330858
.454
.346764
470
.362717
486
.378701
.439
.331851
.455
.347760
471
.363715
487
.379701
.440
.332843
.456
.348756
472
.364714
488
.380700
.441
.333836
.457
.349752
473
.365712
489
.381700
.442
.334829
.458
.350749
474
.366711
490
.382700
• 443
.335823
■ 459
.351745
475
.367710
491
.383700
.444
.336816
.460
.352742
476
.368708
492
.384699
.445
.337810
.461
.353739
477
.369707
493
.385699
.446
.338804
.462
.354736
478
.370706
494
.386699
.447
.339799
.463
.355733
479
■371705
495
.387699
.448
.340793
.464
.356730
480
.372704
496
.388699
.449
.341788
• 46s
.357728
481
■373704
497
.389699
• 450
.342783
.466
.358725
482
■374703
498
.390699
.451
.343778
.467
.359723
483
■375702
499
.391699
.452
.344773
.468
.360721
484
.376702
500
•392699
88
Mathematical Tables
Chords of Arcs from One to Ninety Decrees
Dimensions given in inches.
Ang.
Dcg.
l8-inch
36-inch
72-inch
,.
iH-inch
36-inch
73inch
radius
radius
radius
r.'idiuR
radius
radius
chord
rhord
chord
(.hord
chord
chord
I
••■..,
iW
46
14H6
38 Vi
^■<M
a
H
1'4
2V1
47
142564
382*62
S7»T64
3
'Mo
1%
3?i
48
14*! 64
29962
583^/64
4
iV*
2V1
S
49
i4»964
29*564
59* W2
S
I".64
3%4
6962
SO
iS'/62
3027/i«
6o»H«
6
iH
3«W4
7'?62
SI
15^6
31
63
7
2«H«
4='564
8S!.64
52
152562
3i9<«
63W
8
2H
5'/64
io564
53
i6V1«
32^
64 W
9
2m*
5^64
xx'964
54
16'^
32'H6
6s56
lO
3%*
6962
123 564
55
1656
33H
66W
II
32%4
62?62
I3H64
56
162962
33*^64
673964
12
3*%*
7'"^62
XS564
57
17'^
342564
68*562
13
4^4
8562
x6'964
58
172964
342962
69' Ms
14
4»Hi
82563
173 564
59
172562
352964
70*962
IS
4*564
92564
X85J44
60
18
36
72
l6
5
io)-64
20V62
61
I8'J64
363564
73564
17
5^64
XO<W4
2X962
62
183^4
37564
74' H4
I8
55i
IX'J64
22' ^2
63
x8>5i«
3756
7SW
19
5'M.
1X7,6
23*964
64
X9564
38562
765^6
20
6Vi
121/4
25
6S
X9' '/62
38iH«
7756
21
6M«>
I3V6
26>564
66
X93964
39^62
7827/64
22
6%
I3*?64
2731-64
67
19^6
39*^4
79' 562
23
THi
142564
28*564
68
20I.6
401^
8o«J62
24
73)44
143 '/62
29'5i«
69
202564
402562
8i91s
25
7«H4
153-^64
31' H4
70
20<!.64
4x1964
82»962
36
8J^2
i6>?64
322564
71
202962
4xi5i6
8356
27
8>?^2
X6>?i8
3356
72
2X562
4221 64
84*V64
38
8<564
17' 562
34>5i6
73
2x1562
425564
852^62
29
9V64
18I/62
36M8
74
2I2J62
432!'64
862^2
30
9^16
i8<V64
37"/64
75
215964
43*564
872^2
31
9H
19' 564
383 '/64
76
22562
442^64
882162
32
9*9^4
192 J62
39' M»
77
221 562
44*564
89*V64
33
loj^a
202%4
i,Q^'M
78
2221.62
455i.
9o56
34
xo' ^^2
2X5B4
42562
79
225^64
45*^4
91' 962
35
I05J64
2X21^2
43' 964
80
23964
46962
929i«
36
IIH
22«
44H
81
2356
4654
933564
37
Il2?64
222 J62
45' M«
82
233964
471564
94' 562
38
1X2^2
2ZlAi
46^4
83
23S584
47*564
95' 562
39
12^4
24'/62
48M«
84
24562
481V64
962564
40
I25,i«
2456
49'/4
85
242 164
48H64
97962
41
X23964
25%2
50^/^6
86
243564
49562
98>564
42
X 22 962
255 ".64
5X3964
87
242562
499i«
99H
43
X3?i»
262564
522562
88
25
50^4
looWa
44
133^4
263 ',62
53'5i«
89
25' 564
So«562
100' 5< 8
45
13*562
27^ H4
55?64
90
252964
502962
ioi»564
Chords
89
Fig. 35.
To Find the Length of a Chord which will Divide the Circumference of
a Circle into N Equal Parts Multiply S by the Diameter
N
s
iV
5
N
S
N
5
I
26
.12054
SI
.061560
76
04132s
2
27
.11609
52
.060379
.059240
77
78
040788
040267
3
.86603
28
.11197
53
4
.70711
29
.10812
54
.058145
79
0397S7
S
.58779
30
. I04S3
55
.057090
80
039260
6
.50000
31
.10117
56
.056071
81
038775
7
.43388
32
.098018
57
.055089
82
038303
8
.38268
33
.095056
58
■054139
83
037841
9
.34202
34
.092269
59
.053222
84
037391
10
.30902
35
.089640
60
•052336
85
036953
II
* 28173
36
.087156
61
.051478
86
036522
12
.25882
37
.084804
62
.050649
87
036103
13
.23932
38
.082580
63
.049845
88
035692
14
.22252
39
.080466
64
.049068
89
035291
15
.20791
40
.078460
65
.048312
90
034899
16
.19509
41
.076549
66
.047582
91
034516
17
.18375
42
.074731
67
.046872
92
034141
18
.17365
43
.072995
68
.046184
93
033774
19
.16460
44
.071339
69
.045515
94
033415
20
.15643
45
.069756
70
.044865
95
033064
21
.14904
46
.06S243
71
.044232
96
032719
22
. 14232
47
.066793
72
.043619
97
032381
23
.13617
48
.065401
73
.043022
98
032051
24
.13053
49
.064073
74
.042441
99
031728
25
.12533
50
.062791
75
.041875
100
031411
go
Mulhcmatiral Tallies
Lengths of Chords foe Spacing Cikcle whose Diameter is i
Por circles of other diameten multiply length given in table by diameter of circle.
No. of
Length of
No. of
Length of
No. of
Length of
No. of
Length of
spaces
chord
spaces
chord
spaces
chord
spaces
chord
26
.I305
51
.0616
76
.0413
27
.1161
52
.0604
77
.0408
3
.8660
38
.1120
S3
.0592
78
.0403
4
.7071
29
.1081
54
.0581
79
.0398
5
.5878
30
.1045
55
.0571
80
.0393
6
.5000
31
.1012
56
.0561
8t
.0388
7
.4339
32
.0980
57
.0551
83
.0383
8
.3827
33
.0951
58
.0541
83
.0378
9
.3420
34
.0923
59
.0532
84
.0374
lo
.3090
35
.0896
60
.0523
85
.0370
II
.3817
36
.0872
61
.0515
86
.0365
13
.3588
37
.0848
62
.0507
87
.0361
13
.2393
38
.0826
63
.0499
88
.0357
14
.2225
39
.0805
64
.0491
89
■ 03S3
IS
■ 2079
40
.0785
65
.0483
90
.0349
I6
.1951
41
.0765
66
.0476
91
.0345
17
.1838
42
.0747
67
.0469
92
.0341
I8
.1736
43
•0730
68
.0462
93
.0338
19
.1646
44
.0713
69
.0455
94
.0334
30
.1564
45
.0698
70
.0449
95
■ 0331
31
.1490
46
.0682
71
.0442
96
.0327
33
.1423
47
.0668
72
.0436
97.
0324
33
.1362
48
.0654
73
.0430
98
.0331
24
.130S
49
.0641
74
.0424
99
.0317
35
.1253
SO
.0628
75
.0419
100
.0314
Computed by W. I. Mann, Pittsburg, Pa.
Supplement to Machinery, February, 1903.
Board Measure
91
Board Measure
Length
in feet
Size
12
14
16
18
20
22
24
26
Square feet
IX 8
8
914
10%
12
13H
14%
16
17%
IX 10
10
11%
13%
15
16%
185.6
20
21%
1X12
12
14
16
18
20
22
24
26
IX14
14
1614
18%
21
23^^
25%
28
30%
IX16
16
18%
21!-^
24
26%
29%
32
34%
2X 3
6
7
8
9
10
11
12
13
2X 4
8
9H
10%
12
l3'/6
14%
16
17%
2X 6
12
14
16
18
20
22
24
26
2X 8
16
18%
2114
24
26%
29%
32
34%
2X10
20
23'/^
26%
30
33!/^
36%
40
43%
2X12
24
28
32
36
40
44
48
52
2X14
28
32%
371-6
42
46?6
51%
56
60%
2x16
32
3714
422/6
48
53^
58%
64
69%
3X 4
12
14
16
18
20
22
24
26
3X 6
18
21
24
27
30
33
36
39
3X 8
24
28
32
36
40
44
48
52
3X10
30
35
40
45
50
55
60
65
3X12
36
42
48
54
60
66
72
78
3X14
42
49
S6
63
70
77
84
91
3X16
48
56
64
72
80
88
96
104
4X 4
16
18%
21^
24
26%
29%
32
34%
4X 6
24
28
32
36
40
44
48
52
4X 8
32
37^
42%
48
S3H
58%
64
69%
4X10
40
46%
53^
60
66%
73%
80
86%
4X12
48
56
64
72
80
88
96
104
4X14
56
65I4
74%
84
93%
102%
112
121%
4X16
64
74%
85!'6
96
106%
117%
128
138%
6X 6
36
42
48
54
60
66
72
78
6X 8
48
56
64
72
80
88
96
104
6X10
60
70
80
90
100
110
120
130
6x12
72
84
96
108
120
132
144
156
6X14
84
98
112
126
140
154
168
182
6X16
96
112
128
144
160
176
192
208
8X 8
64
74%
85^
96
106%
117%
128
138%
SXio
80
9M
106%
120
133%
146%
160
173%
8X12
96
112
128
144
160
176
192
208
8X14
112
130%
1495^
168
186%
205%
224
242%
8X16
128
149'/^
170%
192
213%
234%
2S6
277%
10X10
100
116%
l33'/6
150
166%
183%
200
216%
10X12
120
140
160
180
200
220
240
260
10X14
140
163H
186%
210
233%
256%
280
303%
10X16
160
186%
21iM
240
266%
293%
320
346%
12X12
144
168
192
216
240
264
288
312
12x14
168
196
224
252
280
308
336
364
12X16
192
224
256
288
320
352
384
416
X4XI4
196
228%
261 H
294
326%
3S9V6
392
424%
14X16
224
261 '/5
298%
336
373%
410%
448
485%
16X16
256
298%
341'/^
384
426^6
469%
512
554%
92
Mathematical Tables
Hoard Measdre — (Continued)
Size
IX 8
IXIO
IXI2
1X14
IXl6
2X 3
2X 4
2X 6
2X 8
2XIO
2X12
2X14
2Xl6
3X 4
3X 6
3X 8
3XIO
3X12
3X14
3Xl6
4X 4
4X 6
4X 8
4X10
4X12
4X14
4Xl6
6x 6
6X 8
6xio
6X12
6X14
6xi6
8X 8
8Xlo
8X12
8X14
8Xl6
lOXlO
IOX12
10X14
10X16
12x12
12X14
12x16
14x14
14X16
16x16
38
Square foct
i8?6
28
32?{.
37 W
14
18?^
28
37^6
46?i
S6
6S!^
74^
28
42
S6
70
84
98
112
37)-^
S6
74^4
93!^
112
i3fm
84
112
140
168
196
224
149',-^
I862.S
224
261 V6
298?6
233'/^
280
326H
373!6
336
392
4 18
457H
S22'/6
S97W
20
, 1
25
26Ji
30
32
35
37^6
40
42^
IS
16
20
21 W
30
32
40
42^4
SO
53^4
60
64
70
72^6
80
85W
30
32
45
48
60
64
75
80
90
96
105
112
120
128
40
42H
60
64
80
»5M
100
io626
120
128
140
149W
160
17054
90
96
120
128
ISO
160
180
192
210
224
240
256
160
1707^
200
213^6
240
256
280
298%
320
341 '6
250
266?^
300
320
350
373' i
400
426? 6
360
384
420
448
480
S12
490
S22?6
s6o
S97H
640
682?S
22W
28J.4
34
39^
45^6
17
22^
34
4SH
56W
68
79W
90^4
34
SI
68
8S
102
119
136
45 W
68
90^
113^
136
I58?6
i8m
102
136
170
204
238
272
181H
226?^
272
317IS
362^3
283>4
340
396^6
453 !-6
408
476
544
SSSW
634%
725^4
24
asW
30
31^
36
38
42
44W
48
SfM
18
19
24
2SW
36
38
48
So%
60
63W
72
76
84
88%
96
101 W
36
38
54
57
72
76
90
9S
108
114
126
133
144
152
48
50W
72
76
96
101 W
120
126%
144
152
16S
177W
192
ao2%
108
114
144
152
180
190
216
228
252
266
288
304
192
202?S
240
253^
288
304
336
354%
384
40514
300
316%
360
380
410
443^4
480
506%
432
4S6
504
532
576
608
S88
620%
672
709H
768
810%
Note. — By simply multiplying or dividing the above amounts, the number of
feet contained in other dimensions can be obtained.
Surface and Volumes of Spheres 93
Weight of Lumber per iooo Feet Board Measure
Character of lumber
Dry
Partly
seasoned
Green
■ Pine and hemlock
Norway and yellow pine
Oak and walnut
Ash and maple
Pounds
2500
3000
4000
3500
Pounds
2750
4000
Sooo
4000
Pounds
3000
sooo
Surface and Volumes of Spheres
Spheres. (Original.) Trautwine.
Some errors of i in the last figure only.
Diam. S
irface
Solidity
Diam.
Surface
Solidity
Diam.
Surface
Solidity
Hi
00077
I%2
3.7583
.68511
2^2
15.466
S.7190
H2
00307
.00002
'/i
3.9761
.74551
Vi
15.904
5.9641
%4
00690
.00005
5/fc
4.2000
.80939
%2
16.349
6.2161
He
01227
.00013
3/1 s
4.4301
.87681
Me
16.800
6.4751
H2
02761
.00043
J^2
4 . 6664
.94786
11/^2
17.258
6.7412
H
04909
.00102
1/4
4.9088
1.0227
%
17.721
7.0144
^2
07670
.00200
%2
5.1573
1.1013
1%2
18.190
7.2949
Me
1 1045
.00345
Me
5.4119
I . 1839
Me
18.666
7.5829
^2
1S033
.00548
^^2
5. 6728
I . 2704
l=/^2
19.147
7.8783
H
19635
.00818
%
5 9396
1.3611
Vz
19-635
8.1813
%2
24851
.01165
l?i2
6.2126
I. 4561
^2
20.129
8.4919
5/6
30680
.01598
Jie
6.4919
I. 5553
?16
20 . 629
8.8103
1^2
37123
.02127
1532
6.7771
1.6590
^%2
21 . 135
9.1366
^
44179
.02761
w
7.0686
I. 7671
n
21.648
9.4708
1%2
51848
.03511
1%2
7 3663
1.8799
2^2
22 . 166
9.8131
7l6
60132
.04385
?l6
7.6699
1-9974
iMe
22.691
10.164
15^2
69028
.05393
1%2
7.9798
2.1196
25^2
23.222
10.522
H
78540
.06545
?i
8.2957
2 , 2468
H
23.758
10.889
1%2
88664
.07850
21/32
8.6180
2.3789
2542
24.302
11.265
9i6
99403
.09319
iHe
8.9461
2.S161
IMe
24.850
11.649
1%2 I
1075
. 10960
2%2
9.280s
2.6586
"A2
25. 405
12.041
n I
2272
.12783
?4
9.6211
2.8062
%
25.967
12.443
2'/i2 I
3530
. 14798
2=.^2
9.9678
2.9592
2%2
26.535
12.853
"/la I
4849
.17014
is/is
10.321
3.1177
>M6
27.109
13 . 272
2?^2 I
6230
■ 19442
27^2
10.680
3.2818
3^2
27.688
13.700
H I
7671
. 22089
%
11.044
3.4514
3
28.274
14.137
2^2 I
9175
.24967
2%2
II. 416
3.6270
Ha
29.46s
IS- 039
1^6 2
0739
. 28084
1516
11.793
3.8083
H
30.680
15-979
m2 2
236s
.31451
31/i2
12.177
3.9956
Me
31.919
16-957
% 2
4053
.35077
2
12.566
4 . 1888
H
33.183
17.974
29^2 2
5802
.38971
1/^2
12.962
4.3882
Me
34.472
19.031
>M6 2
761 1
.43143
Me
13.364
4.5939
H
35.784
20.129
3>42 2
9483
.47603
%2
13.772
4.8060
Ma
37.122
21.268
I 3
1416
.52360
1/^
14 . 186
5.0243
H
38.484
22.449
^2 3
3410
.57424
%2
14.607
5-2493
Me
39.872
23-674
Me 3
5466
.62804
?i6
15 033
5.4809
H
41 . 283
24.942
'A
Mathematical Tables
Spheres — (Continued)
Diam.
Surfoce
Solidity
Diam.
Surfucc
Solidity
Diam.
Surface
Solidity
3'M«
42.719
26 2S4
8
aoi 06
368 08
MH
671 95
1637 9
^
44 179
27 6n
Ml
207.39
280 8s
94
683 49
1680 3
'M«
45 664
29 016
M
213. 8j
294.01
H
69s 13
1733 3
H
47.173
30 466
9»
330.36
307.58
IS
706 8s
1767.2
'?1e
48 708
31 96s
M2
326.98
321.56
M
718 69
1811 7
4
SO 26s
33.SIO
H
333.71
335 9S
^4
730 63
i8S7 0
Mo
SI 848
.« 106
94
240.53
3S0.77
96
743.6s
1903 0
Jh
S.V4S6
36.751
H
347.4s
366.03
Mi
754 77
1949 8
•>16
55 089
38.448
9
254. 47
381.70
H
767 00
1997.4
y*
S6 745
40.19s
H
261.59
397.83
94
779 32
ao4S.7
M«
58.427
41 994
Vt
368.81
414.41
?6
791 73
2094 8
9i
60 133
43.847
9i
376.12
431.44
16
804.2s
2144 7
Mb
61.863
45. 752
W
283.53
448.93
W
816.8s
2I9S 3
H
63.617
47.713
H
291 04
466.87
Vi
829 57
3346.8
9i»
65.397
49 729
%
298.65
485.31
96
842 40
3399 I
56
67.201
51.801
~<i
306.36
504.31
W
855.29
3352 I
'Mb
69.030
S3. 929
10
U4 16
523.60
96
868.31
2406 0
54
70.883
S6.116
'h
.W2.06
5.13.48
94
881 42
3460 6
'91b
72.759
58.359
M
330 06
563.86
H
894 63
2516 I
^i
74.663
60.663
9i
338.16
S84.74 '
17
907 93
2572.4
'Mb
76.589
63 026
H
346.36
606.13
W
921 33
2629 6
5
78.540
65.450
H
3S4.66
628.04
H
934 83
3687.6
Mb
80.516
67.935
94
363.05
650.46
96
948.43
2746 s
^i
82.516
70.482
li
371. 54
673.42
H
962 13
3806 2
?<fl
84.S41
73.092
II
380.13
696.91
96
975 91
2866.8
H
86.S9I
75.767
H
388.83
720,95
94
989.80
2928 2
5<B
88.664
78.505
M
397.61
745.51
•A
1003.8
2990.S
?i
90 763
81.308
96
406.49
770.64
18
1017.9
3053 6
'/1 6
92.887
84.178
H
415.48
796.33
H
1032.1
3117 7
Hi
95.033
87.113
96
424.56
822.58
y*
1046.4
3182.6
918
97.20s
90. n8
94
433.73
849.40
96
1060.8
3248 5
5i
99 401
93.189
%
443.01
876.79
^i
1075.3
3315.3
'Mb
loi 62
96.331
12
452.39
904.78
96
1089.8
3382.9
H
103.87
99 541
H
461.87
933 34
94
1104. 5
34SI.S
'91b
106.14
102.82
y*
471.44
962.52
%
1119.3
3521.0
j^s
108.44
106.18
96
481.11
992.28
19
1134. 1
3591 4
'5i6
110.75
109.60
Vi
490.87
1022.7
V6
1 149 I
3662.8
6
113.10
113.10
96
S00.73
1053 6
H
1164.3
3735 0
i-i
117.87
120.31
94
S10.71
1085.3
96
1179 3
3808.3
H
122.72
127.83
H
S20.77
1117.5
M
1194 6
3882. s
96
127.68
135.66
13
530.93
1150.3
96
1210.0
3957 6
Mi
132 73
143.79
^6
541 19
1183.8
94
1225.4
4033. 5
H
137 89
152.25
M
551.55
1218.0
J6
1241.0
4110.8
9i
143 14
161.03
96
562.00
1252.7
20
1256.7
4188.8
?6
148.49
170.14
H
572. 55
1288.3
M
1273.4
4367.8
7
153 94
179 59
96
583.20
1324.4
H
1388.3
4347.8
H
159 49
189.39
91
593 93
1361.2
96
1304.2
4438.8
!4
16S.13
199 S3
56
604.80
1398.6
yi
1320.3
4510.9
9i
170.87
210.03
14
615.75
1436.8
96
1336.4
4593. 9
!^
176.71
220.89
!-6
626.80
1475.6
94
1352.7
4677.9
^
182.66
232.13
M
637 95
1515. I
?6
1369 0
4763.0
94
188.69
243.73
96
649 17
1555. 3
31
1385. S
4849.1
J6
194 83
25572
yi
660.52
1596 3
H
1403.0
4936.3
Spheres
Spheres — {Continued)
95
Diam.
Surface
Solidity
Diam.
Surface
Solidity
Diam.
Surface
Solidity
2lH
1418.6
5,024-3
27;i
2441. I
11.341
mA
3739-3
21,501
?6
1435.4
5,113-5
28
2463.0
11.494
A
3766. 5
21.736
^
1452.2
5,203.7
H
2485.1
11,649
3/4
3793.7
21,972
56
1469.2
5,295.1
H
2507.2
11,80s
A
3821 . 1
22,210
%
1486.2
5,397.4
%
2529-5
11,962
35
3848.5
22,449
^
IS03.3
5.480.8
H
2551-8
12,121
A
3876.1
22,691
22
1520.5
5,575.3
%
2574-3
12,281
H
3903.7
22,934
H
1537.9
5,670.8
H
2596.7
12,443
A
3931 -5
23.179
M
1555-3
5,767-6
H
2619.4
12,606
A
3959-2
23,425
H
1572.8
5,865.2
29
2642.1
12,770
H
3987-2
23,674
\^
1590-4
5,964-1
5-6
2665.0
12,936
¥i
4015.2
23,924
%
1608.2
6,064.1
H
2687.8
13.103
A
4043-3
24,176
H
1626.0
6,165.2
%
2710.9
13.272
36
4071 -5
24,429
%
1643.9
6,267.3
Vi
2734-0
13,442
A
4099.9
24,685
23
1661.9
6,370.6
%
2757-3
13,614
H
4128.3
24,942
H
1680.0
6,475 -0
¥i
2780.5
13,787
A
4156.9
25,201
H
1698.2
6,580.6
li
2804.0
13.961
A
4185.5
25,461
%
1716.5
6,687.3
30
2827.4
14.137
A
4214.1
25,724
^
1735 0
6,795.2
\i
2851 . 1
14.315
H
4243.0
25,988
H
1753-5
6,904.2
H
2874-8
14.494
A
4271.8
26,254
%
1772. I
7,014 3
%
2898 . 7
14.674
37
4300.9
26,522
■'A
1790.8
7,125.6
\i
2922.5
14.856
A
4330.0
26,792
24
1809.6
7,238.2
%
2946 . 6
15.039
H
4359-2
27,063
^
1828.5
7,351.9
Yi
2970.6
15.224
A
4388.5
27,337
Vi
1847 -5
7,466.7
H
2994.9
15.411
A
4417.9
27,612
%
1866-6
7,583-0
31
3019 I
15.599
A
4447. 5
27,889
H
1885.8
7.700.1
H
3043 .6
15,788
%
4477.1
28,168,
%
1905. I
7,818.6
H
3068.0
15,979
A
4506-8
28,449
H
1924-4
7,938.3
%
3092.7
16,172
38
4536. 5
28,731
%
1943-9
8,059.2
H
3117-3
16.366
A
4566.5
29,016
2S
1963-5
8,181.3
H
3142-1
16,561
A
4596.4
29,302
H
1983-2
8,304.7
H
3166.9
16.758
A
4626.5
29,590
H
2002.9
8,429.2
li
3192.0
16,957
A
4656.7
29,880
%
2022.9
8,554-9
32
3217.0
17.157
A
4686.9
30,173
yt
2042.8
8,682.0
H
3242.2
17.359
¥*
4717.3
30,466
^
2062.9
8,810.3
Vi
3267.4
17.563
A
4747.9
30,762
%
2083 -0
8,939-9
9i
3292.9
17,768
39
4778-4
31.059
^
2103.4
9,070.6
Vz
3318.3
17,974
A
4809.0
31.359
26
2123. 7
9,202.8
H
3343.9
18,182
A
4839-9
31,661
H
2144.2
9,336.2
H
3369.6
18,392
A
4870-8
31.964
H
2164.7
9,470-8
H
3395.4
18,604
A
4901.7
32,270
?6
2185. 5
9,606-7
33
3421.2
18,817
A
4932.7
32,577
V^
2206.2
9,744-0
'A
3447.3
19,032
H
4964.0
32,886
^
2227.1
9,882.5
H
3473-3
19.248
A
4995.3
33.197
H
2248.0
10,022
9i
3499-5
19,466
40
S026.5
33,510
n
2269.1
10,164
'A
3525-7
19,685
A
S058.1
33,826
27
2290.2
10,306
H
3552 -I
19,907
H
5089.6
34.143
^
2311-5
10,450
H
3578.5
20,129
A
5121.3
34,462
H
2332.8
10,595
'A
3605.1
20.3S4
A
5153-1
34,783
%
2354.3
10,741
34
3631-7
20.580'
A
5184-9
35,106
H
2375.8
10,889
A
3658.5
20,808
%
5216.9
35,431
^
2397.5
11,038
H
3685.3
21.037
A
5248.9
35.758
%
2419.2
11,189
H
3712.3
21,268
41
5281. I
36.087
y6
Malhcmuticul Talilcs
Spheres — (jCanlinued)
Diom.
Surface
Solidity
Diam.
Surface
Solidity
Diam.
Surface
SoUdity
4i^i
S.«i.< .«
36.418
4754
7163. I
%lf3r/
..,.
0.288 s
84.177
W
S34S.6
36,751
J6
7200.7
57.4 -.
V,.V}1 2
84.760
H
5378. I
37.086
48
723« 3
S7.</.^'
'.',374.1
85,344
W
5410.7
37.423
W
7276.0
58,360
;«
9.417.2
85,931
H
5443.3
37.763
M
7313.9
58,815
56
9.460.2
86,521
H
5476.0
38.104
56
7351.9
59.274
55
9.S03.2
87,114
Ji
SS08.9
38.448
\'i
7389 9
59.734
H
9.546. s
87,709
42
5541.9
38.792
56
7428.0
60.197
M
9.590 0
88,307
H
5574. 9
39.140
?4
7466 3
60.663
56
9.6.U 3
88.908
H
5608.0
39.490
J6
7504.5
61,131
Vi
9.676 8
89.511
H
5641.3
39.841
49
7543.1
61.601
56
9.720.6
90.117
W
5674.5
40,194
^6
7581.6
62.074
54
9,764.4
90.726
H
5708.0
40.551
W
7620.1
62.549
56
9.808.1
91.338
H
5741.5
40.908
56
7658 9
63,026
56
9.852.0
91.953
Ji
5775.2
41.268
H
7697.7
63,506
Vi
9,896.0
92.570
43
5808.8
41,630
56
7736.7
63,989
H
9.940.2
93.190
W
5842.7
41.994
54
7775. 7
64,474
■'v
9.984 4
93.812
H
5876. S
42.360
56
7814.8
64,961
1 ,
! 0,029
94.438
H
5910.7
42.729
50
7854.0
65.450
■5t»
10.073
95.066
Vi
5944.7
43.099
H
7893.3
65.941
54
10,118
95.697
56
5978.9
43.472
«
7932.8
66,436
56
10,163
96.330
^4
6013.2
43.846
56
7972.2
66.934
57
10,207
96.967
J6
6047.7
44.224
Vi
8011.8
67.433
56
10,252
97.606
44
6082.1
44.602
56
80S1.6
67.93s
H
10,297
98.248
^
6116.8
44.984
54
8091.4
68.439
56
10.342
98.893
H
6151.5
45.367
56
8131.3
68.946
\h
10.387
99.541
^
6186.3
45.753
SI
8171.2
69.456
56
10.432
100.191
H
6221 . 2
46.141
^6
8211.4
69.967
54
10.478
100,845
56
6256.1
46.530
M
8251.6
70482
56
10.523
101,501
%
6291.2
46.922
56
8292.0
70,999
58
10.568
102,161
56
6326. S
47.317
\'i
8332.3
71,519
56
10,614
102,823
45
6361.7
47.713
56
8372.8
72.040
54
10.660
103.488
H
6397.2
48.112
54
8413.4
72.565
56
10,706
104.ISS
H
6432.7
48.513
56
8454.1
73,092
54
10,751
104.826
?6
6468.3
48.916
52
8494.8
73,622
56
10,798
IOS.499
>i
6503.9
49.321
M
8535.8
74.154
54
10.844
106.175
56
6539.7
49.729
W
8576.8
74.689
56
10.890
106.854
5^4
6575.5
50.139
56
8617.8
75.226
59
10.936
107.536
J6
6611.6
S0.551
Vi
8658.9
75.767
56
10.983
108.231
46
6647.6
S0.965
56
8700.4
76.309
54
11.029
108.909
H
6683.7
5 1. 382
54
8741.7
76.854
56
11.076
109,600
, ^«
6720.0
51.801
56
8783.2
77.401
54
11,122
110,294
56
6756.5
52,222
53
8824.8
77.952
56
11,169
110,990
Vi
6792.9
52.645
).6
8866.4
78.505
54
11,216
111,690
56
6829.5
53.071
^^
8908.2
79.060
56
11,263
112.392
54
6866.1
53.499
56
8950.1
79.617
60
11,310
113.098
%
6902.9
53.929
Vi
8992.0
80.178
56
11.357
113.806
47
6939 9
54,362
56
9034.1
80.741
54
11.404
114.518
V6
6976.8
54.797
^4
9076.4
81.308
56
11.452
115.232
H
7013 9
55.234
' 56
9118.5
81.876
Vi
11.499
"5.949
56
7050.9
55,674
54
9160.8
82,448
56
11.547
116,669
H
7088.3
56.115
^6
9203.3
83,021
54
11.595
I17J92
56
7125.6
56.559
M
9246.0
83.598
56
11.642
118,118
Spheres
Spheres — (Continued)
97
Diam.
Surface
Solidity
118.847
Diam.
Surface
Solidity
Diam.
Surface
Solidity
6i
11,690
6756
14.367
161,927
74H
17.320
Z14.333
H
11.738
119.579
H
14.420
162,827
56
17.379
215.417
H
11,786
120,31s
li
14.474
163,731
H
17.437
216.50S
H
11,834
121,053
68
14.527
164,637
56
17.496
217.597
H
11,882
121,794
'/6
14,580
165,547
H
17.554
218,693
H
11.931
122,538
Vi
14,634
166,460
J6
17.613
219,792
H
11,980
123,286
56
14,688
167,376
75
17,672
220,894
■'A
12,028
124,036
5-i
14,741
168,29s
^6
17.731
222,001
62
12,076
124,789
56
14,795
169,218
M
17.790
223,111
\^
12,126
125.545
54
14.849
170,145
56
17.849
224,224
H
12,174
126,30s
J6
14.903
171,074
\i
17,908
225,341
H
12,223
127,067
69
14,957
172,007
56
17,968
226,463
}i
12,272
127,832
^6
1S.012
172,944
H
18,027
227,588
56
12,322
128,601
H
15.066
173,883
%
18,087
228,716
H
12,371
129.373
56
15.120
174.828
76
18,146
229,848
li
12,420
130,147
H
15.175
175.774
%
18,206
230.984
63
12,469
130,92s
56
15.230
176.723
H
18,266
232.124
H
12,519
131,706
H
15.284
177.677
n
18,326
233.267
Vi
I2,s68
132,490
n
15.339
178.635
H
18,386
234.414
%
12,618
133,277
70
15.394
179.59s
56
18,446
235.566
H
12,668
134.067
H
15.449
180,559
¥i
18,506
236.719
6/i
12,718
134.860
H
15.504
181,525
%
I8,s66
237.879
%
12,768
135.657
56
15.560
182,497
77
18,626
239.041
Ji
12,818
136,456
V2
15.615
183,471
'yi
18,687
240,206
64
12,868
137,259
56
15.670
184,449
H
18,748
241,376
H
12,918
138,065
%
15.726
185,430
56
18,809
242,551
H
12,969
138,874
J6
15.782
186,414
H
18,869
243,728 .
?6
13,019
139,686
71
15.837
187,402
56
18,930
244,908
J^
13,070
140,501
W
15.893
188,394
H
18,992
246,093
56
13,121
141,320
H
15.949
189,389
'A
19.053
247.283
%
13,172
142,142
56
16,005
190,387
78
19,114
248.475
^
13,222
142,966
H
16,061
191.389
H
19.175
249.672
6s
13,273
143.794
56
16. 117
192,39s
H
19.237
250.873
H
13,324
144.625
54
16.174
193,404
56
19.298
252.077
Vi
13,376
145.460
li
16,230
194,417
H
19.360
253.284
%
13.427
146,297
72
16,286
195.433
56
19,422
254.496
H
13.478
147.138
^6
16,343
196,453
54
19.483
255.713
56
i3,S3o
147.982
H
16,400
197.476
A
19.545
256.932
54
13,582
148,828
56
16,456
198.502
79
19.607
258.155
%
13,633
149.680
H
16,513
199.532
H
19.669
259.383
66
13.685
150.533
56
16,570
200,566
H
19.732
260,613
H
13,737
151.390
H
16,628
201,604
56
19.794
261,848
H
13.789
152.251
J6
16,685
202,645
H
19.856
263,088
56
13,841
153. 114
73
16,742
203,689
56
19.919
264,330
H
13.893
153.980
1/6
16.799
204,737
54
19.981
265,577
56
13.946
154.850
W
16,857
205,789
J6
20,044
266,829
54
13.998
155.724
56
16,914
206,844
80
20,106
268,083
J6
14.050
156.600
H
16,972
207,903
'/6
20,170
269.342
67
14.103
157.480
56
17.030
208,966
H
20,232
270,604
^6
14.156
158.363
H
17,088
210,032
56
20,296
271,871
H
14,208
159.250
li
17.146
211,102
H
20,358
273.141
56
14.261
160,139
74
17.204
212,17s
56
20,422
274.416
V6
14.314
161,032
'/6
17,262
213,252
H
20,485
275.694
98
Mulhcmulical Tahlcs
Sphekes — {Continued)
Surface
ao.S49
30,6l2
20,676
20,740
20,804
20,867
20,932
20,996
21,060
21,124
21,189
21,253
21.318
21,382
21,448
21,512
21,578
21,642
21,708
21,773
21.839
21.904
21.970
22,036
22,102
22,167
22,234
22,300
22.366
22,432
22,499
22,565
22,632
22,698
22,765
22,832
22,899
22,966
23,034
23.101
23.168
23.235
23.303
23.371
23.439
23,So6
23.575
23.643
23.711
23.779
23.847
23.916
Solidity Diam.
276.977
278,263
279.553
280,847
282,145
283,447
284,754
286,064
287,378
288,696
290,019
291.345
292,674
294,010
295.347
296,691
298,036
299.388
300,743
302,100
303.463
304.831
306.201
307.576
308.957
310,340
311.728
313,118
314.S14
315.915
317.318
318.726
320,140
321,556
322,977
324,402
325.831
327.264
328,702
330,142
331.588
333.039
334.492
335.951
337.414
338.882
340.352
341.829
343.307
344.792
346.281
347.772
87H
w
89
90
92
93
Surface
Solidity
Diam.
23.984
349.269
93J*
24.053
3S0.77I
94
24.122
3S2.277
H
24.191
353.78s
H
24.260
355.301
H
24.328
356.819
W
24.398
358.342
H
24.467
359.869
W
24.536
.361.400
li
24,606
362.935
9S
24.676
364.476
Mi
24.745
366.019
H
24.815
367.568
H
24.885
369.122
W
24.955
370.678
H
25.025
372.240
H
25.095
373.806
H
25.165
375.378
96
25,236
376.954
W
25.306
378.531
M
25.376
380. 1 IS
H
25.447
381.704
^
25.518
383.297
96
25.589
384.894
H
25.660
386.496
H
25.730
388.102
97
25,802
389.711
H
25.873
391.327
V*
25.944
392.945
H
26.016
394.570
H
26.087
396.197
H
26.159
397.831
H
26.230
399.468
Ji
26,302
401,109
98
26,374
402,756
W
26,446
404.406
y*
26,518
406,060
H
26,590
407,721
W
26.663
409,384
H
26.735
411.054
y*
26.808
412,726
H
26.880
414.405
99
26.953
416.086
!.6
27.026
417.774
y*
27.099
419.464
?6
27.172
421. 161
w
27.245
422.862
H
27.318
424.567
y*
27.391
426.277
%
27.464
427.991
100
27.538
429.710
27.612
431.433
Surface
27.686
27.759
27.833
27.907
27.981
28,055
28,130
28.204
28.278
28.353
28.428
28.S03
28.S77
28.652
28.727
28.802
28,878
28,953
29.028
29.104
29.180
29.255
29.331
29,407
29.483
29.559
29.636
29.712
29.788
29.865
29,942
30.018
30.095
30,172
30,249
30,326
30,404
30,481
30,558
30,636
30,713
30.791
30.869
30.947
31.025
31.103
31.181
31.259
31.338
31.416
Capacity of Rectangular Tanks
99
Capacity of Rectangular Tanks in U. S. Gallons for
Each Foot in Depth
Width of
tank
Length of tank
2 feet
2 feet,
6 ins.
3 feet
3 feet,
6 ins.
4 feet
4 feet,
6 ins.
5 feet
5 feet,
6 ins.
6 feet
Ft. Ins.
2
2 6
3
3 6
4
4 6
5
29.92
37.40
46.75
44
56
67
88
10
32
52.36
65.45
78.54
91.64
59
74
89
104
119
84
80
77
73
69
67.32
84.16
100.99
117.82
134.65
1SI.48
74. 8r
93.51
112.21
130.91
149 -61
168.31
187.01
82.29
102.86
123.43
144.00
164.57
185.14
205.71
226.28
89.77
112. 21
134.65
157.09
179-53
201.97
224.41
246.86
269.30
5 6
6
Width of
Length of tank
tank
6 feet, 6 ins.
7 feet
7 feet, 6 ins.
8 feet
8 feet, 6 ins.
9 feet
Ft. Ins.
2
2 6
3
3 6
4
4 6
S
5 6
6
6 6
7
97.25
121.56
145-87
170,18
194-49
218.80
243.11
267.43
291.74
316.05
104.73
130.91
157-09
183-27
209.45
235.63
261.82
288.00
314.18
340.36
366.54
112. 21
140.26
168.31
196.36
224.41
252.47
280.52
308.57
336.62
364.67
392.72
420.78
119.69
149.61
179-53
209.45
239.37
269.30
299.22
329.14
359.06
388.98
418.91
448.83
478.7s
127.17
158.96
190.75
222.54
254-34
286.13
317.92
349.71
381.50
413.30
455.09
476.88
508.67
540.46
134.6s
168.31
202.97
235.63
269.30
302.96
336.62
370.28
403.94
437.60
471.27
504.93
538.59
572.2s
605.92
7 6
8
8 6
9
MallKiiialical Taljlcs
C/VPACiTY OF Rectangular Tanks in U. S. Gallons fob
Each Foot in Depth — {Continued)
I.^n|{th of tank
Width of
Uiiik
9 feet.
6 ins.
10 feet
149 '"
187.01
224.41
261.82
299.22
336.62
374 03
411.43
448.83
486.23
523-64
561.04
598.44
635.84
673.25
710.65
748.05
10 fei't,
6 ins.
.1709
196*36
235 68
374 90
314-18
3.53-45
392-72
432 00
471-27
510-54
549 81
.589.08
628.36
667-63
706.90
746.17
785.45
824-73
II feet
II feet,
6 ins.
13 feet
Ft. Ins.
a
3 6
3
3 6
4
4 6
S
5 6
6
6 6
7
7 6
8
8 6
9
9 6
142.13
177.66
313.19
348.73
284 . 26
319-79
3SS 32
390-85
426.39
461.92
497-45
523-98
S68,st
604.05
639-58
675- n
164.57
205.71
346.86
28S.00
329.14
370.28
411 43
452.57
493 71
534.85 •
575. 99
617.14
658.28
699.42
740.56
781.71
822.86
864.00
905.14
172 OS
215 06
258 07
301.09
344 10
38s 10
430.13
473 14
S16.15
559 16
602.18
645 19
688.30
713 21
774.23
817.24
860.26
903-26
946.27
989-29
179 S3
224.41
269-03
314 18
.«9 06
403-94
448-83
493-71
538-59
583-47
638.36
673 24
718.13
763 00
807.89
852.77
897.66
942.56
987.43
1032 3
II 6
Number of Barrels (31.5 Gallons) in Cisterns and Tanks
I Bbl. 31.S Gallons 4.2109 Cubic Feet.
Diameter in feet
Depth in
feet
5
6
7
8
9
10
11
13
I
4-663
6.714
9.139
11-937
15.108
18.653
32.659
26.859
5
23.3
36.6
45-7
59-7
75.5
93 3
112. 8
134 3
6
28.0
40.3
54.8
71.6
90.6
III. 9
135 4
161. 2
7
32.6
47.0
64.0
83.6
105.10
130.6
158.0
188.0
8
37.3
53-7
73.1
955
120.9
149-2
180.6
214 9
9
42.0
60.4
82.3
107.4
136.0
167-9
203.1
341.7
10
46.6
67.1
91-4
119-4
151. 1
186.5
225.7
368.6
II
51.3
73.9
100. 5
131. 3
166.3
205.3
248.3
295.4
13
56.0
80.6
109.7
143-2
181. 3
333.8
270.8
322.3
13
60.6
87-3
118. 8
152. 2
196.4
242. 5
293-4
349 3
14
65.3
94-0
127.9
167. 1
211. S
261. 1
316.0
376.0
15
69.0
100.7
137. 1
179- 1
326.6
289.8
338.5
402.9
16
74.6
107.4
146.3
191. 0
241.7
298.4
361.1
4297
17
79.3
114. 1
155.4
202.9
256.8
317.1
383.7
456.6
18
83-9
120.9
164.5
214.9
271-9
335.7
406.2
483. S
19
88.6
127.6
173.6
226.8
387.1
354.4
438.8
SI0.3
30
93.3
134.3
182.8
238.7
302.3
373.0
451. 4
537.2
Number of Barrels in Cisterns and Tanks
Number of Barrels (31.5 Gallons) ik Cisterns and
Tanks — (Continued)
Diameter in feet
Depth
in feet
13
14
15
16
17
18
19
20
21
I
31 522
36.557
41.9
47.7
53.9
60.4
67.3
74.6
82.2
5
157.6
182.8
209.8
238.7
269.5
203.2
336.7
373.0
441.3
6
199. 1
219.3
251.8
286.5
323.4
362.6
404.0
447.6
493.6
7
220.7
255.9
293.8
334.2
377.3
423.0
471.3
522.2
575.8
8
252 2
292.5
335.7
382.0
431.2
483.4
538.7
590.8
658.0
9
283.7
329 0
377.7
429.7
485.1
543-9
606.0
671.5
740.3
10
315.2
365.6
419.7
477-5
539.0
604.3
673.3
746.1
822. 5
II
346.7
402.1
461.6
525.2
592.9
664.7
740.7
820.7
904.8
12
378.3
438.7
503.6
573.0
646.8
725 2
808.0
895.3
987.0
13
409.8
475.2
545.6
620.7
700.7
785.6
875-3
969-9
1069.3
14
441.3
51I-8
587. 5
668.5
754.6
846.0
942-6
1044-5
iiSi.S
15
472.8
548.4
629.5
716.2
808.5
906.5
lOIO.O
1119.1
1223.8
16
504.4
584.9
671.5
764.0
862.4
966.9
1077 -3
1193. 7
1316.0
17
535 9
621. s
713.4
811. 7
916.4
1027.4
1144-6
1268.3
1398.3
18
567.4
658.0
755.4
859.5
970.3
1087.8
1212.0
1342.9
1480.6
19
598.9
694.6
797.4
907.2
1024.2
1148.2
1279-3
1417.S
1562.8
20
630.4
731. 1
839.3
955.0
1078. I
1208.6
1346-6
1492. I
1645.1
Diameter
n feet
Depth in
feet
22
23
24
25
26
27
28
29
30
I
90.3
98.6
107.4
116. 6
126. 1
136.0
148.2
157. 9
167.9
5
451.4
483.3
537.2
582.9
630.4
679-8
731. 1
784.3
839.3
6
541.6
592. 0
644.6
699-4
756-5
815.8
877.4
941. 1
1007.2
7
631.9
690.7
752.0
816.0
882.6
951.8
1023.6
1098.0
II7S.O
8
722.2
789.3
859.5
932.6
1008.7
1087.7
1169.8
1254.9
1342.9
9
812.5
888.0
966.9
1049 -I
1134-7
1223-7
1316.0
1411.7
1510.8
10
902.7
986.7
1074.3
1165.7
1260.8
1359-7
1462 . 2
1568.6
1678.6
II
993-0
1085-3
1181.8
1282.3
1386.9
1495-6
i6o8.5
1725-4
1846.5
12
1083.3
1184.0
1289.2
1398.8
1513.0
1631.6
1764.7
1882.3
2014.0
13
1173.5
12S2.7
1396.6
1515-4
1639. I
1767.6
1900.9
2039-2
2182.2
14
1263-8
1381.3
1504 -O
1632.6
1765-2
1903-6
2047 2
2196.0
2350. I
15
1354 -I
1480.0
1611.5
1748.6
1891 . 2
20,39-5
2193 4
2352 9
2517.9
16
1444-4
1578.7
1718.9
1865. I
2017.3
2175-5
2339 6
2509.7
2685.8
17
1534-5
1677.3
1826.3
1981.7
2143.4
2311.5
2485.8
2666.6
2853.7
18
1624 . 9
1776.0
1933 8
2098.3
2269. 5
2447-4
2632 0
2823.4
3021. 5
19
1715- 2
1874.7
2041.2
2214.8
2395-6
2583-4
2778 3
2980.3
3189.4
20
180S-5
1973.3
2148.6
2321 4
2521.7
2719-4
2924 5
3137-2
3357.3
I02
Malhcmatical Tables
Contents of Cylinders, or Pipes
Contents for one foot in length, in cubic fc-ct, and in U. S.
gallons of 231 cubic inches, or 7.4805 gallons to a cubic fool. A cubic
foot of water weighs about 62^6 lbs.; and a gallon about 8M lbs. iJiams.
2, 3, or 10 times as great give 4, 9, or 100 times the content.
Fori
oot in
Diam-
iter in
inches
ctcr in
decimals
of a ioot
Cubic
feet. Also
Gallons
of 231
area in
square
feet
cubic
inches
Va
.0208
.0003
.0025
M«
.0260
.0005
.0040
H
.0313
.0008
.0057
lU
.0365
.0010
.0078
W
.0417
.0014
.0102
9i«
.0469
.0017
.0129
H
.0521
.002I
■01S9 •
iM«
.0573
.0026
.0193
^4
.C5625
.0031
.0230
'^is
.0677
.0036
.0269
li
.0729
.0042
.0312
»M8
.0781
.0048
.0359
I
.o8.?3
■ 0055
.0408
H
.1042
.0085
.0638
H
.1250
.0123
.0918
H
.1458
.0167
.1249
3
.1667
.0218
.1632
M
.1875
.0276
.2066
^^
.2083
.0341
.2550
H
.2292
.0412
.3085
3
.2500
.0491
.3672
H
.2708
.0576
.4309
H
.2917
.0668
.4998
H
.3125
-0767
.5738
4
.333,5
.0873
.6528
H
.3542
.098s
.7369
H
.3750
.1104
.8263
H
.3958
.1231
.9206
s
.4167
.1364
1.020
y*
.4375
. IS03
I. 125
w
.4583
.1650
1.234
%
.4792
.1803
1.349
6
.5000
.1963
1.469
y*
.5208
.2131
I.S94
Vi
.S4I7
.2304
1.724
H
.5625
.2485
I 8S9
7
.5833
.2673
I 999
y*
.6042
.2867
2.I4S
For I foot
in
length
Diam-
eter in
inches
cter in
decimals
of a foot
Cubic
feet. Also
Gallons
of 331
area in
square
feet
cubic
inches
W
.6250
.3068
3 29s
94
.6458
■ 3276
2
4SO
8
.6667
■3491
2
611
H
.6875
.3712
2
777
H
.7083
.3941
2
948
?i
.7292
.4176
3
I2S
9
.7SCX3
.4418
3
30s
M
.7708
.4667
3
491
M
.7917
.4922
3
683
%
.8125
.5185
3
879
10
.8333
.5454
4
080
H
.8542
.5730
4
286
H
.8750
.6013
4
498
%
.8958
.6303
4
71S
II
.9167
.6600
4
937
«
9375
.6903
S
164
W
.9583
.7213
5
396
94
.9792
.7530
5
633
12
ifoot
.7854
5
875
1,2
1.042
.8522
6
375
13
1.083
.9218
6
895
H
1. 125
.9940
7
436
14
1. 167
1.069
7
997
Vi
1.208
1.147
8
578
IS
1.250
1.227
9
180
'A.
1.292
1. 310
9
801
16
I 333
1.396
10
44
Vi
1. 375
1.485
II
II
17
1. 417
1.576
II
79
yi
1.458
1,670
13
49
18
1.500
1.767
13
33
u
I 542
1.867
13
96
19
1.583
1.969
14
73
'2
I 625
2.074
15
SI
20
1.667
2.182
16
32
y.
1.708
3.293
17
15
21
I.7SO
2.405
17
99
v^
1.792
3.S3I
18
86
Contents of Cylinders, or Pipes 103
Contents of CylinderSj or Pipes — (Continued)
For I
foot in
For I foot in
length
length
Diam-
eter in
Diam-
Diam-
Diam-
eter in
inches
decimals
of a foot
Cubic
feet. Also
Gallons
of 231
eter in
inches
decimals
of a foot
Cubic
feet. Also
Gallons
of 231
area in
cubic
area m
cubic
square
feet
inches
square
feet
inches
22
1.833
2.640
19.75
35
2.917
6.681
49 98
l^
1.87s
2.761
20.66
36
3 000
7.069
52.88
23
1. 917
2.885
21.58
37
3.083
7.467
55.86
^
1.958
3.012
22.53
38
3.167
7.876
58.92
24
2.000
3.142
23.50
39
3.250
8.296
62.06
25
2.083
3.409
25.50
40
3.333
8.727
65.28
26
2.1^7
3.687
27.58
41
3.417
9.168
68.58
27
2.250
3.976
29.74
42
3.S00
9.621
71.97
28
2.333
4.276
31.99
43
3.583
10.085
75.44
29
2.417
4.587
34.31
44
3.667
10.559
78.99
30
2.500
4.909
36.72
45
3.750
11.045
82.62
31
2.583
5.241
39 21
46
3.833
II. 541
86.33
32
2.667
5.585
41.78
47
3.917
12.048
90.13
33
2.750
5.9.40
44.43
48
4.000
12.566
94.00
34
2.833
6.305
47.16
Table Continued, but with the Diameters in Feet
Diam.,
Cubic
U.S.
Diam.,
Cubic
U.S.
Diam.,
Cubic
U.S.
feet
feet
gallons
feet
feet
gallons
feet
feet
gallons
4
12.57
94.0
8
50.27
376.0
20
314.2
2350
y*
14.19
106. 1
H
56.75
424.5
21
346.4
2S9I
H
15.90
119. 0
9
63.62
475. 9
22
380.1
2844
%
17.72
132.5
Vi
70.88
530.2
23
415.5
3108
5
19.64
146.9
10
78.54
587. 5
24
452.4
3384
H
21.65
161. 9
v^
86.59
647.7
25
490.9
3672
H
23.76
177.7
II
95.03
710.9
26
530.9
3971
%
25. 97
194.3
Vz
103.90
777.0
27
572.6
4283
6
28.27
211. 5
12
113. 1
846.1
28
615.8
4606
H
30.68
229.5
13
132.7
992.8
29
660. S
4941
H
33.18
248.2
14
153.9
1152
30
706.9
5288
H
35.79
267.7
15
176.7
1322
31
754.8
5646
7
38.49
287.9
16
201. 1
1504
32
804.3
60x7
H
41.28
308.8
17
227.0
1698
33
855.3
6398
H
44.18
330.5
18
254. S
1904
34
907.9
6792
%
47.17
352. 9
19
283. S
2121
35
962.1
7197
I04
Miilljcnialical Tables
Contents of Linings of Wells
For (lianiclcrs Iwicc a.s j^rcal as ihubc in ihc UiIjIc, for the cuhic yards
of digging, lake out those opjxjsitc one half ol the greater diameter; and
multiply them by 4. Thus, for the cubic yards in each foot of depth of
a well 31 feet in diameter, first take out from the table those opposite the
diameter of 155.4 feet; namely, 6.989. Then 6.989 X 4 = 27.956 cubic
yards required for the 31 feet diameter. But for the stone lining or
walling, bricks or plastering, multiply the tabular quantity opp<Jsitc
//(;// the greater diameter by 2. Thus, the perches of stone walling for
each foot of depth of a well of 31 feet diameter will be 2.073 X 2 =
4.146. If the wall is more or less than one foot thick, within usual
moderate limits, it will generally be near enough for i)ractice to assume
that the number of perches, or of bricks, will increase or decrease in the
same pro[)ortion.
The size of the bricks is taken at 8!4 X 4 X 2 inches; and to be laid
dry, or without mortar. In practice an addition of about 5 per cent
should be made for waste. The brick lining is supposed to be 1 brick
thick, or S'l ins.
Caution. — Be careful to observe that the diameters to be used for
the digging are greater than those for the walling, bricks, or plastering.
For each foot of depth
For each foot of depth
For this
For these three col-
For this
For these three col-
column
umns use the diameter
column
umns use the diameter
use the
in clear of the lining
use the
in clear of the lining
Diam-
diam-
eter of
_
Diam-
eter
diam-
eter of
eter
in
feet
the dig-
Stone
lining
No. of
in
feet
the dig-
Stone
lining
No. of
ging
I foot
bricks
Square
ging
I foot
bricks
Square
thick.
Perches
•
yards of
plaster-
thick.
Perches
in a
lining
yards of
plaster-
lining
Cubic
of 25
I brick
ing
Cubic
of 25
I brick
ing
yards ol
cubic
thick
yards of
cubic
thick
digging
feet
digging
feet
I
.0291
.2513
57
.3491
4
.4654
.6283
227
I 396
H
.045S
.2827
71
■ 4364
H
.S2S4
.6597
241
I 484
Vi
• 0654
.3142
85
■ 5236
H
.5890
.6912
255
I 571
y*
.0891
.3456
99
.6109
H
.6563
.7226
269
1.658
2
.1164
.3770
H4
.6982
s
.7272
.7540
283
I 745
H
.1473
.4084
128
■ 7855
M
.8018
.7854
297
I 833
W
.1818
.4398
142
.8727
'.i
■8799
.8168
311 I 920
y*
.2200
.4712
156
.9600
H
9617
.8482
326 2 007
3
.2618
.5027
170
1.047
6
1.047
.8796
340 209s
H
.3073
SMI
184
I.I3S
14
1. 136
.9111
354 2 182
W
.3563
.5655
198
1.222
Vi
1.329
9425
368 2 269
H
.4091
■5969
212
I 309
94
1.32s .9739 1
382 2.356
A cubic yard = 202 U. S. gallons.
Contents of Linings of Wells
Contents of Linings of Wells
los
For each foot of depth
For each foot of depth
For this
For these three col-
For this
For these three col-
column
umns use the diameter
column
umns use the diameter
use th^
in clear of the lining
use the
in clear of the lining
Diam-
diam-
eter of
Diam-
eter
diam-
eter of
eter
in
feet
the dig-
ging
Stone
Hning
No. of
in
feet
the dig-
ging
Stone
lining
No. of
I ioot
bricks
Square
I foot
bricks
Square
thick.
in a
yards of
thick.
in a
yards of
Perches
lining
plaster-
Perches
lining
plaster-
Cubic
of 25
I brick
ing
Cubic
of 25
I brick
ing
yards of
cubic
thick
yards of
cubic
thick
digging
feet
digging
feet
7
1-425
1.005
396
2.444
16H
7.681
2.168
919
5.673
H
1-529
1.037
410
2.531
'A
7.919
2.199
933
5.760
Vi
1.636
1.068
42s
2.618
9i
8. 161
2.231
948
5. 847
H
1-747
1. 100
439
2.70s
17
8.407
2.262
962
5.934
8
1.862
1.131
453
2.793
'/4
8.656
2.293
976
6.022
M
1.980
1. 162
467
2.880
Vi
8.908
2.325
990
6.109
Vi
2.102
1.194
481
2.967
U
9-165
2.356
1004
6.196
¥i
2.227
I. 225
495
3-054
18
9.425
2.388
1018
6.283
9
2.356
1. 257
509
3 -142
H
9.688
2.419
1032
6.371
M
2.489
1.288
523
3-229
\i
9-956
2.450
1046
6.458
H
2.625
1. 319
538
3.316
%
10.23
2.482
106 1
6.545
94
2.765
1. 351
552
3.404
19
10.50
2.S13
1075
6.633
lo
2.909
1.382
566
3.491
H
10.78
2.545
1089
6.720
y*
3 056
1. 414
580
3 578
M
11.06
2.576
1103
6.807
Vi
3.207
1.445
594
3.665
H
11.35
2.608
1117
6.894
%
3 362
1.477
608
3.753
20
11.64
2.639
1131
6.982
II
3.520
1.508
622
3.840
H
11.93
2.670
1 145
7.069
H
3.682
1-539
637
3.927
li
12.22
2.702
1160
7.156
M
3.847
I-571
651
4.014
H
12.52
2.733
1174
7.243
H
4.016
1.602
665
4.102
21
12.83
2.765
1188
7.. 331
12
4.189
1.634
679
4.189
Vi
13.14
2.796
1202
7.418
Vi
4 365
1.665
693
4.276
Vz
13.45
2.827
1216
7 505
H
4-545
1.696
707
4.364
n
13.76
2.859
1230
7.593
%
4.729
1.728
721
4.451
22
14.08
2.890
1244
7.680
13
4-916
1.759
736
4.538
H
14.40
2.922
1259
7-767
Vi
5-I07
1. 791
750
4.625
1,.',
14.73
2.953
1273
7-854
H
5.301
1.822
764
4.713
H
15.06
2.985
1287
7.942
H
5.500
1. 854
778
4.800
23
15.39
3.016
1301
8.029
14
5. 701
1.885
792
4.887
H
15.72
3.047
1315
8. 116
H
5.907
1. 916
806
4.974
Vi
16.06
3.079
1329
8.203
H
6. 116
1.948
820
5.062
H
16.41
3- no
1343
8.291
?4
6.329
1-979
834
5.149
24
16.76
3.142
1357
8.378
15
6.545
2. on
849
5-236
Vi
17. II
3.173
1372
8.46s
H
6.765 ,.
2.042
863
5 323
li
17.46
3.204
1386
8.552
Vz
6.989
2.073
877
5. 411
%
17.82
3 236
1400
8.640
Vi
7.216
2.10S
891
5. 498
25
18.18
3.267
1414
8.727
i6
7.447
2.136
905
5.585
A cubic yard = 202 U. S. gallons.
Io6 M;illicm;ilit:il T;il»Ics
If pcrihes arc named in a contract, it is necessary, in order to prevent
fruiul, to specify the number of cubic feet contained in the perch; for
slonc-quarricrs have one jierch, stone-masons another, etc. Engineers,
on this account, contract by the cubic yard. The [K-rch should be done
away with entirely; perches of 25 cubic feet X 0.926 = cubic yards; and
cubic yards -r- 0.926 = perches of 25 cubic feet.
CHAPTER III
NATURAL SINES, TANGENTS, ETC.
Sine
The sine of any angle acb or the sine of any circular arc ab is the
perpendicular distance, as, from one end of the arc a to the radius
passing through the other end b of the arc. It
is equal to one-half the chord of the arc abn,
which is twice the arc ab; or the chord of the
arc abn is equal to twice the sine of half the arc,
or twice the sine of ab.
The sine of the angle tcb, if icb equals 90°, is
equal to the radius of the circle.
Cosine
The cosine of an arc ab is the distance cs from
the center of the circle c to the intersection of the
sine as with the radius cb, and is equal to ya or the sine of the arc ta.
But the angle tea is equal to the difference between 90° and the angle
acb; or the difference between the arcs tab and ab; and is the comple-
ment of acb. Hence the cosine of an angle or arc is equal to the sine of
its complement, and vice versa.
Versed Sine
The versed sine of an arc is the distance sb from the foot s of the sine
to the arc at b, measured on the radius cb.
Natiiral Sines, Tangents, etc.
The versed sine of an arc ab is equal to the rise of twice the arc; or
equal to the rise of abn.
Tangent
The tangent bw of an arc ab is the perpendicular distance from the
radius at one extremity of the arc b to the intersection w of the perpen-
dicular bw with the prolongation of a radius drawn through the other
extremity of the arc at a. '
107
io8
M:itll<in:iti( ;il lal/lcs
The Secant
The secant of an arc is the distance cw from the center of the arc to
the intersection of the tangent at U' of the prolonged radius ca.
If the angle Icb equals 90 degrees and lea be the complement of atb,
the sine ya of this complement, its versed sine ly, tangent lo and secant
CO become respectively the cosine, coversed sine, cotangent and co-
secant of the angle acb, and vice versa.
When the radius ab is ecjual to unity the corresiwnding sines, cosines,
tangents, etc., arc called natural sines, cosines, etc.; and the table con-
taining their lengths for different angles is the table of natural sines, etc.
The lengths of the sines, etc., for the arcs of any other circle, whose
radius may be greater or less than i, arc found by multiplying the tabu-
lar values by such radius.
The following table contains ordy natural sines, tangents and secants;
the other lengths may be found for any angle not exceeding 90 degrees
as follows:
Cosine
Versed sine
Coversed sine
Cotangent
Cosecant
Sine
Tangent
Secant
Cosine
= sine of the complement of the given angle.
= I — cosine.
= I — sine.
= tangent of the complement.
= I divided by natural sine.
I cos r ;r
= ■ = = V(i — cos^).
cosec cot
sm
cos
cot
tan
sin
= _L = i^ = Vr^ + tangents
/"; :~::z sm . , ^ i
V (i — sm*) = — = sme X cotangent =
mn see
Cotangent = -r- = —
Versed sine
Coversed sine
Radius
cos _
sm tan
radius — cosine,
radius — sine.
= tangent X cotangent = V sine^ + cosine*.
The formulae for the solution of the right-angled and the oblique-
angled triangle are given; for further information the reader is referred
to works on Trigonometry.
Solution of Oblique-angled Triangles
109
Solution of the Right-angled Triangle
Let A , B and C be the angles of the triangle and a, b and c the sides
opposite those angles respectively.
Then
w^
= sine A, a = c sine A.
<^'^
= cosine A, b = c cosine A.
(3)f
= tangent A, a = b tangent A.
(^)^
= cot^, b=acotA. ^
, . Sin A
(S) Cos^
= tangent^. J;^^
.,, Cos 4
(^^ Sin A
(7) Sine A
(8) Sine A
= cotangent A. ^y^
+ cos2 A = I ■=>
= Vi-cosM. ^°"*'-
(9) Cos A = Vi — sine^^.
Solution of Oblique-angled Triangles
Fig. 38.
Value of any side c is:
_ a sin C _ b sin C
sin A sin 5 *
Value of any angle A :
Sin .4 =
Cosyl =
Tan^ =
a sin C _ a sin B
b — a cos C c — a cos B
c2 4. ^2 _ a2
2 be
asinC
asinB
b — a cos C c — a cos B
no
Mallii-malical Taljics
Natural Sinks, Tangents and Secants
Advancing by lo min.
Deg.
Min.
Sine
Tan-
gent
Secant
Oeg.
Min.
Sine
Tan-
gent
Secant
0
oo
.0000
.0000
I. 0000
so
.1536
.ISS4
i.oiao
lO
0029
.0029
I. 0000
9
00
.1564
.1584
I. 0135
JO
.oos8
.00S8
I. 0000
10
.1593
.1614
I. 0129
JO
.0087
.0087
i.oocm
ao
.1623
.1644
1. 0134
40
.0116
.0116
I .0001
30
.1650
.1673
I. 0139
so
.014s
• 0«4S
I. 0001
40
.1679
.1703
I. 0144
I
00
.OI7S
.01 75
I. 0003
so
.1708
.1733
I. 0149
10
.0204
.0204
I.0003
10
00
.1736
.1763
I.OIS4
20
.0233
.0233
I 0003
10
.1765
.1793
I 0160
30
.0262
.0262
1.0003
30
.1794
.1823
I 0165
40
.0291
.0291
1.0004
30
.1822
.1853
1.0170
50
.0320
.0320
1.0005
40
.1851
.1883
I. 0176
2
00
.0349
• 0349
1.0006
50
.1880
.1914
I 0181
10
.0378
.0378
1.0007
II
00
.1908
.1944
I. 0187
20
• 0407
.0407
1.0008
10
.1937
.1974
1.0193
30
.0436
.0437
1. 00 10
20
.1965
.2004
1.0199
40
.0465
.0466
I. 0011
30
■ 1994
.303S
1.0305
so
.0494
.0495
I. 0012
40
.3022
.ao6s
1.0211
3
00
.0523
.0524
1. 0014
SO
.2051
.309s
I. 0217
10
.OS52
.OSS3
1. 0015
12
00
.2079
.2136
1.0223
20
.0581
.0582
1. 0017
10
.2108
.2156
1.0230
30
.0610
.0612
1. 0019
20
.2136
.2186
1.0236
40
.0640
.0641
I. 0021
30
.2164
.2217
1.0243
SO
.0669
.0670
1.0022
40
.2193
.2247
1.0249
4
00
.0698
.0699
1.0024
SO
.3321
.2378
1.0256
10
.0727
.0729
1.0027
13
00
.3350
.3309
1.0263
20
.o7S6
.0758
1.0029
10
.2278
.23.W
1.0270
30
.078s
.0787
1. 0031
20
.2306
.2370
1.0277
40
.0814
.0816
1.0033
30
.2334
.2401
1.0284
SO
.0843
.0846
1.0036
40
.2363
.2432
I 0291
5
00
.0872
.0875
1.0038
50
.2391
.2462
1.0299
10
.0901
.0904
1.0041
14
00
.2419
.2493
1.0306
20
.0929
.0934
1.0043
10
.2447
.2524
I 0314
30
.0958
.0963
1.0046
20
.2476
.2555
I. 0321
40
.0987
.0992
1.0049
30
.2504
.2586
1.0329
SO
.1016
.1022
I. 0052
40
.2532
.2617
1.0337
6
00
' .1045
.losi
i.ooss
SO
.2560
.2648
1.034s
10
.1074
.1080
1.0058
15
00
.3588
.2679
1.03S3
20
.1103
.1110
I. 0061
10
.3616
.2711-
I. 0361
30
.1132
.1139
1.0065
20
.3644
.2742
1.0369
40
.1161
.1169
1.0068
30
.2672
.2773
1.0377
SO
.1190
.1198
1.0072
40
.3700
.2805
1.0386
7
00
.1219
.1228
I. 007s
SO
.3728
.2836
1.0394
10
.1248
.1257
1.0079
16
00
.2756
.2867
1 0403
20
.1276
.1287
1.0082
10
.2784
.2899
1.0412
30
.130S
.1317
1.0086
20
.3812
.2931
1.0421
40
.1334
.1346
1.0090
30
.2840
.2962
1.0429
SO
. 1363
.1376
1.0094
40
.3868
.2994
1.0439
8
00
.1392
.140S
1.0098
SO
.3896
.3026
I .0448
10
.1421
.I43S
I. 0102
17
00
.2934
.3057
I 04S7
30
.1449
.1465
I. 0107
10
.2952
.3089
1.0466
30
.1478
.149s
I.OIII
30
.2979
.3121
I .0476
40
.1507
.IS24
I.0II6
30
■ 3007
.3153
1.0485
Natural Sines, Tangents and Secants
Natural Sines, Tangents
AND Secants — {Continued)
Deg.
Min.
Sine
Tan-
gent
Secant
Deg.
Min.
Sine
Tan-
gent
Secant
40
■ 303s
.3185
1.049s
so
.4514
.5059
I. 1207
SO
.3062
.3217
1.0505
27
00
.4540
■ S095
I . 1223
l8
00
■ 3090
■ 3249
I. 0515
10
• 4566
.5132
I . 1240
10
.3118
.3281
I 0525
20
■ 4592
■ 5169
I. 1257
20
.3145
• 3314
1.0535
30
.4617
.5206
I. 1274
30
.3173
.3346
I.OS4S
40
.4643
.5243
1.1291
40
.3201
.3378
I 0555
SO
.4669
.5280
I . 1308
SO
.3228
.3411
1.0566
28
00
.4695
.5317
I . 1326
19
00
.3256
.3443
1.0576
10
.4720
• 5354
I • 1343
10
.3283
.3476
1.0587
20
.4746
5392
1.1361
20
.3311
.3508
1.0598
30
.4772
.5430
I ■ 1379
30
.3338
.3S4I
1.0608
40
.4797
.5467
I . 1397
40
.3365
.3S74
1.0619
SO
.4823
.5505
1.1415
SO
.3393
.3607
I. 0631
29
00
.4848
.5543
I -1434
20
00
.3420
.3640
1.0642
10
.4874
.5581
I. 1452
10
.3448
.3673
I 0653
20
.4899
.5619
1.1471
20
.3475
• 3706
1.0665
30
.4924
.5658
I . 1490
30
.3502
.3739
1.0676
40
.4950
.5696
I . 1509
40
.3S29
.3772
1.0688
50
.4975
.5735
I . 1528
SO
.3SS7
.380s
1.0700
30
00
.5000
.5774
I . 1547
31
00
.3S84
.3839
1.0711
10
.5025
.5812
I . 1566
10
.3611
.3872
1.0723
20
.5050
.5851
I . 1586
20
.3638
.3906
1.0736
30
.5075
.5890
I. 1606
30
.3665
.3939
1.0748
40
.5100
.5930
I. 1626
40
.3692
.3973
1.0760
SO
.5125
.5969
I. 1646
so
.3719
.4006
1.0773
31
00
• 5150
.6009
I. 1666
32
00
.3746
.4040
1.0785
10
.5175
.6048
1 . 1687
10
.3773
.4074
1.0798
20
.5200
.6088
I. 1707
20
.3800
.4108
1.0811
30
.5225
.6128
I. 1728
30
.3827
.4142
1.0824
40
.5250
.6168
I. 1749
40
.38S4
.4176
1.0837
SO
.5275
.6208
I. 1770
so
.3881
.4210
1.0850
32
00
.5299
.6249
I . 1792
23
00
.3907
.424s
r.0864
10
.5324
.6289
1.1813
10
.3934
.4279
1.0877
20
.5348
.6330
I. 1835
20
.3961
.4314
I. 0891
30
.5373
.6371
I. 1857
30
.3987
.4348
1.0904
40
5398
.6412
I. 1879
40
.4014
.4383
I. 0918
50
.5422
.6453
1.1901
so
.4041
.4417
1.0932
33
00
.5446
.6494
I . 1924
24
00
.4067
.4452
1.0946
10
■ 5471
.6536
I . 1946
10
.4094
.4487
I. 0961
20
.5495
.6577
I. 1969
20
.4120
• 4522
I 0975
30
• 5519
.6619
r.1992
30
.4147
.4557
1.0989
40
• 5544
.6661
I . 201S
40
.4173
.4592
I. 1004
SO
.5568
.6703
I . 2039
SO
.4200
.4628
1.1019
34
00
.5592
.6745
1.2062
25
00
.4226
.4663
I . 1034
10
.5616
.6787
I . 2086
10
• 4253
.4699
I . 1049
20
.5640
.6830
1.2110
20
.4279
.4734
I . 1064
30
.5664
.6873
I. 2134
30
.4305
.4770
I . 1079
40
.5688
.6916
I. 2158
40
.4331
.4806
I. 1095
SO
.5712
.6959
I. 2183
50
.4358
.4841
I.IIIO
35
00
■ 5736
.7002
I . 2208
36
00
.4384
.4877
1.1126
10
.5760
.7046
I . 2233
10
.4410
.4913
1.1142
20
.5783
.7089
1.2258
20
.4436
■ 4950
1.1158
30
.5807
.7133
1.2283
30
.4462
.4986
1.1174
40
.5831
.7177
1.2309
40
.4488
.5022
1.1190
SO
.5854
.7221
I. 2335
iia
Matlicmatir.il 'I'aliles
Natural Sines
, Tangents
AND Secants
— (Continued]
Deg.
Min.
Sine
Pan-
sent
Secant
Deg.
Min.
Sine
Tan-
gent
Secant
36
00
.S878
7265
I . 2361
10
.7092
i.oosS
I 4183
10
.S90I
7310
1.3387
30
.7112
1.0117
1.4225
20
.S92S
7355
1.2413
30
.7133
1.0176
1.4267
30
.5948
7400
1.2440
40
.7153
1.0335
I. 4310
40
.5972
7445
I . 2467
SO
.7173
1.039s
1 4352
so
•599S
7490
1.2494
46
00
.7193
I.03SS
1.4396
37
00
.6018
7536
I. 2521
10
.7214
I .0416
1.4439
10
.6041
7581
I. 2549
20
.7234
1.0477
1.4483
20
.6065
7627
I.2S77
30
.7254
1 0S.J8
1.4527
30
.6088
7673
1.2605
40
.7274
1.0S99
I. 4572
40
.6111
7720
1.26.33
so
.7294
1. 0661
1.4617
SO
.6134
7766
I. 2661
47
00
.7314
1.0724
1.4663
38
00
.6157
7813
1.2690
10
.7333
1.0786
1.4709
10
.6180
7860
1.2719
20
.7353
1.0850
1 4755
30
.6202
7907
1.2748
30
.7373
1 0913
1.4802
30
.6225
7954
1.2778
40
.7392
1 0977
1.4849
40
.6248
8002
1.2808
SO
.7412
1.1041
1 4987
SO
.6271
80S0
1.2837
48
00
.7431
I. 1106
1.4945
39
00
.6293
8098
1.2868
10
.7451
1.1171
I 4993
10
.6316
8146
1.2898
20
.7470
I. 1237
1.S042
20
.6338
8195
1.2929
30
.7490
I. 1303
I S092
30
.6361
8243
1.2960
40
.7509
1.1369
1 5141
40
.6383
8292
I. 2991
SO
.7528
1.1436
1.5192
SO
.6406
8342
1.3022
49
00
.7547
1. 1504
1.5243
40
00
.6428
8391
I 3054
10
.7566
I. 1571
1.5294
10
.6450
8441
1.3086
20
.7585 1 I. 1640
1 5345
20
.6472
8491
1.3118
30
.7604 1 1.1708
I 5398
30
.6494
8541
1.3151
40
.7623
I 17-8
1.5450
40
.6517
8391
I. 3184
50
.7642
I . 1847
I.S504
SO
.6539
8642
I. 3217
50
00
.7660
1.1918
I.SS57
41
00
.6561
8693
1.3250
10
.7679
1.1988
1.5611
10
.6583
8744
1.3284
20
.7698
1.2059
1.5666
20
.6604
8796
I. 3318
30
.7716
1.2I3I
1.5721
30
.6626
8847
1.3352
40
.7735 1.2203
1.5777
40
.6648
8899
1.3386
50
.7753
I . 2276
1.5833
SO
.6670 ,
8932
I. 3421 1
51
00
.7771
1.2349
1.5890
42
00
.6691 ;
9004
1.3456
10
.7790
I 2423
1 5948
10
.6713
9057
1.3492
30
.7808
1.2497
1.6005
20
.6734
91 10
1.3527
30
.7826
1.2572
I 6064
30
.6756
9163
1.3563
40
.7844
1.2647.
I. 6123
40
.6777
9217
1.3600
SO
.7862
1 2723
1.6183
SO
.6799
9271
I 3636
52
00
.7880
1 2799
1.6243
43
00
.6820
9325
1.3673
10
.7898
I . 2876
1.6303
10
.6841
9380
1.3711
20
.7916
1.2954
1.6365
20
.6862
9435
1.3748
30
.7934
1 3032
I 6427
30
.6884
9490
1.3786
40
.7951
1.1311
1.6489
40
.6905
9545
1.3824
50
.7969
1 3190
I 6553
so
.6926
9601
1.3863
S3
00
.7986
1.3270
I. 6616
44
00
.6947
9657
1.3902
10
.8004
1 3351
I 6681
10
.6967
9713
I. 3941
20
.8021
1.3432
1.6746
20
.€988
9770
1.3980
30
.8039
1 3514
I 6812
30
.7009
9827
1.4020
40
.8056
I.3S97
1.6878
40
.7030
9884
I. 4061
50
.8073
1.3680
1.694s
SO
.7050
9942
1 . 4101
54
00
.8090
I 3764
1.7013
4S
00
.7071 I
0000
I. 4142
10
.8107
1.3848
I. 7081
Natural Sines, Tangents and Secants
"3
Natural Sines, Tangents and Secants — (Conlinued)
Deg.
Min.
Sine
Tan-
gent
Secant
Deg.
Min.
Sine
Tan-
gent
Secant
20
.8124
1.3924
1.7151
30
■ 8949
2.00S7
2.2412
30
.8141
I . 4019
I. 7221
40
.8962
2.0204
2.2543
40
.8158
I. 4106
I. 7291
50
.8975
2.03S3
2.2677
50
.8175
1.4193
1.7362
64
00
.8988
2.0503
2.2812
55
00
.8192
r.4281
1.7434
10
.9001
2.o6s5
2.2949
10
.8208
I ■ 4370
I . 7507
20
.9013
2.0809
2.3088
20
.8225
I . 4460
I. 7581
30
.9026
2.096s
2.3228
30
.8241
I.4S50
1.765s
40
.9038
2.1123
2.3371
40
.82S8
I. 4641
I . 7730
SO
.9051
2.1283
2.3515
SO
.8274
I . 4733
I . 7806
6S
00
.9063
2.1445
2,3662
56
00
.8290
1.4826
1.7883
10
.9075
2. 1609
2.3811
10
.8307
1.4919
1.7960
20
.9088
2.177s
2.3961
20
.8323
I . S013
1.8039
30
.9100
2.1943
2.4114
30
.8339
1.S108
1.8118
40
.9112
2.2113
2.4269
40
.8355
I.S204
I. 8198
50
.9124
2 . 2286
2.4426
50
.8371
I. 5301
1.8279
66
00
.9135
2.2460
2.4586
57
00
.8387
1.5399
I. 8361
10
.9147
2.2637
2.4748
10
.8403
1.5497
1.8443
20
.9159
2.2817
2.4912
20
.8418
1-5597
1.8527
30
.9171
2 . 2998
2.5078
30
.8434
1.5697
I. 8612
40
.9182
2.3183
2.5247
40
.8450
1.5798
I . 8699
50
.9194
2.3369
2.5419
50
.8465
1.5900
1.8783
67
00
.920s
2. 3559
2.5593
58
00
.8480
1.6003
I. 8871
10
.9216
2.3750
2.5570
10
.8496
I. 6107
1.8959
20
.9228
2.3945
2.5949
20
.8511
I. 6213
1.9048
30
.9239
2.4141
2.6131
30
.8526
I. 6319
1.9139
40
.9250
2.4342
2.6316
40
.8542
1.6426
1.9230
SO
.9261
2.4545
2.6504
50
.8557
1.6534
1.9323
68
00
.9272
2.4751
2.669s
59
00
.8572
I . 6643
I. 9416
10
.9283
2.4960
2,6888
10
.8587
1.6753
1.9511
20
.9293
2.5172
2,7085
20
.8601
1.6864
1.9606
30
.9304
2.5386
2.728s
30
.8616
1.6977
1 . 9703
40
.9315
2.560s
2.7488
40
.8631
1.7090
I . 9801
50
.9325
2.5826
2.769s
50
.8646
1.7205
1.9900
69
00
.9336
2.6051
2.7904
60
00
.8660
I. 7321
2.0000
10
.9346
2.6279
2.8117
10
.8675
1.7437
2.0101
20
.9356
2.6511
2.8334
20
.8689
1.7556
2.0204
30
.9367
2.6746
2.8555
30
.8704
1.7675
2.0308
40
.9377
2.698s
2.8779
40
.8718
r.7796
2.0413
50
.9387
2.7228
2.9006
SO
.8732
I. 7917
2.0S19
70
00
.9397
2.7475
2.9238
61
00
.8746
I . 8040
2.0627
10
.9407
2.7725
2.9474
10
.8760
1.816s
2.0736
20
.9417
2.7980
2.9713
20
.8774
I. 8291
2.0846
30
.9426
2.8239
2.9957
30
.8788
I. 8418
2.0957
40
.9436
2.8502
3.0206
40
.8802
1.8546
2 . 1070
50
.9446
2,8770
3.0458
SO
.8816
1.8676
2.1185
71
00
.9455
2.9042
3.0716
62
00
.8829
1.8807
2.1301
10
.9465
2.9319
3.0977
10
.8843
1.8940
2.1418
20
.9474
2.9600
3.1244
20
.8857
1.9074
2.1537
30
.9483
2.9887
3.151S
30
.8870
I. 9210
2.1657
40
.9492
3.0178
3.1792
40
.8884
1.9347
2.1786
50
.9502
3.047s
3.2074
50
.8897
1.9486
2.1902
72
00
9511
3.0777
3.2361
63
00
.8910
I . 9626
2 . 2027
10
.9520
3.1084
3.2653
10
.8923
1.9768
2.2IS3
20
.9528
3.1397
3.2951
20
.8936
I. 9912
2.2282
30
.9537
3.1716
3.3255
114 M;illKtii.ili(iil Tahles
Natural Sines, Tangents and Secants — {Continued)
Deg.
Min.
Sine
Tan-
gent
3.3041
Secant
Dcg.
Min.
Sine
Tan-
gent
Secant
40
.9540
3 3S6s
30
.9890
6 6913
6.76SS
SO
• 9SSS
3.2371
33881
40
.9894
6.8269
6.8998
73
oo
.9563
3 2709
3.4303
SO
■ 9899
6 9683
70396
lO
.957.2
3 3052
3 4532
83
00
.9903
7.IIS4
7 I8S3
ao
.9580
3.3402
3.4867
10
.9907
7-2687
7.3372
*>
.9588
3.37S9
3 5309
20
99"
7-4287
7 49S7
40
.9596
3.4124
3 5559
30
.9914
7 S9S8
76613
so
.9605
3 4 195
3 5915
40
9918
7 7704
7 8344
74
00
.9613
3.4874
3.6280
SO
.9922
7 9.530
8 0156
10
.9621
3.5261
3.6652
83
00
.9925
8.1443
8 30SS
30
.9628
3.5656
3.7032
10
.9929
8 J150
8 4047
30
.9636
3 6059
3.7420
30
.9933
8.5555
8 6138
40
.9644
3.6470
3 7817
30
• 9936
8.7769
8.8337
SO
.9652
3.6891
3.8222
40
.9939
9.0098
9 0652
75
00
.9659
3.7321
38637
50
•9943
9 2SS3
9 3093
10
9667
3.7760
3.9061
84
00
9945
9 S144
9 5668
20
.9674
3 8208
3.9495
10
.9948
9 7882
9 8391
30
.9681
3.8667
3.9939
20
9951
10.0780
10.1275
40
.9689
3.9136
4 0394
30
• 9954
10 3854
10 4334
SO
.9696
3.9617
4.0859
40
9957
10.7119
10 758s
76
00
.9703
4.0108
4.1336
50
-9959
1I.OS94
II 1045
10
.9710
4.0611
4 . 1824
85
00
-9963
"430
11.474
20
.9717
4.1126
4.2324
10
.9964
11.826
11 868
30
.9724
4.1653
4.2837
30
.9967
12.251
12.291
40
.9730
4.2193
4.3362
30
.9969
12 706
13.745
SO
.9737
4.2747
4 3901
40
.9971
13 197
13.23s
77
00
.9744
4-3315
4. 4454
SO
.9974
13 737
13 763
10
.9750
4 3897
4.S022
86
00
.9976
14 301
14 336
20
.9757
4 4494
4.5604
10
-9978
14 924
14 9S8
30
.9763
4.5107
4.6202
20
-9980
IS 605
15 637
40
.9769
4.5736
4.6817
30
.9981
16.350
16.380
50
.9775
4.6382
4-7448
40
.9983
17.169
17.198
78
00
.9781
4.7046
4-8097
50
.9985
18.07s
18.103
10
.9787
4.7729
4-8765
87
00
-9986
19 081
19.107
20
.9793
4.8430
4-9452
10
-9988
20.206
20 230
30
.9799
4.9152
S 0159
20
-9989
21.470
21.494
40
.980s
4.9894
S.0886
30
-9990
22.904
22 926
50
.9811
S.0658
5. 1636
40
-9992
24 543
24.562
79
00
.9816
5. 1446
5.2408
50
-9993
26 432
26.451
10
.9822
5-2257
s 320s
88
00
-9994
38.636
28.654
20
.9827
5 3093
5 - 4026
10
.9995
31.243
31 258
30
.9833
5. 3955
5.4874
20
-9996
34 368
34 382
40
.9838
5.484s
5.5749
30
-9997
38.188
38.203
50
.9843
5. 5764
5.6653
40
9997
42 964
42 976
8o
00
.9848
5.6713
5. 7588
50
-9998
49 104
49 "4
10
.9853
5. 7694
5.8554
89
00
-9998
57.290
57.299
20
.9858
5.8708
5. 9554
10
.9999
68.750
68.757
.30
.9863
5. 9758
5 0589
20
-9999
8S 940
85 946
40
.9868
6.0844
6 1661
30
I 0000
114 589
"4 593
SO
.9872
6.1970
6.2772
40
1. 0000
171 885
171.888
8l
00
.9877
6.3138
6.3925
SO
I .0000
343 774
343 775
10
.9881
6.4348
6.SI2I
90
00
I. 0000
Infi-
Infi-
30
.9886
6.S606
6.6363
nite
nite
Approximate Measurement of Angles
115
Approximate Measurement of Angles
(i) The four fingers of the hand, held at right angles to the arm
and at arm's length from the eye, cover about 7 degrees; and an angle
of 7 degrees corresponds to about 12.2 feet in 100 feet; or to 36.6 feet in
100 yards; or to 645 feet in a mile.
(2) By means of a two-foot rule, either on a drawing or between
distant objects in the field. If the inner edges of a common two-foot
rule be opened to the extent shown in the column of inches, they will be
inclined to each other at the angles shown in the column of angles.
Since an opening of J'i inch (up to 19 inches or about 105 degrees) corre-
sponds to from about 5^^ degree to i degree, no great accuracy is to be
expected, and beyond 105 degrees still less, for the liability to error then
increases very rapidly as the opening becomes greater. Thus, the last
^ inch corresponds to about 12 degrees.
Angles for openings intermediate of those given may be calculated to
the nearest minute or two, by simple proportion, up to 23 in-^hes of
opening, or about 147 degrees.
Table of Angles Corresponding to Openings of a 2-foot
Rule. (Original.) Trautwine.
Ins.
Deg. Min.
Ins.
Deg.
Min.
Ins.
Deg.
Min.
Ins.
Deg. Min.
H
I 12
3'/^
16
46
6H
32
40
10
49 IS
I 48
17
22
33
17
49 54
H
2 24
%
17
59
7
33
54
M
50 34
3 00
18
35
34
33
51 13
%
3 36
4
19
12
H
35
10
'/i
SI 53
4 II
19
48
35
47
52 33
I
4 47
H
20
24
H
36
25
%
53 13
S 23
21
37
3
S3 S3
H
S S8
\<i
21
37
H
37
41
II
54 34
6 34
22
13
38
19
55 14
Vi
7 10
?4
22
50
8
38
57
H
55 55
7 46
23
27
39
35
56 35
H
8 22
5
24
3
H
40
13
H
57 16
8 s8
24
39
40
51
57 57
2
9 34
V^
25
16
Vi
41
29
?4
58 38
10 10
25
53
42
7
59 19
H
10 46
Vi
26
39
%
42
46
12
60 00
II 22
27
7
43
24
60 41
\<i
II 58
H
27
44
9
44
3
M
61 23
12 34
28
21
44
42
62 5
5-4
13 10
6
28
58
y^
45
21
K'
62 47
13 46
29
35
45
59
63 28
3
14 22
}i
30
II
1,4
46
38
%
64 II
14 S8
30
49
47
17
64 53
M
15 34
H
31
26
54
47
56
13
6S 35
16 10
32
3
48
35
66 18
ii6
Matlicniuticul Tahlcs
TaBLLS of AngUCS COKKICSIHJNUING Tii (U-\ MV..S OP A 2-FOOT
Rule — {CotUini.'
(3) With the same table, using feet instead of inches. —
From any i)oinl measure 12 Jcct toward* each object and place marks.
Measure the distance in feci between these marks. Suppose the first
column in the table to be feci instead of inches. Then opposite the
distance in feel will be the angle.
V& foot = 1.5 inches.
1 in. = .083 ft.
2 ins. = .167 ft.
3 ins. = .25 ft.
4 ins. = .^2,3 ft-
5 ins. = .416 ft.
6 ins. = .5 ft.
7 ins. = .583 ft.
8 ins. = .667 ft.
9 ins. = .75 ft.
10 ins. = .833 ft.
11 ins. = .917 ft.
12 ins. = 1.0 ft.
(4) Or, measure toward* each object 100 or any other number
of feet and |)lace marks. Measure tlie distance in feet between the
marks. Then
half the distance between the marks
Sine of half _
the angle the distance measured toward one of the objects
Find this sine in the table, etc.; take out the corresponding angle and
multiply it by 2.
• If it is inconvenient to measure toward the objects, measure directly from them.
Tapers per Foot and Corresponding Angles
117
Tapers per Foot and Corresponding Angles
Computed by E. M. Willson
Taper
Included
Angle with
Taper
Included
Angle with
per
foot
angle
center line
per
foot
angle
center line
Deg.
Min
.Sec.
Deg.
Min
. Sec.
Deg.
Min
. Sec.
Deg. Min
. Sec.
Hi
0
4
28
0
2
14
2H
II
18
10
5 39
5
Hi
0
8
S8
0
4
29
2V1
II
53
36
5 56
48
Me
0
17
54
0
8
57
2H
12
29
2
6 14
31
9^2
0
26
52
0
13
26
2%
13
4
24
6 32
12
H
0
35
48
0
17
54
2',<i
13
39
42
6 49
SI
^2
0
44
44
0
22
22
3
14
15
0
7 7
30
^6
0
S3
44
0
26
52
3'/i
14
SO
14
7 25
7
H2
2
34
0
31
17
3M
15
25
24
7 42
42
Vi
II
36
0
35
48
35i
16
0
34
8 0
17
%2
20
30
0
40
IS
3K2
16
35
40
8 17
SO
Me
29
30
0
44
45
35i
17
10
40
8 35
20
>'/i2
38
22
0
49
II
3%
17
45
40
8 52
50
?^
47
24
0
53
42
zH
18
20
34
9 10
17
13/^2
56
24
0
58
12
4
18
55
28
9 27
44
Me
2
5
18
2
39
4^6
19
30
18
9 45
9
15^2
2
14
16
7
8
4H
20
S
2
10 2
31
H
2
23
10
II
35
4?i
20
39
44
10 19
52
1%2
2
32
4
16
2
4'/^
21
14
2
10 37
I
. 916
2
41
4
20
32
45^
21
48
54
10 54
27
1%2
2
50
2
25
I
4?4
22
23
22
II II
41
^6
2
59
42
29
51
m
22
57
48
II 28
54
2)42
3
7
56
33
58
S
23
32
12
II 46
6
iHe
3
16
54
38
27
sH
24
6
28
12 3
14
m2
3
25
SO
42
SS
sM
24
40
42
12 20
21
%
3
34
44
47
22
5?i
25
14
48
12 37
24
m2
3
43
44
SI
52
sH
25
48
48
12 54
24
Wi&
3
52
38
56
19
SH
26
22
52
13 II
26
n^2
4
I
36
2
0
48
SM
26
56
46
13 28
23
H
4
10
32
2
5
16
Sji
27
30
34
13 45
17
2%2
4
19
34
2
9
47
6
28
4
2
14 2
I
1^6
4
28
24
2
14
12
61/6
28
37
58
14 18
59
3^2
4
37
20
2
18
40
6W
29
II
34
14 35
47
I
4
46
18
2
23
9
6?i
29
45
18
14 52
39
iHe
S
4
12
2
32
6
6H
30
18
26
15 9
13
l^
S
21
44
2
40
52
65 g
30
51
48
IS 2S
54
iMe
S
39
54
2
49
57
6M
31
25
2
15 42
31
iVi
5
57
48
2
58
54
e;;^
31
58
10
IS 59
5
lVi6
6
IS
38
3
7
49
7
32
31
12
16 IS
36
iH
6
33
26
3
16
43
7'/6
33
4
8
16 32
4
iMe
6
51
20
3
25
40
7'/4
33
36
40
16 48
20
iH
7
9
10
3
34
35
7?6
34
9
50
17 4
SS
I9i6
7
26
58
3
43
29
7I/2
34
42
30
17 21
IS
i5^
7
44
48
3
52
24
75i
35
IS
2
17 37
31
I»H6
8
2
38
4
I
19
7?4
35
47
32
17 S3
46
1%
8
20
26
4
10
13
7^/i
36
19
54
18 9
57
I'Me
8
38
16
4
19
8
8
36
52
12
18 26
6
I'/i
8
S6
2
4
28
I
%H
37
24
22
18 42
II
I' 5^6
9
13
SO
4
36
55
8M
37
56
26
18 s8
13
2
9
31
36
4
45
48
8?i
38
28
16
19 14
8
2«
10
7
10
5
3
35
8J.i
39
0
16
19 30
8
2I4
10
42
42
5
21
21
8?i
39
31
52
19 45
S6
1 1 8 MatliL-maliciil I'ablcs
Tapers per Foot and Corresponding Angles — (jContinued)
Taper
Includcfl
Angle with
Tupcr
Included
Angle with
foot
angle
center line
per
foot
angle
center line
Deg. Min. Sec.
Deg. Min. Sec.
Deg. Min. Sec.
Deg. Min. Sec.
8?4
40 3 42
20 I SI
loM
46 45 24
23 22 42
VA
40 35 i6
20 17 38
10)^6
47 IS 32
23 37 46
9
41 6 44
20 33 22
io5h
47 45 30
23 52 45
9V6
41 38 28
20 49 14
IO?4
48 15 24
24 7 42
9W
42 9 18
21 4 39
ir,:^
1« 15 10
24 22 35
m
42 40 26
21 20 13
1 1
II 48
24 37 24
9W
43 11 24
21 35 42
I i -
; . 14 20
24 52 10
9H
43 42 20
21 SI 10
II' 1
50 13 46
25 6 S3
9%
44 13 6
22 6 33
11%
SO 43 4
25 21 32
9^/6
44 43 48
22 21 54
Il'-i
SI 12 14
25 36 7
10
45 14 22
22 37 II
n'--
SI 41 18
25 SO 39
10^
45 44 52
22 52 26
III
52 10 16
26 5 8
loH
46 15 46
23 7
1 i'h
52 39 2
26 19 31
CHAPTER IV
DIFFERENT STANDARDS FOR WIRE GAUGES
Different Standards for Wire Gauges in Use in the
United States
Dimensions of sizes in decimal parts of an inch
1^
H.. S. & Co.
"F.&G."
steel music
wire gauge
U.S.
standard
for plate
American or
Brown &
Sharpe
"III
>J 0 U3
m
3
0 M
^ a
2; &
000000
.46875
.464 .
000000
00000
.4375
.432 .
00000
0000
.40625
;46"'
.454
.3938
.400
0000
000
.375
.40964
.425
.3625
.372
000
00
.0087
.34375
.3648
.38
.3310
.348 .
00
0
.0093
0578
.3125
.32486
.34
.3065
.324 .
0
I
.0098
0710
.28125
.2893
.3
.2830
.300
227
I
2
.0106
0842
.265625
.25763
.284
.2625
.276
219
2
3
.0114
0973
.25
.22942
.259
.2437
.252
212
3
4
.0122
1 105
.234375
.20431
.238
.2253
.232
207
4
5
.0138
1236
.21875
.18194
.22
.2070
.212
204
5
6
.0157
1368
. 20312s
. 16202
.203
.1920
.192
201
6
7
.0177
isoo
.1875
.14428
.18
.1770
.176
199
7
8
.0197
1631
.171875
.12849
.16s
.1620
.160
197
8
9
.0216
1763
.15625
.11443
.148
.1483
.144
194
9
10
.0236
1894
. 140625
. IOI89
.134
.1350
.128
191
10
II
.0260
2026
.125
.090742
.12
.1205
.116
188
II
12
.0283
2158
.I0937S
.080808
.109
.loss
.104
i8s
12
13
.0303
2289
.09375
.071961
.095
.091S
.092
182
13
14
.0323
2421
.078125
.064084
.083
.0800
.080
180
14
15
.0342
2S52
.0703125
.057068
.072
.0720
.072
178
15
16
.0362
2684
.0625
.05082
.06s
.0625
.064
175
16
17
.0382
2816
.05625
.045257
.058
.0540
.056
172
17
18
.04
2947
.05
.040303
.049
.0475
.048
168
18
19
.042
.04375
.03589
.042
.0410
.040
164
19
20
.044
3210
.0375
.031961
.035
.0348
.036
161
20
21
.046
.034375
.028462
.032
.03175
.032
157
21
22
.048
3474
.03125
.025347
.028
.0286
.028
155
22
23
.051
.028125
.022571
.025
.0258
.024
153
23
24
.oS!>
3737
.02s
.0201
.022
.0230
.022
ISI
24
25
.OS9
.021875
.0179
.02
.0204
.020
148
25
26
.063
4000
.01875
.01594
.018
.0181
.018
146
26
27
.067
.0171875
.01419s
.016
.0173
.0164
143
27
28
.071
4263
.015625
.012641
.014
.0162
.0149
139
28
119
I20
Materials
Different Standards for Wirk Gauges in Use in thk
United States — {/Continued)
29
30
31
32
33
34
3S
36
37
38
39
40
.074
.078
.082
.086
•1^
.0140625
01 25
0109375
.01015625
.009375
00859375
.0078125
0070312s
.006640625
.00625
.011257
.0I002S
.008928
•0079s
.00708
.006304
.005614
•oos
•004453
.003965
.003531
003144
.1"!
.£fc
i c !£
3:5
0x50
0141
0132
0128
0118
0104
009s
C090
.2 3
.0136
.0124
.0116
.0108
.0100
.00921
.0084I
.0076
.0068J
.0060
.0052
.0048
.134
.127
.120
• IIS
.112
.110
.108
.106
.103
.101
099
097
•3 6
n
BiRMINGH.AM GaUGE FOR ShEET BrASS, SiLVER, GoLD AXD ALL
Metals except Steel and Iron
Thick-
Thick-
Thick-
Thick-
Thick-
Thick-
No.
ness,
No.
ness,
No.
ness,
No.
ness,
No.
ness,
No.
ness,
inch
inch
inch
inch
inch
inch
I
.004
7
•ois
13
.036
19
.064
25
.095
31
.133
2
.005
8
.016
14
.041
20
.067
26
.103
32
143
3
.008
9
.019
^S
.047
21
.072
27
.113
33
.145
4
.010
10
.024
16
.051
22
•074
28
.120
34
.148
5
.012
II
.029
19
■OS7
23
.077
29
.124
35
.158
6
.013
12
.034
18
.061
24
.082 1
30_
.126
36
.167
C; auges Gener.ally used by Mills in the U. S. Rolling Sheet
Iron. (Vary Slightly from Birmingham Gauge).
No.
Pounds per
square foot
No.
Pounds per
square foot
No.
Pounds per
square foot
No.
Pounds per
square foot
I
12 50
8
6.86
IS
2.8r
22
I 25
2
12.00
9
6.24
16
2. so
23
1. 12
3
II 00
10
5.62
17
2.18
24
1. 00
4
10.00
11
5. 00
18
1.86
25
.90
S
8.75
12
4.38
19
1.70
26
.80
6
8 12
13
3.75
20
1.54
27
.72
7
7.50
14
3.12
21
1.40
28
.64
Band and Hoop Iron Weights per Lineal Foot
Band and Hoop Iron Weights per Lineal Foot
No. of
Width ia inches
gauge
H
%
'A
I
m
iH
m
iVz
m
6
8
10
lbs.
4231
3581
2929
lbs.
.5078
.4296
.3515
.2734
.1953
.1562
.1367
.1171
.1074
.0976
.0877
.0781
.0705
bs.
5924
5013
4101
bs.
674
5729
4689
lbs.
762
64s
527
469
41
352
293
264
234
20s
176
161
146
bs.
846
716
S86
521
4S6
391
326
293
26
229
195
179
165
bs.
931
788
64s
573
501
430
358
322
286
251
21S
197
179
I
lbs.
016
8S9
703
62s
547
469
391
352
313
273
234
215
19s
lbs.
1. 10
.931
.762
.677
■592
.508
.423
.381
.339
.269
■ 254
12
13
2278
3190
3645
14
15
1628
2278
2604
i6
17
18
19
20
21
1302
1 139
0976
0895
0814
0731
0651
0588
1822
1595
1367
1253
1 139
1023
091 1
0822
2083
1822
1562
1432
1302
1 169
104 1
0939
23
No. of
Width in inches
gauge
1%
1%
2
2H
2I/4
2%
2^2
2%
2H
2^
4
6
8
9
10
II
12
13
14
IS
16
17
18
lbs.
1-367
1. 185
1.003
.914
.820
.729
.638
.547
.456
.410
.36s
■ 319
.273
lbs.
1.465
1.270
1.074
.977
.897
.781
.684
.586
.488
.439
.391
.342
.293
lbs.
1.562
1. 354
1. 146
1.042
.938
.833
.729
.62s
.521
.469
.417
.365
.313
lbs.
1.660
1.439
1. 217
1. 107
.996
.88s
• 775
.664
.553
.498
.443
lbs.
1.758
1.523
1.289
1. 172
1.055
.938
.820
.703
.586
.527
.469
lbs.
1.855
1.608
1. 361
1.237
1. 113
.990
.866
.742
.618
.557
.495
lbs.
1.953
1.693
1.432
1.302
1. 172
1.042
.911
.781
.651
.586
.521
lbs.
2.051
1.777
1.504
1.367
1. 231
1.094
.957
.820
.684
lbs.
2.148
1.862
1.576
1.423
1.289
1. 146
1.003
.859
.716
1
2
bs.
246
947
647
497
348
198
048
898
749
122 Materials
Band and Hoop Iron Weights per Lineal Foot — {Continued)
Width in inches
No. o( I
gauge
lUS.
IIJS.
ItJS.
liJS.
IDS.
IDS.
IDS.
3.344
3.S39
2.734
2 930
3.12s
3.321
3Si6
a.l88
2 370
2552
2.734
2.917
3.099
3.281
3.031
2.201
2 370
2.539
2.708
2.878
3.047
1. 87s
2.031
2.188
2.344
2.SOO
2.6s6
2.813
1. 719
1.862
2.00S
2.148
2.292
2.435
2.578
1.563
1.693
1.823
1.953
2.083
2.214
2.344
1.406
1.523
1. 641
1.758
1.87s
1.992
2.109
1.250
1.354
1.458
1.563
1.667
1. 771
1.87s
1.094
1.18s
1.276
1.367
1.458
1.549
1. 641
■ 938
1. 016
1.094
.781
.846
.911
lbs.
3.906
3.646
3 38s
3 I2S
2.864
2.604
2.344
2.083
1.823
54
lbs.
4 297
4. oil
3 724
3.437
3. 151
2.86s
2.578
3.292
2.005
Mba.
4.688
4. 375
4 063
3-750
3438
3-125
3.813
3.500
3.188
Weights of Flat Rolled Iron per Lineal Foot
123
Weights of Flat Rolled Iron per Lineal Foot
For thicknesses from He inch to 2 inches and widths from i inch to
12J4 inches.
Iron weighing 480 pounds per cubic foot.
Thick-
I
i'/4
i>6
1%
2
2H
2H
3%
12
ness in
inches
inch
inches
inches
inches
inches
inches
inches
inches
inches
Ma
.208
.260
.313
.36s
.417
.469
.521
.573
2.50
^
• 417
.521
.625
.729
.833
.938
1.04
I. IS
5-00
ViS
.62s
.781
.938
1.09
I. 25
1. 41
1.56
1.72
7-So
H
.833
1.04
1.25
1.46
1.67
1.88
2.08
2.29
10.00
Me
1.04
1.30
I.S6
1.82
2.08
2.34
2.60
2.86
12.50
H
1.25
1.56
1.88
2.19
2.50
2.81
3-13
3-44
15 00
Me
1.46
1.82
2.19
2.55
2.92
3.28
3-65
4.01
17 -SO
H
1.67
2.08
2.50
2.92
3-33
3-75
4-17
4-58
20.00
^e
I 88
2.34
2.81
3.28
3-75
4.22
4-69
S-16
22.50
^
2.08
2.60
3-31
3.6s
4-17
4.69
5.21
S.73
25.00
iHe
2.29
2.86
3-44
4.01
4.58
5.i6
5.73
6.30
27.50
y*
2. so
3- 13
3-75
4.38
500
5.63
6.25
6.88
30.00
1^6
2.71
3-39
4.06
4-74
5.42
6.09
6.77
7-45
32-50
J6
2.92
3.6s
438
5.10
5.83
6.56
7.29
8.02
35 00
1^6
3- 13
3.91
4.69
S.47
6.2s
703
7.81
8.59
37.50
I
3 33
4.17
s-oo
S.83
6.67
750
8.33
9-17
40.00
iHe
3-54
4-43
531
6.20
7.08
7-97
8.8s
9-74
42.50
If6
3.7s
4.69
S.63
6.56
750
8.44
9-38
10.31
45 -00
1^6
3.96
4.95
5. 94
6.93
7.92
8.91
9-90
10.89
47.50
iH
4 17
S.21
6.2s
7.29
8.33
9 38
10.42
11.46
50.00
iHe
4.37
5-47
6.56
7.66
8.75
984
10.94
12.03
52.50
m
4.S8
5. 73
6.88
8.02
9.17
10.31
11.46
12.60
55 -00
ij-ie
4.79
5.99
7.19
8.39
9S8
10.78
11.98
13-18
57-50
iH
5.00
6.25
7 so
8.75
10.00
11.25
12.50
13-75
60.00
me
5.21
6. SI
7.81
9-11
10.42
11.72
13 02
14-32
62.50
iH
S.42
6.77
8.13
948
10.83
12.19
13-54
14-90
65.00
I'Me
S.63
703
8.44
9.84
11.25
12.66
14.06
IS -47
67 -SO
m
6.83
7.29
8.7S
10.21
11.67
13 13
14-58
16.04
70.00
Il?l6
6.04
7. 55
9.06
10. 57
12.08
13-59
IS 10
16.61
72.50
m
6.25
7.81
9.38
10.94
12.50
14.06
15-63
17.19
75-00
I>M6
6.46
8.07
9.69
11.30
12.92
14-53
16. IS
17.76
77.50
2
6.67
8.33
10.00
11.67
13 33
1500
16.67
18-33
80.00
1 24 Mutcriuls
Weights of I'lat Rolled Iron per Lineal Foot — (Conliitued)
Thick-
3
3W
3W
3W
4M
4W
4M
13
ness in
inches
inches
inches
inches
inches
ItlLllCS
inches
inches
inches
inches
M«
.62s
.677
.729
.781
.833
.885
.938
• 990
3. so
\i
I. 25
1.35
1.46
1.56
1.67
1-77
1.88
I 98
5 00
?1«
1.88
2.03
3.19
3.34
2. so
3.66
3.81
3 97
7 SO
H
3. so
2.71
2.92
3.13
3 33
3 S4
3.7s
3.96
10.00
^«
3 13
3 39
3.65
3.91
4.17
4.43
4.69
4.9s
13.50
H
3-75
4.06
4.38
4.69
SCO
s 31
S.63
S.94
15.00
lU
4.38
4.74
5. 10
5. 47
S.83
6.20
6 56
6.93
17. SO
Vi
S.oo
5.42
5.83
6.25
6.67
7.08
7.50
7.93
3O.0O
9<«
S.63
6.09
6.56
7.03
7. SO
7.97
8.44
8.91
33.50
H
6.2s
6.77
7.29
7.81
8.33
8.85
9-38
9.90
35.00
•Me
6.88
7.45
8.02
8.59
917
9 74
10.31
10.89
37.50
%
7.50
8.13
8.75
9.38
10.00
10.63
11.35
11.88
30.00
»?^n
8.13
8.80
9.48
10.16
10.83
II. SI
13.19
12.86
33.SO
?6
8. 75
9.48
10.21
10.94
11.67
12.40
13 13
13.8s
35.00
>51o
9 38
10.16
10.94
11.72
12.50
13-38
14 06
14.84
37.50
I
10.00
10.83
11.67
12.50
13-33
14-17
15.00
15.83
40.00
iMe
10.63
II. SI
12.40
13.28
14.17
IS. OS
IS. 94
16.82
42.50
iH
11.25
12.19
13.13
14.06
15.00
15-94
16.88
17.81
45 00
iMb
11.88
12.86
13.8s
14.84
15.83
16.82
17.81
18.80
47.50
iH
12.50
13.54
14.58
15.63
16.67
17.71
18.7s
19.79
SO. 00
151 8
13.13
14.22
15.31
16.41
17.50
18.59
19-69
20.78
52.50
i9i
13. 75
14.90
16.04
17.19
18.33
19.48
20.63
31.77
SS.oo
i^«
14.38
15.57
16.77
17.97
19.17
20.36
21.56
22.76
57.50
i!^
15.00
16.25
17.50
18.7s
20.00
21.25
22.50
23 75
60.00
19^0
15.63
16.93
18.23
19.53
20.83
22.14
33.44
24.74
63.50
15^
16.25
17.60
18.96
20.31
21.67
23.02
34.38
35-73
65.00
I' Me
16.88
18.28
19.69
21.09
22.50
23.91
25.31
36.73
67.50
i?4
17.50
18.96
20.42
21.88
23-33
34.79
26.25
37.71
70.00
I'9<6
18.13
19.64
21.15
22.66
24.17
25.68
27.19
38 70
73.50
I'/i
18.75
20.31
21.88
23.44
25.00
26.56
28.13
39.69
75.00
i>5ie
19-38
20.99
22.60
24.22
25.83
27.45
29.06
30 68
77.50
3
20.00
21.67
23 33
25.00
36 67
28.33
30.00
31 67
80.00
Weights of Flat Rolled Iron per Lineal Foot 125
Weights of Flat Rolled Iron per Lineal Foot — {Continued)
Thick-
5
5M
s!-^
5%
6
6H
6H
6%
12
ness in
inches
inches
inches
inches
inches
inches
inches
inches
inches
inches
He
1.04
1.09
I -IS
1.20
1.25
1.30
1.35
1.41
2.50
H
2.08
2.19
2.29
2.40
2.50
2.60
2.71
2.81
5.00
Me
3.13
3.28
3.44
3.59
3.75
3 91
4.06
4.22
7.50
y*
4.17
4.38
4.58
4.79
500
5. 21
5.42
5.63
10.00
9ie
S.21
5.47
5.73
5.99
6.25
6.51
6.77
7 03
12.50
%,
6.2s
6.56
6.88
7.19
7-50
7.81
8.13
8.44
15 00
7/ie
7.29
7.66
8.02
8.39
8.75
9.11
9.48
9 84
1750
yi
8.33
8.75
9.17
9. 58
10.00
10.42
10.83
11.25
20.00
9<e
938
984
10.31
10.78
II. 25
11.72
12.19
12.66
22.50
^
10.42
10.94
11.46
11.98
12.50
13 02
13.54
14.06
25 00
iMe
11.46
12.03
12.60
13 iS
13.75
14.32
14.90
15. 47
27.50
H
12.50
13.13
13.75
14.38
15 00
IS. 63
16.25
16.88
30 00
ijle
13.54
14.22
14.90
15.57
16.25
16.93
17.60
18.28
32.50
^
14.58
15.31
16.04
16.77
17.50
18.23
18.96
19.69
35 00
1^6
15.63
16.41
17.19
17.97
18.7s
19 -53
20.31
21.09
37.50
I
16.67
17.50
18.33
19.17
20.00
20.83
21.67
22.50
40.00
iMe
17.71
18.59
19.48
20.36
21.25
22.14
23.02
23.91
42.50
IH
18.75
19.69
20.63
21.56
22.50
23.44
24.38
25.31
45.00
iMe
19 79
20.78
21.77
22.76
23.75
24.74
25.73
26.72
47.50
IW
20.83
21.88
22.92
23.96
25.00
26.04
27.08
28.13
50.00
iMe
21.88
22.97
24.06
25.16
26.25
27.34
28.44
29.53
52.50
l?6
22.92
24.06
25.21
26.35
27.50
28.65
29.79
30.94
55.00
17/16
23.96
25.16
26.35
27.55
28.7s
29.9s
31.15
32.34
57.50
I^^
25.00
26.25
27.50
28.75
30.00
31.2s
32.50
33-75
60.00
I?^6
26.04
27.34
28.6s
29 95
31.25
32.55
33 85
35.16
62.50
IH
27.08
28.44
29.79
31.15
32.50
33.85
35.21
36.56
65.00
I'Me
28.13
29.53
30.94
32.34
33.75
35.16
36.56
37.97
67. SO
m
29.17
30.63
32.08
33.54
35.00
36.46
37.92
39 38
70.00
l>?i6
30 21
31.72
33.23
34.74
36.25
37.76
39-27
40.78
72.50
I^
31 25
32.81
34.38
35.94
37.50
39.06
40.63
42.19
75.00
I»5^6
32.29
33.91
35.52
37.14
38.75
40.36
41.98
43. 59
77. SO
2
33 33
35.00
36.67
38.33
40.00
41.67
43.33
45. 00
80.00
1 26 Matcri:il.s
Weights of Flat Kulleu Ieon pek Lineal Foot — (Continued)
Thick-
7
IM
74
IH
8
8^
8li
8^4
13
ness in
inches
inches
inches
inches
inches
inches
inches
inches
inches
inches
Ma
1.46
1. 51
I.S6
1. 61
1.67
1.73
1.77
I 83
3. so
H
3.93
3.03
3.13
3.23
3.33
3.44
3. 54
3.6s
5. 00
?1.
4.38
4. S3
4.69
4.84
5.00
5.16
S.31
S.47
7 SO
H
S.83
6.04
6.2s
6.46
6.67
6.88
7.08
7.39
10.00
?!«
7.39
7SS
7.81
8.07
8.33
8.59
8.85
9.11
13 SO
?i
8.7s
9.06
9.38
9.69
10.00
10.31
10.63
10 94
15 00
M«
10.21
10.57
10.94
11.30
11.67
13. 03
12.40
13.76
17 SO
W
11.67
12.08
12.50
12.92
13.33
13. 75
14.17
14.58
30 00
9i«
13 13
13. 59
14.06
14 53
15 00
15.47
IS. 94
16.41
33.50
56
14 58
15 10
15 63
16 IS
16.67
17.19
17.71
18.33
35.00
>M.
16.04
16.61
17.19
17.76
18.33
18.91
19.48
20.05
27 50
^4
17. SO
18.13
18.7s
19 38
20.00
20.63
21.25
31.88
30 00
>^«
18.96
19.64
20.31
20 99
21 67
22.24
23.02
33 70
32 so
T6
20.42
21.15
21.88
22.60
23 33
24.06
24.79
35. 53
35 00
'5i8
21.88
22.66
23.44
24.22
25 00
25.78
26.56
37. 34
37 so
I
23.33
24.17
25.00
25.83
26.67
27. SO
28.33
2917
40.00
iHo
24.79
25.68
26.56
27.45
28.33
29.22
30.10
30.99
42.50
1^6
26.25
27.19
28.13
29.06
30.00
30.94
31.88
33.81
45 00
i?^fl
27.71
28.70
29.69
30.68
31.67
32.66
33.65
34.64
47 50
l'/4
29.17
30.21
31.25
32.29
33.33
34.38
35.42
36.46
50.00
l^ia
30.62
31.72
32.81
33.91
3S-00
36.09
37.19
38.38
52.50
1?6
32.08
33.23
34.38
35. 52
36.67
37.81
38.96
40.10
55 00
1^6
33S4
34.74
35.94
37.14
38.33
39 53
40.73
41 93
57.50
m
35 00
36.25
37.50
38.75
40.00
41.25
42.50
43.75
60.00
191 B
36.46
37.76
39.06
40.36
41.67
42.97
44.27
45.57
62.50
iH
37 92
39.27
40.63
41.98
43.33
44.69
46.04
47.40
65.00
I' He
39- 38
40.78
42.19
43. 59
45. 00
46.41
47.81
49.22
67.50
i?4
40.83
42.29
43.75
45.21
46.67
48.13
49.58
51.04
70.00
i>5i«
42.29
43.80
45.31
46.82
48.33
49.84
51.35
52.86
73.50
iH
43.75
45.31
46.88
48.44
50.00
51.56
53.13
54.69
75.00
i>M()
45 21
46.82
48.44
50.05
51.67
53.28
54.90
56.51
77.50
3
46.67
48.33
50.00
51.67
53.33
55 00
56.67
58.33
80.00
Weights of Flat Rolled Iron per Lineal Foot 127
Weights of Flat Rolled Iron per Lineal Foot — {Continued)
Thick-
9
9Vi
9H
9%
10
loH
loi/4
loH
12
ness in
inches
inches
inches
inches
inches
inches
inches
inches
inches
inches
He
1.88
1.93
1.98
2.03
2.08
2.14
2.19
2.24
2,50
H
3.75
3.85
3.96
4.06
4.17
4.27
4.38
4.48
5.00
Me
S.63
5.78
5-94
6.09
6.2s
6.41
6.56
6.72
7.50
H
7-50
7.71
7.92
8.13
8.33
8.54
8.75
8.96
10.00
<>U.
938
9.64
9.90
10.16
10.42
10.68
10.94
11.20
12.50
%
II. 25
11.56
11.88
12.19
12.50
12.81
13.13
13.44
15.00
7/6
13.13
13.49
13. S5
14.22
14.58
14.95
15.31
15.68
17.50
H
15.00
15.42
IS. 83
16.25
16.67
17.08
17.50
17.92
20,00
9ia
16.88
17.34
17.81
18.28
18.75
19.22
19.69
20.16
22.50
H
18.75
19.27
19.79
20.31
20.83
21.35
21.88
22,40
25.00
iMe
20.63
21.20
21.77
22.34
22.92
23.49
24.06
24.64
27.50
H
22.50
23.13
23.75
24.38
25.00
25.62
26.25
26.88
30.00
1^6
24.38
25.05
25.73
26.41
27.08
27.76
28.44
29.11
32.50
?i
26.25
26.98
27.71
28.44
29.17
29.90
30.63
31.35
35.00
>M6
28.13
28.91
29.69
30.47
31.25
32.03
32.81
33.59
37. so
I
30.00
30.83
31.67
32.50
33.33
34.17
35.00
35.83
40.00
iVie
31.88
32.76
33.65
34.53
35.42
36.30
37.19
38.07
42.50
iH
33 75
34.69
35.63
36.56
37.50
38.44
39.38
40.31
45.00
iHi
35.63
36.61
37.60
38.59
39.58
40.57
41.56
42.5s
47.50
i!4
37.50
38.54
39.58
40.63
41.67
42.71
43.75
44.79
SO. 00
me
39 38
40.47
41.56
42.66
43.75
44.84
45.94
47.03
52.50
i?i
41.25
42,40
43-54
44.69
45.83
46.98
48.13
49.27
55.00
iMe
43.13
44.32
45.52
46.72
47.92
49."
50.31
51. 51
57.50
m
45.00
46.25
47.50
48.75
50.00
51.25
52.50
53.75
60,00
l?i6
46.88
48.18
49.48
50.78
52.08
S3. 39
54.69
5599
62,50
i^i
48.75
50.10
51.46
52.81
54.17
55.52
56.88
58.23
65.00
iiMe
50.63
52.03
53.44
54.84
56.25
57.66
59.06
60.47
67.50
m
52.50
53.96
55.42
56.88
58.33
59.79
61.25
62.71
70.00
11^6
54.38
55.89
57.40
S8.91
60.42
61.93
63.44
64.95
72.50
i^/i
56.25
57.81
59.38
60.94
62.50
64.06
65.63
67.19
75.00
I'Me
58.13
59. 74
61.35
62.97
64.58
66.20
67.81
69.43
77.50
2
60.06
61.67
63.33
65.00
66.67
68.33
70.00
71.67
80.00
1 28 Mali-rials
Weights of Flat Rolled Iron per Lineal Foot — {Continued)
Thick-
II
iiW
im
ii?4
13
I3M
I3^i
13)4
ness in
inches
inches
inches
inches
inches
inches
inches
inches
Mb
2.29
a. 34
2.40
2.45
3.50
2.SS
3 60
3.66
\i
458
4.69
4.79
4.90
5 00
S.io
S 21
s 31
■^u
6.88
7 03
7.19
7 34
7 so
7.66
7.81
7.97
W
9 17
9 38
958
9 79
10.00
10.21
10.43
10.63
5iB
11.46
11 72
11.98
12.24
12.50
13.76
13.03
13.38
H
13-75
14 06
14.38
14 69
15 00
IS. 31
IS. 63
IS 94
lU
16.04
16.41
16.77
17.14
17 50
17.86
18.33
18 59
Vi
18.33
18.75
19.17
19 58
30. 00
30.43
30.83
31.35
9<«
20.63
21.09
21.56
21.94
23 so
33.97
23.44
23 91
56
22.92
23-44
23 96
24.48
25.00
35.52
36.04
26 56
'Mb
25.21
25.78
26.35
26.93
37 50
38.07
28.65
29 33
%
27SO
28.13
28.7s
29.38
30.00
30.63
31.2s
31 88
>?k
29.79
30.47
31 -IS
31.82
32. so
33.18
33 85
34 53
''A
32.08
32 81
33-54
34.27
3S.OO
35. 73
36.46
37.19
'Mb
34.38
35.16
35 94
36.72
37.50
38.28
3906
39 84
I
36.67
37.50
38-33
39.17
40.00
40.83
41.67
43 so
iMb
38.96
39 84
40-73
41.61
43 50
43.39
44.37
45.16
I'i
41-25
42.19
43.13
44.06
45.00
45.94
46.88
47.81
I?i8
43-54
44.53
45 52
46 SI
47.50
48.49
49.48
so. 47
iM
45-83
46 88
47 92
48.96
so 00
SI 04
53.08
S3. 13
iMfl
48.13
49.22
50.31
SI. 41
53.50
53. 59
54.69
55. 78
iH
50 42
51.56
52 71
S3.8S
55 00
56.15
57 39
58.44
1^1 B
52.71
S3. 91
55. 10
56.30
57 SO
58.70
59 90
61.09
m
55 00
56.2s
S7.SO
58.75
60.00
61. 35
62.50
63.7s
1?<8
57.29
58.59
59 90
61.20
62.50
63.80
65.10
66.41
iH
59-98
60.94
62.29
63.65
65.00
66.35
67.71
69.06
I' Ma
61.88
63.28
64.69
66 09
67.50
68.91
70.31
71.72
1^4
64.17
65.63
67.08
68. S4
70.00
71.46
72 92
74.38
!'»!«
66.46
67.97
69.48
70.99
72.50
74.01
75 53
77.03
iTi
68.75
70.31
71.88
73.44
75 00
76.56
78.13
79.69
I'^ie
71.04
72.66
74.27
75.89
77. SO
79.11
80 73
82.34
2
73.33
75. 00
76.67
78.33
80 00
81.67
83 33
85.00
The weights for 12-inch width are repeated on each page to facilitate making the
additions necessary to obtain the weights of plates wider than 12 inches. Thus, to
find the weight of is!4"X ;s", add the weights to be found in the same line for 3M Xji
and i2Xji=9.48 + 35-00 = 44.48 pounds.
Areas of Flat Rolled Iron
129
Areas of Flat Rolled Iron
For thicknesses from Ms inch to 2 inches and widths from i inch to 125.1 inches.
Thick-
I
. '^^
_ 1\*L
I?4
2
2^4
. ^'•^
2%
12
ness in
inches
inch
inches
inches
inches
inches
inches
inches
inches
inches
He
.063
.078
.094
.109
.125
.141
.156
.172
.750
%
.125
.156
.188
.219
.250
.281
.313
• 344
1.50
Me
.188
.234
.281
.328
.375
.422
.469
.516
2.2s
\i
.250
.313
■ 375
.438
.500
.563
.625
.688
3.00
Me
.313
• 391
• 469
.547
.625
.703
.781
.859
3.75
%
■ 375
• 469
.563
.656
.750
.844
.938
1.03
4.50
Me
.438
.547
.656
.766
.875
.984
1.09
1.20
5. 25
¥t
.500
.625
.750
.875
1. 00
1. 13
1. 25
1.38
6.00
9i6
.563
.703
.844
.984
1.13
1.27
1. 41
1.55
6.75
H
.62s
.781
.938
1.09
1.25
1. 41
1.56
1.72
7.50
iHe
.688
.859
1.03
1.20
1.38
1.55
1.72
1.89
8.25
%
.750
.938
1. 13
1. 31
1.50
1.69
1.88
2.06
9.00
1^6
.813
1.02
1.22
1.42
1.63
1.83
2.03
2.23
9-75
li
.875
1.09
1. 31
1.53
1.75
1.97
2.19
2.41
10.50
me
.938
1. 17
1. 41
1.64
1.88
2. II
2.34
2.58
11.25
I
1. 00
1.25
1.50
1.75
2.00
2.25
2.50
2.75
12.00
iMe
1.06
1.33
1.59
1.86
2.13
2.39
2.66
2.92
12.75
m
1. 13
1. 41
1.69
1.97
2.25
2.53
2.81
3.09
13.50
iMe
1. 19
1.48
1.78
2.08
2.38
2.67
2.97
3.27
14.25
iH
1. 25
1.56
1.88
2.19
2.50
2.81
3.13
3-44
15.00
iMe
1. 31
1.64
1.97
2.30
2.63
2.95
3.28
3.61
15.7s
iji
1.38
1.72
2.06
2.41
2.75
3.09
3.44
3.78
16.50
iMe
1.44
1.80
2.16
2.52
2.88
323
3.59
3.9s
17.2s
i^^
1.50
1.88
2.25
2.63
3-0O
3.38
3-75
4.13
18.00
i9ie
1.56
I 95
2.34
2.73
3.13
3. 52
3.91
4.30
18.7s
i5i
1.63
2.03
2.44
2.84
3.25
3.66
4.06
4-47
19 50
I'He
1.69
2. II
2.53
2.95
3.38
3.80
4.22
4.64
20.25
1%
1. 75
2.19
2.63
3.06
3.50
3.94
4.38
4.81
21.00
I'Me
1. 81
2.27
2.72
3-17
3.63
4.08
4.53
4.98
21.75
l7/i
1.88
2.34
2.81
3.28
3.75
4.22
4.69
5.16
22.50
I»M6
1.94
2.42
2.91
3.39
3.88
436
4.84
5. 33
23.25
2
2.00
2. so
3.00
3.50
4.00
4.50
5.00
5.50
24.00
UO
Malrrials
WEiGirTs OF Flat Rollkd Stkel per Lineal Foot
For thicknesses from ^U inch to 2 inches and widths from I inch to u?i inches.
Thick-
inches
inches
ness in
inches
I
inch
.638
ht
.797
• 957
H
.850
1.06
1.28
W«
1.06
1.33
1.59
H
1.28
I 59
1.92
M«
1.49
1.86
2.23
H
1.70
2.12
2.SS
?i.
1.92
2.39
2.87
H
2.12
2.6s
3.19
•Mo
2.34
2.92
3. SI
?4
2.55
3.19
3.83
"?i6
2.76
3.45
4.14
li
2.98
3-72
4.47
I .'. ; «
T, to
3 99
478
I
4-25
5.10
i'i«
3.61
4-52
S.42
iH
3.83
4.78
5.74
iho
4.04
5.05
6.06
iH
4-25
5.31
6.38
iMo
4.46
558
6.69
iH
4.67
5.84
7.02
ilU
4.89
6. II
7.34
m
5. 10
6.38
7.65
I?<»
S.32
6.64
7.97
iH
5.52
6.90
8.29
i>Me
5. 74
7.17
8.61
m
595
7-44
8.93
ll?16
6.16
7.70
9.24
r^6
6.38
7.97
9-57
I' Mo
6.59
8.24
9.88
3
6.80
8.S0
10.20
I}*
inches
1.49
1.86
2.23
2.60
3 35
3.72
4.09
4-47
4.84
5.20
5. 58
5. 95
6.32
6.70
7.07
7-44
7.81
8.18
8.56
8.93
9 30
9.67
10.04
10.42
10.79
II. IS
11.53
11.90
3
2M
inches
inches
1.38
1.44
1.70
1. 91
2.12
2 39
2. 55
2.87
2.98
3.35
3.40
3.83
3 83
4.30
4.2s
4.78
4.67
5.26
5.10
5-75
5 53
6.21
5.95
6.69
6.38
7.18
6.80
7.6s
7.22
8.13
7.65
8.61
8.0S
909
8.50
9-57
8.93
10.04
9.35
10.52
9.78
11.00
10.20
11.48
10.63
11.95
II. OS
12.43
11.47
12.91
11.90
13.40
12.33
13.86
12.75
14.34
13.18
14.83
13 60
15.30
2H
inches
1.59
3.13
3.65
3.19
3.72
4.25
4.78
5-31
5.84
6.38
6.90
7.44
7.97
8.50
9 03
9 57
10.10
10.63
11.16
11.69
12.22
12.75
13.28
13.81
14.34
14.88
15 40
15.94
16.47
17.00
2H
inches
1-75
2-34
3.92
351
4.09
4.67
5.36
S.84
6.43
7.02
7.60
8.18
8.77
9 35
9 93
10.52
II. II
11.69
13.27
12.8s
13.44
14.03
14.61
15.19
15.78
16.37
16.95
17.53
18.13
18.70
13
inches
7.65
10. ao
13.75
15.30
17.85
20.40
22.95
25.50
28.0s
30.60
33.15
35.70
38.25
40.80
43 35
45 90
48 45
51 00
S3 55
56.10
58.6s
61.30
63.75
66.30
68.85
71.40
73. 95
76.50
.79 OS
81.60
Weights of Flat Rolled Steel per Lineal Foot 131
Weights of Flat Rolled Steel per Lineal Foot — {Continued)
Thick-
3
3H
3H
3H
4
4H
4H
Si
12
ness in
inches
inches
inches
inches
inches
inches
inches
inches
inches
inches
?i6
1. 91
2.07
2.23
2.39
2.55
2.71
2.87
3.03
7.65
H
2.55
2.76
2.98
3.19
3.40
3.61
3.83
4.04
10.20
*/i6
3 19
3. 45
3-72
3-99
4-25
4.52
4.78
5. 05
12.75
9i
3.83
4.15
4-47
478
5.10
5.42
5.74
6.06
IS. 30
lU
4.46
483
5.20
5.58
5.95
6.32
6.70
7.07
17.8s
H
5.10
5.53
5.95
6.38
6.80
7.22
7-65
8.08
20.40
9i6
S-74
6.22
6.70
7- 17
7.65
8.13
8.61
9.09
22. 95
H
6.38
6.91
7.44
7-97
8.50
903
9-57
10.10
25 50
iMe
7.02
7.60
8.18
8.76
9-35
9-93
10.52
II. II
28.0s
H
7.65
8.29
8.93
9-57
10.20
10.84
11.48
12.12
30.60
1^6
8.29
8.98
9.67
10.36
II. OS
11.74
12.43
13.12
33 IS
^
8.93
967
10.41
II. 16
11.90
12.65
13.39
14.13
35.70
1^6
9-57
10.36
II. 16
11.95
12.75
13.55
14.34
15.14
38.2s
I
10.20
II. OS
11.90
12.75
1360
14.45
15.30
16.15
40.80
1M6
10.84
11.74
12.65
13-55
14-45
15-35
16.26
17 16
43.35
iH
11.48
12.43
13.39
14.34
15-30
16.26
17.22
18.17
45.90
1^6
12.12
13 12
14.13
15.14
16.15
17.16
18.17
19.18
48.4s
i34
12. 75
13.81
14.87
15-94
17.00
18.06
19.13
20.19
5100
i^Ae
13.39
14.50
15.62
16.74
17-85
18.96
20.08
21.20
53-55
iH
14 03
15 -20
16.36
17.53
18.70
19-87
21.04
22.21
s6.io
ilU
14 66
15.88
17.10
18.33
19 55
20.77
21.99
23.22
58.65
iV^
15.30
16.58
17.85
19-13
20.40
21.68
22.95
24.23
61.20
l9i6
15.94
17.27
18.60
19.92
21.25
22.58
23.91
25.24
63.75
i5.6
16.58
17.96
19 -34
20.72
22.10
23.48
24.87
26.25
66.30
liMe
17.22
18.65
20.08
21.51
22.95
24.38
25.82
27.26
68.85
i?4
17.85
19 -34
20.83
22.32
23.80
25.29
26.78
28.27
71.40
li^ie
18.49
20.03
21.57
23.11
24.65
26.19
27.73
29.27
73-95
I'/i
19- 13
20.72
22.31
23.91
25 SO
27.10
28.69
30.28
76 -SO
iiS/ie
19.77
21.41
23.06
24.70
26.35
28.00
29.64
31.29
79-05
2
20.40
22.10
23.80
25.50
27.20
28.90
30.60
32.30
81.60
r.^2 Materials
Weights of Flat Rolled Steel per Lineal Foot — {Coniinurd)
Thick-
ness in
inchi-s
s
inches
SU
inches
inches
inches
6
inches
inches
6W
inches
inches
13
inches
3.19
435
3 35
4.46
3SI
4.67
3.67
4.89
3.83
S.io
3 99
5.31
4.14
4»
5 74
76s
10. 30
S.31
6.38
7.44
8.50
5-58
6.69
7.81
8-93
5. 84
7.02
8.18
935
6 II
7 34
8.56
9 77
6.38
7.6s
8.93
10.20
6.64
7-97
9 29
10.63
6.90
8.29
9.67
11. OS
7.17
8.61
10 04
11.48
12.75
is 30
17 8s
30 40
3\t
f4
9- 57
10.63
11.69
12.75
10.04
II. 16
12.27
13-39
10.52
11.69
12.8s
14.03
11.00
12.22
13.44
14.67
11.48
12.75
14 03
15-30
11-95
13 28
14.61
15.94
12.43
13 81
IS. 20
16.58
13.91
14 34
15.78
17.122
32 95
25 so
38 05
30.60
I
13-81
14.87
15-94
17.CXD
14.50
15 62
16.74
17 -8S
15-19
16.36
17-53
18.70
15.88
17.10
18.33
19 55
16.58
17-85
19-13
20. 40
17.27
18.60
19.92
21.25
17 95
19 34
20.72
22.10
18.6s
ao.o8
21.51
22.9s
33 IS
35 70
38.2s
40.80
I'-ifl
i-Mb
18.06
19 13
20.19
21.25
18.96
20.08
21.20
22.32
19.87
21.04
22.21
23.38
20.77
21.99
23.22
24.44
21.68
22.9s
24.23
2S-SO
22.58
23.91
25.23
26.56
2348
24.87
26.24
27.62
24.39
25.82
27.25
28.69
43. 35
45 90
48.4s
SI .00
m
22.32
23.38
24.44
25-50
23-43
24-54
25-66
26.78
24.54
25.71
26.88
28.0s
25.66
26.88
28.10
29.33
26.78
28. OS
29-33
30.60
27.90
29.22
30.55
31.88
29.01
30.39
31.77
33. IS
30.12
31.56
32.99
34.43
S3.SS
s6.io
S8.6S
61. 30
1%
26.57
27.63
28.69
29-75
27.89
29.01
30.12
31.24
29.22
30.39
31.55
32.73
30.5s
31.77
32.99
34.22
31.88
33.15
34.43
35.70
33.20
34. S3
35.86
37.19
34. S3
35. 91
37.30
38.68
35.86
37-29
38.73
40.17
63.7s
66.30
68.8s
71.40
i'Mb
3
30.81
31-87
32-94
3400
32.35
33.47
34. 59
35.70
33.89
35.06
36.23
37.40
35. 43
36.65
37.88
39.10
36.98
38.2s
39.53
40.80
38.52
39-85
41.17
42.50
40.0s
41.44
42.82
44.20
41.60
4303
44.46
45.90
73. 95
76.50
790s
81.60
Weights of Flat Rolled Steel per Lineal Foot 133
Weights of Flat Rolled Steel pee Lineal Foot — {Continued)
Thick-
ness in
inches
7
inches
7H
inches
7H
inches
7M
inches
8
inches
8H
inches
8H
inches
inches
12
inches
3/^6
4.46
4.62
4.78
4.94
5.10
5.26.
5.42
5. 58
7.6s
H
5-95
6.16
6.36
6.58
6.80
7.01
7.22
7.43
10.20
Vi6
7-44
7.70
7.97
8.23
8.50
8.76
9.03
9-29
12.75
%
8.93
9 25
9.57
9.88
10.20
10.52
10.84
11.16
iS-30
^6
10.41
10.78
ir.i6
11.53
11.90
12.27
12.64
13 02
17.85
'A
11.90
12.32
12 75
13.18
13.60
14.03
14.44
14-87
20.40
918
13-39
13.86
14.34
14.82
15.30
IS. 78
16.27
16.74
22.95
%
14.87
IS -40
15.94
16.47
17.00
17.53
18.06
18.59
25.50
iMe
16.36
16.94
17. S3
18.12
18.70
19.28
19.86
20.45
28.0s
H
17.8s
18.49
19.13
19.77
20.40
21.04
21.68
22.32
30.60
1^6
19-34
20.03
20.72
21.41
22.10
22.79
23.48
24.17
33.15
}i
20.83
21.57
22.32
23.05
23.80
24.55
25.30
26.04
35.70
me
22.32
23.11
23.91
24.70
25.50
26.30
27.10
27-89
38.25
I
23-80
24-65
25.50
26.35
27.20
28.05
28.90
29 75
40.80
iHe
25-29
26.19
27.10
28.00
28.90
29.80
30.70
31 -61
43. 35
1V6
26.78
27-73
28.68
29.64
30.60
31.56
32.52
33-47
45.90
1^6
28.26
29.27
30.28
31.29
32.30
33.31
34.32
35-33
48.45
iH
29.75
30.81
31.88
32.94
34.00
35.06
36.12
37-20
51.00
1^6
31-23
32.3s
33.48
34. 59
35.70
36.81
37.93
39 -OS
53.55
iH
32.72
33-89
35.06
36.23
37.40
38.57
39.74
40.91
56.10
iMe
34-21
35.44
36.66
37.88
39 10
40.32
41.54
42.77
58.6s
iJ^
35-70
36.98
38.26
39.53
40.80
42.08
43.35
44-63
61.20
I9i6
37-19
38.51
39.84
41.17
42.50
43.83
45.16
46-49 .
63.75
i^
38.67
40.0s
41.44
42.82
44.20
45.58
46.96
48-34
66.30
1IM6
40.16
41-59
43.03
44.47
45.90
47.33
48.76
50.20
68.8s
iH
41-65
43.14
44.63
46.12
47.60
49.09
50.58
52.07
71.40
Il?<6
43.14
44.68
46.22
47.76
49.30
50.84
52.38
53-92
73.95
1%
44-63
46.22
47.82
49-40
51.00
52.60
54.20
55-79
76.50
ii^-ia
46.12
47.76
49.41
SI. OS
52.70
54.35
56.00
57-64
79.0s
2
47-60
49.30
51 00
52.70
54.40
56.10
57.80
59 -50
81.60
1.34 Materials
Weights of Flat Rolled Steel per Lineal Foot — (Continued)
Thick-
ness in
inches
9
9W
9W
^i
10
loM
10'
13
inches
inches
inches
inches
inches
inches
inch<
^U
S.74
5 '
6.22
6.38
6.54
6.70
6.86
7.6s
y*
7.6s
7.>'
8.29
8. so
8.71
8.92
914
10. 20
9i«
9S6
9-83
10.10
10.36
10.62
10.89
II. 16
11.42
12 75
H
11.48
11.80
12.12
12.44
12. 7S
13 07
13 39
13 71
15.30
lu
13.40
13.76
14.14
14.51
14.88
15.25
IS. 62
IS 99
17 8S
H
15.30
IS. 73
16.16
16.58
17.00
17.42
17.8s
18.28
20.40
9i«
17.22
17-69
18.18
18.65
19.14
19.61
30.08
20.56
22. 95
58
19 13
19-65
20.19
20.72
21.25
21.78
22.32
22.85
25 SO
'H6
21.04
21.62
22.21
22.79
23.38
23 96
24. 54
25.13
28. OS
H
22.96
23-59
24.23
24.86
25.50
26.14
26.78
27.42
30.60
>^8
24.86
25-55
26.24
26.94
27.62
28.32
29.00
29 69
33 IS
%
26.78
27-52
28.26
29. ox
29.75
30.50
31.24
31.98
35.70
mt
28.69
29.49
30.28
31.08
31.88
32.67
33.48
JJ.28
38.25
I
30.60
31-45
32.30
33. IS
34.00
34.8s
35.70
36-55
40.80
iM*
32.52
33.41
34.32
35.22
36.12
37.03
37.92
38-83
43 35
iV6
34.43
35. 38
36.34
37.29
38.25
39-21
40.17
41.12
45 90
i^«
36.34
37.35
38.36
39.37
40.38
41.39
42.40
43.40
48.4s
iH
38.26
39 31
40.37
41.44
42.50
43.56
44.63
45.69
51.00
1^9
40.16
41.28
42.40
43 52
44.64
45.75
46.86
47.97
S3 55
iH
42.08
43.25
44.41
45.58
46.75
47.92
4908
50.2s
56.10
iM«
44.00
45-22
46.44
47:66
48.88
50.10
SI. 32
52.54
58.65
i^
4590
47.18
48.45
49-73
51.00
52.28
5355
54.83
61 20
i9<«
47.82
49.14
so. 48
51.80
53.14
54.46
55. 78
57.11
63.7s
1^6
49-73
51.10
52.49
53.87
55.2s
56.63
58.02
59.40
66.30
i>Mb
SI. 64
53 07
54. SI
55.94
57-38
58.81
60.24
61. 68
68.85
ly*
53 56
55.04
56.53
58.01
59.50
60.99
62.48
63.97
71.40
I'^6
55.46
57.00
58.54
60.09
61.62
63 17
64.70
66.24
7395
lu
57.38
58.97
60.56
62.16
63.7s
65.35
66.94
68.53
76.S0
v^u
59-29
60.94
62.58
64.23
65.88
67.52
69.18
70.83
790s
2
61.20
62.90
64.60
66.30
68.00
69.70
71.40
73.10
81.60
Weights of Flat Rolled Steel per Lineal Foot 135
Weights of Flat Rolled Steel per Lineal Foot — (Continued)
Thick-
ness in
inches
II
inches
iiM
inches
iiH
inches
liJ4
inches
12
inches
I2'/4
inches
12!.^
inches
12%
inches
?i6
7.02
7.17
7-32
7.49
7-6s
7.82
7-98
8.13
H
9-34
9S7
9-78
10.00
10.20
10.42
10.63
10.84
Me
11.68
11.95
12.22
12.49
12.75
13.01
13.28
13-55
H
14 03
14-35
14.68
14.99
15.30
IS -62
15-94
16.26
lU
16.36
16.74
17.12
17-49
17.85
18.23
18.60
18.97
M
18.70
19-13
19-55
19-67
20.40
20.82
21.25
21.67
9ifi
21.02
21.51
22.00
22.48
22.9s
23.43
23.90
24-39
56
23.38
23.91
24.44
24.97
25.50
26.03
26.56
27.09
>H6
25.70
26.30
26.88
27.47
28.05
28.64
29.22
29.80
%
28.0s
28.68
29-33
29.97
30.60
31.2s
31.88
32.52
1^6
30.40
31.08
31-76
32.46
33 IS
33-83
34.53
35.22
■"A
32.72
33.47
34.21
34.95
35.70
36.44
37.19
37.93
1^6
35 06
35-86
36.66
37.46
38.25
39 05
39-84
40.64
I
37.40
38.2s
39 10
39-95
40.80
41.6s
42.50
43-35
iHe
39-74
40.64
41.54
42.45
43-35
44.25
45.16
46.06
ij-i
42.08
43-04
44.00
44.94
45.90
46.86
47.82
48.77
iMe
44.42
45-42
46.44
47-45
48.45
49.46
50.46
51.48
iH
46.76
47-82
48.88
49-94
5100
52.06
53-12
54.19
iM«
4908
50.20
SI. 32
52.44
53-55
54.67
55-78
56.90
i?6
SI. 42
52.59
53.76
54-93
56.10
57.27
58.44
59.60
iMe
53.76
54.99
56.21
57.43
S8.6s
59-87
6i.io
62.32
l!.2
56.10
57-37
58.65
59- 93
61.20
62. 48
63 .75
65. 03
i?i6
58.42
59-76
61.10
62.43
63.75
6S.08
66.40
67.74
i=/6
60.78
62.16
63.54
64.92
66.30
67.68
69.06
70.44
iiMe
63.10
64 -55
65-98
67.42
68.8s
70.29
71.72
73 IS
i?i
65.4s
66.93
68.43
69.92
71.40
72.90
74.38
75.87
Il?l6
67.80
69-33
70.86
72.41
73.95
75.48
77 03
78.57
i56
70.12
71.72
73-31
74.90
76.50
78.09
79-69
81.28
ii^ie
72.46
74.11
75.76
77.41
79 05
80.70
82.34
83.99
2
74.80
76.50
78.20
79- 90
81.60
83.30
85.00
86.70
The weights for 12-inch width are repeated on each page to facilitate making the
additions necessary to obtain the weights of plates wider than 12 inches. Thus to
find the weight of is!'^" X^6", add the weights to be found in the same line for 3'/^ X^
and i2Xj6=io.4i -|- 35.70 = 46.11 pounds.
..i6
MaU-fials
WlCIGHTS AND AREAS OK SqUAKK AND RoUNI) BaRS OF WROUGHT
Iron and CiRCUUFERUNct of Round Bars.
One cubic foot weighing 480 lbs.
Weight of
D bar
I foot long
.013
.052
.117
.208
.326
.469
.638
.833
LOSS
1.302
I.S76
1.87s
2.201
2.SS2
2.930
3 333
3.763
4.219
4.701
5. 208
5742
6.302
6.888
7.S00
8.138
8.802
9.492
10.21
10.9s
11.72
12.51
13. 33
14.18
IS OS
IS. 95
16.88
17.83
18.80
19.80
20.83
21.89
22.97
24.08
25.21
26.37
27. S5
28.76
Weight of
O bar
I foot long
.010
.041
.092
.164
.256
.368
.501
.654
.828
I 023
I 237
1 473
1.728
2.004
2.301
2.618
2. 955
3.313
3.692
4.091
4. 510
4.950
5.410
5. 890
6.392
6.913
7455
8.018
8.601
9.204
9.828
10.47
II. 14
11.82
12.53
13 2S
14.00
14.77
IS- 55
16.36
17.19
18.04
18.91
19.80
20.71
21.64
22. S9
Area of
D bar
in square
inches
.0039
.0156
.0352
.062s
.0977
.1406
.1914
.2500
.3164
.3906
.4727
.5625
.6602
.7656
.8789
I. 0000
1.1289
1.2656
1.4102
1.562s
1.7227
1.8906
2.0664
2.2500
2.4414
2.6406
2.8477
3 0625
3 2852
3 S156
3.7539
4.0000
4 2539
4 5156
4.7852
5.062s
5 3477
5. 6406
s 9414
6.2500
6.5664
6.8906
7.2227
7.5625
7 . 9102
8.2656
8.6389
Area of
Circum-
0 bar
ference of
in square
0 bar
inches
in inches
.0031
1963
.0123
.3927
.0276
.5890
.0491
.7854
.0767
9817
.1104
1 . 1781
.1503
1.3744
.1963
I 5708
.2485
I. 7671
.3068
I 963s
.3712
2.1598
• 4418
2.3562
.S183
2.SS2S
.6013
2.7489
■ 6903
2.9452
■ 7854
3.I4I6
.8866
3.3379
• 9940
3 5343
I . I07S
37306
1.2272
3 9270
I. 3530
4.1233
1.4849
4.3197
1.6230
4 S160
I. 7671
4.7124
I. 9175
4.9087
2.0739
5.1051
2.2365
5.3014
2.4053
S.4978
2.5802
5 6941
2.7612
5.890s
2.9483
6.0868
3.1416
6.2832
3 3410
6 4795
3 5466
6 6759
3 7583
6.8723
3 9761
7.0686
4.2000
7 2649
4 4301
4.6664
4.9087
5.1572
5.4119
5.6727
S.9396
6.2126
6.4918
6.7771
Weight oi Square and Round Bars 137
Weight of Square and Round Bars — {Continued)
Thickness
Area of
Area of
Circum-
or diam-
Weight of
□ bar
I foot long
Weight of
0 bar
I foot long
D bar
0 bar
ference of
eter in
inches
in square
inches
in square
inches
0 bar
in inches
3
30 00
23 56
9.0000
7.0686
9.4248
He
31 26
24-55
9-3789
7-3662
9.6211
H
32 55
25.57
9.7656
7-6699
9-8175
•>i8
33.87
26.60
10.160
7-9798
10.014
Vi
35 21
27.65
10.563
8.2958
10.210
Me
3658
28.73
10.973
8.6179
10 . 407
%
37-97
29.82
II. 391
8.9462
10.603
yi6
39 39
30.94
II. 816
9.2806
10.799
Vi
40.83
32.07
12.250
9.6211
10.996
9i6
42.30
33 23
12.691
9.9678
II. 192
%
43.80
34.40
13- 141
10.321
11.388
iHe
45-33
35.60
13 598
10.680
11-585
M
46.88
36.82
14 -063
11.045
II. 781
l?i6
48.45
38.05
14-535
II. 416
11.977
J6
50.05
39.31
15.016
11-793
12.174
1^6
51.68
40.59
15.504
12.177
12.370
4
53-33
41.89
16.000
12.566
12.566
He
55 01
43.21
16.504
12.962
12.763
^
56.72
44.55
17.016
13-364
12.959
Ma
58.45
45.91
17-535
13-772
13- 155
^
60.21
47.29
18.063
14.186
13-352
Me
61.99
48.69
18.398
14.607
13-548
?i
63.80
50.11
19 141
IS -033
13-744
^6
65.64
51.55
19.691
IS -466
13-941
^
67.50
53.01
20.250
15-904
14-137
Me
69.39
54.50
20.816
16.349
14 334
5i
71 30
56.00
21.391
16.800
14-530
»H6
73-24
57-52
21.973
17-257
14-726
?4
75-21
59 -07
22.563
17.721
14-923
»M6
77-20
60.63
23.160
18.190
15 -119
%
79.22 _
62.22
23-766
18.665
15-31S
1^6
81.26
63.82
24.379
19.147
15 512
s
83.33
6545
25.000
19 63s
IS -708
Me
85.43
67.10
25.629
20.129
15-904
M
87.55
68.76
26.266
20.629
16.101
Me
89.70
70.45
26.910
21.135
16.297
M
91.88
72.16
27.563
21.648
16.493
Me
94.08
73-89
28.223
22.166
16.690
?6
96.30
75.64
28.891
22.691
16.886
^6
98-55
77.40
29.566
23.221
17.082
H
100.8
79-19
30.250
23-758
17-279
Me
103. 1
81.00
30.941
24.301
17-475
^
105.5
82.83
31.641
24.850
17.671
iMe
107.8
84-69
32.348
25.406
17.868
M
no. 2
86.56
33-063
25.967
18.064
»Me
112. 6
88.45
33 -78s
26.535
18 . 261
^
115-I
90.36
34-516
27.109
18.457
iMe
117-S
92.29
35 254
27.688
18.653
6
120.0
94.25
36.000
28.274
18.850
Me
122.5
96.22
36.754
28.866
19.046
H
125. 1
98.22
37-516
29.465
19.242
^e
127.6
100.2
38.28s
30.069
19-439
138 MaUri lis
Weight of Square and Round Bars — (.Continuei)
Thickness
Area of
Area of
Circum-
or diam-
Wcisht of
WfiKht of
0 »J:ir
I foot tonx
D bar
0 bar
ference o(
eter in
D bar
in square
in square
0 bar
incli'
l.iu J
inches
inches
in inches
6h
102.3
39 063
30.680
19.63s
9i»
132.8
104.3
39 848
31.296
19 831
n
135. 5
106.4
40.641
31.919
ao 038
lit
IJ8.1
108. s
41 441
32.548
30. 224
W
140.8
110.6
42 250
33.183
ao.420
^«
M3 6
112,7
43.066
33 824
ao.617
96
146.3
114. 9
43.891
34.472
20.813
'H<i
149 I
117. 1
44 723
3S 12s
21.009
%
151.9
"9 3
45 563
35.78s
21.206
'Mo
154.7
121. 5
46.410
36.450
21.402
%
157.6
123.7
47.266
37.122
21.598
»5<<i
160.4
126.0
48.129
37.800
21.795
7
163.3
128.3
49000
38.48s
21.991
H«
166.3
130.6
49 879
3917s
22.187
H
169.2
132.9
SO. 766
39 871
22.384
M«
172.2
135.2
51. 660
40.574
22.580
H
175.2
137.6
52.563
41.282
22.777
9<«
178.2
140.0
53.473
41.997
22.973
H
181.3
142.4
54 391
42.718
23.169
•M
184.4
144.8
55.316
43-445
23.366
H
187.5
147.3
56 250
44.179
23.562
9^6
190.6
149.7
57.191
44.918
23.758
96
193-8
152.2
S8 141
45-664
23 9SS
>Ma
197.0
154.7
59.098
46.415
24.151
%
200.2
157.2
60.063
47.173
24-347
>9^8
203. S
159.8
61.035
47.937
24 544
^/6
206.7
162.4
62.016
48.707
24.740
»M«
210.0
164.9
63 004
49.483
24.936
8
213 3
167.6
64.000
50.265
25.133
Mb
216.7
170.2
65.004
51 oS4
25.329
^
220.1
172.8
66.016
51.849
25 52s
?i.
223. 5
175. 5
67.03s
• 52.649
25.722
V4
226.9
178.2
68.063
53.456
25.918
M»
230.3
180.9
69.098
54.269
26.114
H
2.« 8
183.6
70.141
55.088
26.311
Mb
237.3
186.4
71.191
55.914
26.S07
H
240.8
189.2
72.250
56.745
26.704
?<•
244.4
191.9
73.316
57.583
26.900
96
248.0
194.8
74.391
58.426
27.096
»M8
251.6
197.6
75.473
59.276
27.293
94
255.2
200.4
76.563
60.132
27.489
'9i6
258.9
203.3
77.660
60.994
27.685
7/6
262,6
206.2
78.766
61.862
27.882
»9i«
266.3
209.1
79.879
62.737
28.078
9
270.0
212. 1
81.000
63.617
28.274
M.
273.8
215.0
82.129
64. 504
28.471
H
277.6
218.0
83.266
65-397
28.667
M«
281.4
221.0
84.410
66.296
28.863
M
285.2
224.0
85 563
67.201
29.060
M«
289 I
227.0
86,723
68.112
29.256
96
293.0
230.1
87.891
69.029
29.452
M«
296.9
233-2
89.066
69 953
29.649
Weight of Square and Round Bars
139
Weight of Square and Round Bars — {Continued)
Thickness
or diam-
Weight of
n bar
Weight of
0 bar
Area of
n bar
Area of
0 bar
Circum-
ference of
eter in
I foot long
I foot long
in square
in square
0 bar
inches
inches
inches
in inches
9}^
300.8
236.3
90.250
70.882
• •
29.845
9i6
304.8
239.4
91.441
71.818
30.041
5/i
308.8
242.5
92.641
72.760
30.238
>M6
312.8
245.7
93.848
73.708
30.434
%
316.9
248.9
95.063
74.662
30.631
>%6
321.0
252.1
96.285
75.622
30.827
%
32s. I
255.3
97.516
76.589
31 023
15/15
329.2
258. 5
98.754
77.561
31.200
10
333.3
261.8
100.00
78.540
31.416
He
337. 5
265.1
loi . 25
79-525
31.612
W
341.7
268.4
102.52
80.516
31.809
fi6
346.0
271.7
103.79
81.513
32.00s
H
3S0.2
275.1
105.06
82.516
32.201
Ma
354.5
278.4
106.3s
83 525
32.398
%
358.8
281.8
107.64
84-541
32.594
Me
363.1
285.2
108.94
85-562
32.790
V^
367.5
288.6
110.25
86.590
32.987
9ia
371.9
292.1
III. 57
87.624
33.183
96
376.3
29s. 5
112.89
88.664
33-379
•He
380.7
299.0
114.22
89.710
33 576
%
385.2
302.5
115.56
90.763
33-772
1^6
389.7
306.1
116. 91
91.821
33.968
J6
394.2
309.6
118.27
92.886
34.16s
1^6
398.8
313.2
119.63
93 956
34 361
II
403 -3
316.8
121.00
95 033
34.558
He
407.9
320.4
122.38
96.116
34.754
V6
412.6
324.0
123.77
97.205
34.950
Me
417.2
327.7
125.16
98.301
35.147
H
421.9
331.3
126.56
99.402
35.343
Me
426.6
335.0
127.97
100.51
35.539
96
431.3
338.7
129.39
101.62
35.736
Me
436.1
342.5
130.82
102.74
35.932
^^
440.8
346.2
132.25
103.87
36.128
«/i6
445.6
350.0
133.69
105.00
36.32s
96
4S0.5
353.8
135.14
106.14
36.521
>He
455. 3
357.6
136.60
107.28
36.717
M
460.2
.361.4
138.06
108.43
36.914
iMe
465.1
365.3
139-54
109.59
37.110
J6
470.1
369.2
141.02
no. 75
37.306
iMe
475. 0
373.1
142.50
III. 92
37 503
14© Mati'ri.ils
Weights and Areas of Cold Rolled Steel Shafting
Uiam-
Area,
Circum-
Weight
Diam-
Area,
Circum-
Weight
eter,
square
ference,
per fool.
eter.
square
ference,
per foot.
inches
inches
inches
pounds
2*18
inches
inches
pounds
M«
.0276
.5890
.09s
3-7S«3
6.8722
12.80
M
.0491
.7854
.167
2M
3.9761
7.0686
13 S3
9i.
.0767
.9817
.260
2^8
4.2000
7.2749
14 35
H
.1104
1.1781
-375
2H
4-4301
7-4613
IS 07
lit
.IS03
I 3744
-5"
2ji«
4.6664
7-6576
IS.89
H
.1963
1.5708
.667
2^
4-9087
7.8540
16.70
^6
.2485
I. 7671
-84s
2?l8
S-1572
8. 0503
17. 55
H
.3068
1.963s
I. OS
aH
S-4119
8.2467
18.41
>H«
.3712
2.1598
1.26
2>H8
S-6727
8.4430
19.31
y*
.4418
2.3562
I. SO
2H
S-9396
8.6394
20.21
i^ie
.5185
2.552s
1.77
2'M8
6.2126
8.8357
21.15
%
.6013
2.7489
2.0S
2li
6.4918
9.0321
22.09
>?io
.6903
2.9452
2.3s
2l$'i8
6.7771
9.2284
23.06
1
.7854
3.1416
2.68
3
7.0686
9.4248
240s
iM.
.8866
3.3379
3.02
M
7-6699
9-8I7S
26.09
iH
.9940
3-5343
3.38
3^8
7-9798
10.014
37.16
1^8
I . I07S
3.7306
3-77
3'/4
8.2958
10.210
38.23
iV*
I . 2272
3 9270
4-17
3H
8.9462
10.603
30.43
iMb
I.3S30
4.1233
.4-61
3lU
9.2806
10.799
31.58
iW
1.4849
4.3197
S-OS
3W
9.6211
10.996
32.73
iM«
1.6230
4.S160
552
3H
10.321
11.388
35.20
m
I. 7671
4.7124
6.0I
3' Ms
10.680
11.585
36.40
iMb
1.917s
4.9087
6.52
3?4
II. 04s ■
II. 781
37.57
iW
2.0739
S.iosi
7.06
3'/6
11.793
12.174
39.40
1>H8
2.236s
S.3014
7.61
3>^8
12.177
12.370
41.04
i?4
2.40S3
S.4978
8.18
4
12.566
12.566
43.75
I'Me
2.5802
5-6941
8.78
4H
14.186
13-352
48.26
1%
2.7612
5 -890s
9-39
4?i8
15-466
13-941
52.62
ima
2.9483
6.0868
10.03
4!^
IS -904
14.137
54."
2
3.1416
6.2832
10.69
4H
17.728
14.923
60.88
2H8
3-34IO
6.4793
11-35
4'M8
19.147
15.512
65.50
2H
3.5466
6. 6759
12.07
S
19.635
15.708
67.45
Corrugated Iron Roofing
141
Sheet Iron
Weight of a superficial foot.
Number of
Weight per
Number of
Weight per
gauge
foot
gauge
foot
I
II. 25
16= He
2.5
2
10,62s
17
2.1875
3=W
10.00
18
1.875
4
9.37s
19
1. 7188
5
8.7SO
20
1.5625
6
8. 125
21
I . 4063
7
7SO
22=!'^2
1.2500
8
6.875
23
1. 120
9
6.250
24
1. 000
10
S.62S
25
.900
11 = 5-8
S-ooo
26
.800
12
4-375
27
.720
13
3.750
28
.640
14
3- 125
29
.560
IS
2.8125
30
.500
Galvanized Sheet Iron
Am. Galv. Iron Ass'n. B. W. G.
No.
Ounces
avoir.
per
square
foot
Square
feet per
2240
pounds
No.
Ounces
avoir.
per
square
foot
Square
feet per
2240
pounds
No.
Ounces
avoir.
per
square
foot
Square
feet per
2240
pounds
29
28
27
26
25
12
13
14
IS
16
2987
2757
2560
2389
2240
24
23
22
21
20
17
19
21
24
28
2108
1886
1706
1493
1280
19
18
17
16
14
33
38
43
48
60
1084
943
833 •
746
597
Corrugated Iron Roofing
B. W.
gauge
Weight per square
(100 square feet).
Plain
Galvanized
Number
28
26
24
22
20
18
16
Pounds
97
los
128
ISO
185
270
340
Weighs from 5 to is per cent
heavier than plain, accord-
ing to the number B. W. G.
Allow one-third the net width for lapping and for corrugations.
2^ to 3!^ pounds for rivets will be required per square.
From
142
Malcriiils
Sizes and Weight of Sheet Tin
Mark
iC
iiC
mC
iX
iXX
iXXX...
iXXXX
DC
DX
DXX ...
DXXX .
DXXXX
SDC
SDX
SDXX...
SDXXX.
iCW
Number of
sheets in
box
22S
225
225
22s
225
22s
225
100
100
100
IOC
100
200
200
200
200
225
Dimension
Length,
inches
13W
iM
1294
I3?4
I3?4
1394
13?4
mi
mi
mi
mi
mi
IS
15
IS
IS
I3?4
Breadth,
inches
94
10
10
I2>^
I2W
12!.^
125.4
I2!-i
Weight of
box.
pounds
lOS
98
140
161
182
203
los
126
147
168
189
168
189
210
231
112
A bo.x containing 225 sheets, 1354 by 10, contains 214.84 square feet;
but allowing for seams it will cover only 150 square feet of roof.
A roof covered with metal should slope not less than i inch to the foot.
Weights of Sheet Metals per Square Foot
Thick-
Wrought
Cast
Steel,
Copper,
Brass,
Lead,
Zinc.
ness,
inches
iron,
pounds
iron,
pounds
pounds
pounds
pounds
pounds
pounds
Me
2.53
2.34
2.5s
2.89
2.73
3.71
2.34
H
5 OS
4.69
S.io
5-78
5.47
7-42
4-69
^0
7.58
7.03
7.66
8.67
8.20
II -13
7-03
H
10.10
938
10.21
11.56
10:94
14-83
938
M.
12.63
11.72
12.76
14-45
13-67
18-54
11.72
H
15 l6
14.06
15-31
17-34
16.41
22.25
14.06
Ht
17.68
16.41
17.87
20.23
19- 14
25-96
16.41
H
20.21
18.75
20.42
23 13
21.88
29.67
18.7s
H
25 27
23 44
25. S2
28.91
27.34
37-08
23.44
H
30.31
28.13
30.63
34 69
32.81
44 SO
28.13
Ji
35-37
32. 8l
35-73
40.47
38.28
SI 92
32.81
I
40.42
37. SO
40.83
46.25
43-75
59-33
37.50
Weight of Copper and Brass Wire and Plates
143
Weight of Copper and Brass Wire and Plates
Brown and Sharpe Gauge.
Weight of wire per
Weight of plates per
No. of
Size of
1000 lineal feet
square foot
each no.,
gauge
inch
Copper,
Brass,
Copper,
Brass,
pounds
pounds
pounds
pounds
0000 I .46000
640.5
605.28
20.84
19-69
000 .40964
508.0
479.91
18.55
17
S3
00 . 36480
402.0
380.77
16.52
IS
61
0
.32476
319-5
301.82
14-72
13
90
I
.28930
253-3
239 45
13.10
12
38
2
.25763
200.9
189.82
11.67
II
03
3
.22942
159 3
150 .-52
10.39
9
82
4
.20431
126.4
119.48
9-25
8
74
5
.18194
100.2
94.67
8.24
7
79
6
. 16202
79-46
75.08
7.34
6
93
7
.14428
63.01
59-55
6.54
6
18
8
. 12849
49 98
47.22
5-82
5
SO
9
.11443
39-64
37-44
5-18
4
90
10
. 10189
31 43
29.69
4.62
4
36
II
.090742
24.92
23.55
4-11
3
88
12
.080808
19.77
18.68
3.66
3
46
13
.071961
15-65
14.81
3.26
3
08
14
.064084
12.44
11-75
2.90
2
74
IS
.057068
9.86
9-32
2.59
2
44
16
.050820
7-82
7.59
2.30
2
18
17
.045257
6.20
5.86
2.05
94
18
.040303
4-92
4-65
1.83
72
19
.035890
3-90
3.68
1.63
54
20
.031961
3 09
2.92
1.45
37
21
.028462
2.45
2.317
1.29
22
22
.025347
1.94
1.838
I. IS
08
23
.022571
1.54
1.457
1.02
966
24
.020100
1.22
1. 155
.911
860
25
.017900
• 699
.916
.811
766
26
.01494
.769
.727
.722
682
27
.014195
.610
.576
.643
608
28
.012641
.484
.457
.573
541
29
.011257
.383
.362
.510
482
30
.010025
.304
.287
.454
429
31
.008928
.241
.228
.404
382
32
.007950
.191
.181
.360
340 .
33
.007080
.152
.143
.321
303
34
.006304
.120
.114
.286
270
35
.005614
.096
.0915
.254
240
36
.005000
.0757
.0715
.226
214
37
.004453
.0600
.0567
.202
191
38
.003965
.0467
.0450
.180
170
39
.003531
.0375
■ 0357
.160
ISI
40
.003144
.0299
.0283
.142
.I3S
Specific gravity
8.880
8.386
8 698
8.218
Weight per cubic foot
555
524-16
543.6
S13.6
144 Mutcriak
Weight of Sueet and Bar Brass
Sheets
Round
1
Sheets
Square
Round
Thick-
per
bars
Thick-
per
bars
bars
ness.
square
I foot
ness,
square
1 foot
1 fool
inches
foot,
loHK,
inches
foot.
long,
Ions,
pounds
■ Ol.s
;K^un(ls
.01 1
i' 11
pounds
pounds
pounds
M«
3.7
4S 95
4.08
3 ao
H
5-41
.05.S
.o.|5 1
I'h
48.69
4. 55
3 S7
^9
8.12
.125
.1
l')i<i
51. 4
5.08
3.97
W
10.76
.225
.175
iH
54.18
5.6s
4 41
M«
13.48
350
.275
I9i8
65.8s
6.23
486
H
16.25
SI
• 395
m
59 SS
6.81
5. 35
^»
19
.69
.54
i?i«
62.25
7. 45
5 85
Vi
21.65
.90s
.71
I'/i
65
8.13
637
9^8
24 3
1. 15
9
i9i8
67 75
8.83
6 93
w
27.13
1.4
I.I
i5i
70.35
9 55
7.48
•Mb
29.77
1.72
1.35 ,
I' Mb
73
10.27
8.05
Vk
32.46
2.05
1.66 1
Wk
75.86
II
8.65
'?^«
35.18
2.4
1.85 i
I'?l8
78.55
11.82
9.39
J6
37.85
2.75
2.15
1T6
81.25
12.68
9 95
'?<•
40.5s
3. IS
2.48
I'5<B
84
13. S
10.58
I
4329
3.6s
2.8s 1
2
86 75
14.35
11.25
Weight of Round Bolt Copper per Foot
Diameter,
inches
Pounds
Diameter,
inches
Pounds
Diameter,
inches
Pounds
.425
.756
1,18
1.70
2.31
I
iH
iH
iH
iH
1
3.02
3.83
4.72
5. 72
6.81 ,
i-}4
' 3
1
7.99
9 27
10.64
13. 10
Areas and Weights of Fillets of Steel, Cast Iron and Brass 145
Areas and Weights of Fillets of Steel, Cast Iron
AND Brass
Calculations are based on the following weights:
Steel 489 . 6 pounds per cubic foot.
Cast iron 45°
Cast brass 504
Fig. 39.
Radius
Area
Weight of steel
Weight of cast iron
Weight of cast brass
R
Per foot
Per inch
Per foot
Per inch
Per foot
Per inch
M6
.0008
.0029
.00024
.0026
.00022
0029
.00025
^6
.0033
.oiis
.00096
.0106
.0009
.0118
.0010
ri6
.0075
.0255
.0021
.0235
.0019
.0263
.0022
H
.0134
.0455
.0038
.0418
.003s
.0469
.0040
Vie
.0209
.0712
.0059
.0655
.0054
.0733
.0061
H
.0302
.1027
.0085
.0945
.0078
.1058
.0088
lU
.0411
.1397
.0116
.1285
.0107
■ 1439
.0120
H
.0536
.1825
.0152
.1679
.0140
.1880
.0157
%6
.0679
.2310
.0192
.2I2S
.0177
.2380
0200
H
.0834
.2847
.0237
.2169
.0218
.2932
.0244
iMe
.1014
.3447
.0287
• 3I7I
.0264
.3550
.0300
H
.1207
.4105
.0342
.3777
■ 031S
.4228
.0352
^Hs
.1416
.4817
.0401
.4432
.0369
.4962
.0414
'A
.1643
.5580
.0465
.5134
.0428
.5747
.0479
1^6
.1886
.6405
.OS34
.5893
.0491
.6597
.0550
I
.2146
.7300
.0608
6716
.0559
.7519
,0626
iH
.2716
.9250
.0771
.8sio
.0709
.9527
.0794
•iM
.3353
1. 140
.0950
1.049
.0874
1. 174
.0979
i^
.4057
1.200
.1000
1. 104
.0920
1.236
.1030
i^^
.4828
1.642
.1368
•I.SII
.1259
1. 691
.1410
iH
.5668
I 930
.1608
1.776
■ 1479
1.988
■ I6S7
iH
.6572
2.23s
.1862
2.056
.1713
2.302
.1920
ili
.7545
2.565
.2137
2 360
.1970
2.642
.2202
2
.858S
2.917
.2431
2.684
.2237
3.005
.2504
2H
.9692
3.292
.2743
3.029
.2502
3-091
.2826
2>4
1.086
3.695
.3079
3.399
.2832
3.806
.3172
2%
1. 210
4. IIS
.3429
3.786
.3155
4.238
.3532
2H
1. 341
4.560
.3800
4.19s
.3496
4.697
.3014
2H
1.478
5.030
.4192
4.628
.3857
5. 181
.4317
2%
1.623
5.S07
.4589
5 066
.4222
S.672
.4727
2H
1.774
6.027
.5022
5.545
.4621
6.208
.5017
3
1. 931
6.56s
.S47I
S.940
.4950
6.762
.5635
3H
2.096
7 123
.5937
6.555
.5462
7.339
.6116
3H
2.267
7.700
.6417
7.084
.5903
7-931
.6609
3%
2.444
8.300
.6917
7.636
.6363
8.549
7124
ZVi
2.629
8.92s
.7438
8. 211
.6926
9.193
.7661
35i
2.820
9.575
.7979
8.809
.7341
9.862
.8220
3%
3.018
10.27
.8523
9.448
.7873
10.58
.8817
3l<i
3.222
10.97
.9142
10.09
.8408
11.30
.9417
4
3.434
11.6s
.9709
10.72
.8933
12.00
1. 000
4Vi
3.652
12.40
1.033
II. 41
.9508
12.77
1.064
4!'i
3.876
13.15
1.096
12.10
1.008
13.54
1. 130
49i
4.I07
13-97
1. 164
12.8s
1. 071
14-39
1. 199
4H
4.346
14.77
1. 231
13.59
1. 132
15.21
1.270
m
4. 59°
IS. 60
1.300
14.33
1. 196
16.07
1.340
m
4.842
16.45
1. 371
IS. 13
1. 261
16.94
1. 412
4%
5. 100
17 32
1.444
15 93
1.328
17.84
1-487
5
5.365
18.2s
1. 521
16.79
1.400
18.80
I-S70
Contributed by Ernest J. Lees.
140
Malcriiils
Gauges and Wkiguts ov Iron Wikk
The siw-s and weights from No. ao to No. 40 arc those of the Trenton Iron Co.
Trenton. .\. J.
i
No.
1),,,M„NT,
Lineal (ect
No.
Diameter,
Lineal feet
inches
to the pound
inches
.013
to the pound
31
.031
392 772
31
3333. 6s3
33
.038
481 234
32
.013
3620.607
23
.02s
603.863
i3
.011
3119 092
24
.022s
745. 710
34
.010
3773 584
3S
.020
943.396
35
.0095
4182 S08
36
.oi8
1164.689
1 36
.009
4657.738
37
.017
1305.670
37
.0085
5222 035
38
.016
1476.869
38
.008
5896.147
29
.015
1676.989
39
.0075
6724 391
30
.014
1925.321
40
.007
7698.353
American Steel & Wire Company
Full sizes of plain wire
o
o
o
o
o
o
o
o
o
o
o
o
Fig. 40.
Gauge
Diameter
of Amer-
ican Steel
& Wire
Co. 's gauge
.2830
.2625
.2437
.2253
.2070
.1920
.1483
.1350
.1205
.1055
.0915
.0800
.0720
.0625
.0540
.0475
.0410
.0348
Weight
one mile,
pounds
1128.0
970.4
836.4
714.8
6034
S19 2
441.2
369.6
309 7
256.7
204. 5
156.7
117. 9
90 13
73 01
55 01
41.07
31-77
23.67
17.05
Feet to
pound
4.681
6.313
7.386
8.750
14.29
17 OS
20.57
25.82
33.69
44 78
58.58
72.32
95 98
128.6
166.2
223 o
309.6
Iron Wire
147
Iron Wire
Measured by Washburn & Moen gauge. List prices per pound.
No.
0000 to 9
10 and II
12
13 and 14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
* Bright
market wire
$0.10
.11
.11^2
.12}.^
.14
.14
IS
.16
■ 19
.20
.21
.22
.23
.24
.25
.26
.28
.29
.30
.32
.33
.35
.37
.40
• 45
• 55
Galvanized
market
wire
$0.10
.11
.iiH
.12}.^
.14
.14
.IS
.16
■ 19
.20
.21
.22
.23
.24
.25
.26
.28
■29
.30
.32
.33
.35
.37
.40
• 45
.55
Annealed
stone wire,
bright or
black
$0.14
.15
.16
■ 19
.20
.21
.22
.23
.24
.25
.26
.28
■ 29
.30
.32
.33
.35
.37
.40
.45
.55
Tinned
market
wire
$0.15
.16
.17
.17
.I7'/2
.I7'/2
.18
Tinned
stone
wire
i8>/^
19
19
20
20
* Coppered Market Wire and Coppered Bessemer Spring Wire take same list prices
as Bright Market Wire.
148
Ma(cri;il.s
Nails and Tacks
< oiiuii'jii Wire N.u!
Measured by \S'ashburn & Mocn Gauge
Size
Length and gauge
Approx.
,
Inch
No.
pound
2d
I
IS
876
3d
lU
14
S68
4d
iMi
I2!i
316
Sd
m
12h
271
6d
2
11! -J
281
7d
2W
n!-v
161
8d
2\i
loU
106
9d
2H
loU
96
lod
3
9
69
1 2d
iV*
9
63
i6d
SH
8
49
20d
4
6
31
3od
4'A
5
24
4od
5
4
18
sod
sH
3
14
6o<l
6
2
II
Length axd Number of Tacks to the Pound
Name,
Length,
No. to the
Name,
Length,
No. to the
ounces
inches
pound
ounces
inches
pound
I
H
16,000
10
>H»
1600
iM
^.
10,666
12
H
1333
2
M
8,000
14
'^«
1143
2\.\
M.
6,400
16
%
1000
3
H
S.333
18
>M«
888
4
Mo
40,000
20
I
800
6
^a
2,666
22
iMb
727
8
%
2,000
24
1^
666
United States Standard Threads
United States Standard Threads
149
Nominal
diameter of
screw,
inches
No. of
threads
per
inch
Diameter of
tap at root of
thread
Size of tap
drill, giving a
clearance of
i-i the height of
the original
thread triangle
Area at
root of
thread,
square
inches
Safe load
on threaded
bolt on
basis of
6000 pounds
stress per
sq. in. of
section at
Inches
Nearest
64ths
Inches
Nearest
64ths
root of
thread,
pounds
H
.250
20
.185
?16 -
.196
'3/64-
.027
162
Me
.312
18
.240
15-64 +
.252
1/4 +
.045
270
%
.375
16
.294
1^64-
.307
Via —
.068
408
•'M
.437
14
.345
M42 +
.360
2%4 +
.093
558
H
.500
13
.400
1?42-
.417
2J64-
.126
756
^Ae
.562
12
.454
2?64 +
.472
1542 +
.162
997
n
.62s
II
.507
1/i +
.527
^%2-
.202
1,210
iMe
.687
II
.569
?i5 +
.589
l?i2-
.254
1,520
H
.750
10
.620
% -
.642
*Hi +
.302
1,810
1^6
.812
10
.683
iHe-
.704
*%4 +
.366
2,190
■'A
.875
9
.731
*'Ai-
.755
3/4 +
.420
2,520
1^6
.937
9
.793
5^4-
.817
13/'16 +
.494
2,960
I
1. 000
8
.838
21:^2-
.865
55/64 +
.551
3.300
iHe
1.062
8
.900
2932-
.927
5?64 +
.636
3,810
iH
1. 125
7
.939
1^6 +
.970
31/^2 +
.694
4,160
. 1^6
1. 187
7
1.002
I +
1.032
l!'^2 +
.788
4,720
iH
1.250
7
1.064
1M5 +
1.095
l3/fe +
.893
5,350
iH
1.375
6
1. 158
I5i2 +
I. 215
ij;i2 -
I.OS7
6,340
i\i
l.Soo
6
1.283
l%2 +
1.345
lH/i2 +
1.295
7.770
iH
1.625
5'/-2
1.389
125/64-
1.428
I2%4 +
1.51S
9,090
m
1.750
5
1.490
13164 +
1.534
117/^2 +
1.746
10,470
1%
1.87s
5
1. 615
13 964 +
1.659
l2I/^2 +
2.051
12,300
2
2.000
4H
1. 711
12 3/^2-
1.760
l*%i-
2.302
13,800
214
2.250
Ali
1. 961
16I/64 +
2.010
21-64 -
3.023
18,100
2H
2.500
4
2.175
211/64 +
2.230
215.64-
3.719
22,300
2%
2.750
4
2.425
22%4 +
2.480
231/64-
4.620
27,700
3
3-000
3I/6
2.629
2H +
2.691
211/16 +
5.428
32,500
354
3-250
3M2
2.879
2^/8 +
2.941
21^6 +
6.510
39.000
3H
3- 500
3H
3.100
33/^2 +
3.167
3i'/64-
7.548
45,300
3%
3 750
3
3.317
3^6 +
3.389
325/64-
8.641
SI. 800
4
4.000
3
3.567
3^6 +
3.639
3*'/64-
9.963
59.700
I50
Materials
JB
CO
1
1
•UI -bs
jod •sqi
OOO'OI )v
» M ri "^ ■* "^ **> * O « JO 1^ O jj Q t "O
•UI -b*
iad 'sqi
ooSi IV
1
•UI 'Ijs
»d' -sqi
ooo'oi ^v
•UI -bs
JDd* •sqi
ooSi JV
«• - « c, -^ ^ « r: rf. -■ ;j uj« Jj 5 g.^ 5
a
s
•ui -bs jad
•sqi ooS'ii IV
•UI -bs J3d
•sqi ooS'zi IV
•UI -bs J3d
■sqi ooo'oi ;v
<
JO uiOMOg
S i>8 8- 2 "S 8 ft ^ K^'g g S" « ? ? ft S ;i5
««MM««.^r^*
v.og
?&s:?2'S^ft?5'SS;S's^'&&%'R^s;S.5
«««•«■«■« r^ r^ ^ «
\ri \n \fi
Nioi>. dio »o »o tn tn m
1
s
pKJjqi
JO uio;;oa
liirillBlilfllllilsl
-;»;„„«»-■«•««
^|gis = sii^?^SH'Ss^i§i:
iHM»i-i»i-ir4NnnMr>jrofO-<r«'<r
QOl/^r^ 0O»/^ 1/^ lO lO »0 Ifl
10ulCSl--OOS>0«'*<000 >-if»)l/5t~O>i->IO00C1
Mi-Jl-jMMCIM'citiNcifOfOW'T
1
qoui
jad sprajqx
Ifl lO lO
oco^ -j-roM M o o>oo t-t-<o<o in VI \n ■^ ■^ -9 -9
4»1
aiUEIQ
tn irt in
nu^t^ Mi/> lo in m in in
iflKii^ro vontnt^ Mil-. r~ r»iot~ xn m
Nr*)ro.tti/5io(or-oo HI n r<i m lo t^ oo wior*
M w M «' « l-i >.i « « « ei M
United States Standard Bolts and Nuts
151
^ioiovo"difOt~*Nr*ioN N
10 "O t-- 00 c^ I
w -^ 10 t>- a» M
00 o^oo o*r*r^"^'*^o%c?*»oo
Oi-.i-i5-<3-t^ioiO'^" «.«..
t*-Q0<Ococ^Ch»o^O N
^ ^ 10 "O t^ 00 a»
o o
10 rr
■^ dl po
po '^ 10 r*
000 M t^-<tfOfO»00»/^r^Nf*?
^Cft<S'«t«ooq QwrO'^io'Ot^
0N»O o'"^'-^"cfit^OvOr^Ch(N
10 0% 00 10 00 t^ N
M i-r 10 "^ "^ Oi 00
q (N »H 00 (N r^ IN
»o^ r* 00 a. o I-.
fO O t» TT I
- ^ r* o^ t-(
N
low o^Mio O^O^o^f^-^r^iot^
OOwO <N t^t^lOlOO tOOOOOlO
CftChM (Sob C^ O>00CTtlOi-i o »-<
^fONMrfoCNodlOt^t^N-^
C^M roiOt-*O^N ^r^Qf^t^O
wi-iMM(NC(C»rorOfO'^
VO lO^lOMOO^OO ^t-tOO lOT
rMO^O M i-H (N loiot^oo -^OOO
tCi-r^QO-rtM(^fClCo%dlOOO
^OOO 0*0 <N -rJ-lOt^Oi-t '^t'OOO
MMMMI-tMtSOIC^OI
t"2i!:i<^cn<N loioo^iooo o t>-
Ttioio*ooifOt^ofrCiocf<>Jo
io<o t*ooa>t-t cs -^lot^o^M ro
MMMihMMWN
r*w M n o^N lotoo^iooo o t*
t>-OiO*MW do 0»OTtt^NTl-
WO '*^0*rO'^N»0 r>-tO lOQ^
':flOlOVOO>rot-(S t~*lON « O
10*0 r*0O 0»M N Tfiot-^crkt-i fO
MI-IIHI-tlHI-t(N(N
^00 t-c t-^TTPOroioOior^N fO
00 lOM ^VOO -rfO »Ot-00 t--'^
^O^ri rj-^ooo O f^ roi-iO>Ot^
t^coo»M w Tj-ior^o^M fvjiooo
l-<MMMI-ltHtS(N(NIN
»o 10 10 to 10 10 to
N l>lOC^ t-lON l>.lON
M QOt^^DlOrO(NM OOt^tO
rOlOvOOOON'ttOOO MfOiO
W N N ci POrorOfOrO'^'^Tt-'^
N10t>> MIOt>> MIOt*
fOfO(OrO'^^Tf'*tio»o»oio*o
00
^
fO
0
0
IN
lO
^_^
X
,«
«
Ht
ro
t^
0
ts
1-
t-
01
^
n
M
fO
CO
PO
to
-*
Tf
"i-
T
•*
10
10
0
0
<)
M
^J
„
M
-N
M
»
t^
r^
r^oo
n
VO
t^
t~ 00
00
cr>
01
0
0
"
M
M
M
2
N
m
IS
„
^
^
<o
ro
M
10
10>0 >£>
«^
r~
r~oo
00
o>
o>
0
0
<0 fOt^-MloOOtN^ fOt^iH
-<3-io»oio^ioio t^t^ooodod 0%
lo »o 10 10
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f^ fo po fo r*^ <N oi w ci ci ci ci o)
MIOC^ NlOt^ NlOt*
f^fOforo^^^^ioioioio^o
IS2
Materials
Nuts and Washers, Number to the Pound
United States Standard Nuts
Approumatc Number in One Hundred Pounds
Hot pressed
Cold punched
Size of
bolt,
inches
Blank Tapped
Plain
Chamfered,
trimmed and
reamed
Square
Hexagon
Square
Hexagon
Square "«""
Square
blank
Heia-
blank
H
^
Vi
91 »
5i
9i
1
iH
iM
iH
iV4
iH
1%
iJ6
2
2H
2H
2ji
2V^
2%
3
7200
4010
2540
I7S0
1 17s
910
6SS
387
260
172
133
98
73
58
. 44
38
31
25
20
18
15
12
9
7
8400
5300
3070
2080
1430
1030
798
479
31S
216
ISS
114
91
73
57
41
39
32
25
21
20
16
II
8^4
7SOO
4SOO
2720
1900
1250
980
700
408
264
176
139
lOI
77
61
49
40
33
27
21
18' J
15^4
12^^
9^4
7.4
9000
SSoo
3200
2170
IS12
1150
850
528
332
230
180
129
96
77
60
44
40
33
26
22
20Vi
16'/^
II.4
9
6700
4100
2400
1550
HOC
82s
580
348
228
156
122
88
65
54
42
33
27
23
19
17
7S0O
4700
2800
1830
1300
990
700
438
290
198
140
103
77
63
SO
39
31
28
24
30
7400
4000
2730
1700
1 160
900
653
386
360
170
133
90
69
54
43
35
29
24
3oV4
17
IS
12
8880
4800
3276
3040
1392
1080
784
463
312
304
146
108
83
6s
53
43
35
29
36
23
30
16
Wrought Steel Plate Washers
Wrought Steel Plate Washers
153
Fig. 41.
In 200-pound Kegs. List prices per 100 pounds.
Thickness,
Size of
Outside
Size of hole.
English
Approximate
Per 100
bolt,
diameter,
inches
standard
number in
pounds
inches
inches
wire gauge
100 pounds
No.
^6
9^6
'/4
18
44.075
$14.00
H
Vi
5i6
16
13,845
12.20
Me
li
H
16
11,220
11.40
%
I
lU
14
6,573
10.50
Mb
iH
Vi
14
4,261
9.70
H
i?6
9i6
12
2,683
9.20
?i6
iH
^6
12
2,249
9.10
5i
1%
'Me
10
1,315
9.00
H
2
i^ie
10
1,013
8.80
-;i
2V4
15/19
9
858
8.80
I
2^
iH
9
617
8.80
1^6
2H
i54
9
S16
8.80
IW
3
i?6
9
403
9.00
1%
3»
r\'i
8
320
9.00
m
3^^
i^i
8
278
9.20
m
3%
i?4
8
247
9.20
1%
4
iji
8
224
950
i?6
4«
2
8
200
9. SO
2
4V'2
2\^
8
180
9 50
In ordering, always specify size of bolt.
Fig. 42.
Showing Lock Washer on Bolt.
When the nut is screwed upon the bolt, it first strikes the rib on the
lock washer, which, being harder than the nut, progressively upsets
and forces some of the metal of the nut into the thread of the bolt,
thereby preventing the nut from backing off or loosening.
Can be used on any make of bolt or nut. The same bolt, nut and lock
washer can be used as often as required.
Prices upon receipt of specifications.
IS4
MutcriaLi
r
l-IG. 43.
The positive lock washer is so constructed that the "body" of the
washer carries the load of compression and the tapered ends are thus
rehevcd and the spring is constant. The barbs, being free to move when
subjected to vibration, force themselves deeply into the nut and metal
backing.
Are reversible and can be used many times. Do not injure the nut,
its thread, or the threads of the bolt.
Machine Bolts
155
Machine Bolts
Approximate Weight per 100 of Machine Bolts with Square
Heads and Square Nuts
Length
K4
Me
H
Vie
H
9i«
^
Pound
Pound
Pound
Pound
Pound
Pound
Pound
H
2.55
4.4
7.71
10
%
2.64
4.65
8.04
10.53
I
2.73
4-9
8.36
11.03
15.5
19.8
28.95
iV*
2.9
5-4
9.01
II. 9
16.7
21.6
30.89
iH
3.08
5.9
9.66
12.8
17-9
23.4
31 83
2
3-43
6.8
10.94
14. 5
20.4
27
36.7
2M2
4-45
7.8
12.74
17.25
24.91
31. S
41. 55
3
5.45
8.7
14.37
18.75
27.64
33 I
45. 4
3H
6.46
9.7
15.83
20.90
29.74
36.7
49.28
4
7.09
10.7
17.3
23.09
32.89
40.3
53-16
4H
7-7
II. 7
18.76
25.27
34.98
43
57 04
S
8.3
12.7
20.2
27.50
36.01
47.3
61.9
sH
8.9
13.7
21.58
29 59
38.61
SO. 9
65-77
6
95
14-7
22.95
31.68
41.22
52.9
68.9
6}^
10.2
15.7
24.42
33-9
43.82
56. 5
72.77
7
10.8
16.7
25-9
35.73
46.42
60.7
76.71
7W
II S
17.7
27-37
37.56
49.02
64 -3
80.58
8
12. 1
18.7
28.84
39
SI. 64
67.9
84-45
9
13.4
20.8
31.8
43.18
56.84
75. 1
92.19
10
14.6
22.9
34.75
47.36
62.04
82.3
99 94
II
15.8
24.9
37-7
51.6
67.24
89.5
107.69
12
17
26.9
40.65
55.76
72.44
96.7
IIS. 44
13
18.2
28.9
43-6
59-92
77.64
103.9
123.19
14
19 4
31. 0
46.55
64.20
82.84
III. I
130.94
IS
20.6
33
49.5
68.36
88.04
118. 3
138.69
16
21.8
35
52.45
72.52
93.24
125. 5
146.44
17
23
37
55.4
76.68
98 -44
132.7
154.19
18
24.2
39
58.35
80.84
103.64
139 9
161.94
19
25-4
41
61.3
85
108.83
147. 1
169.69
20
26.6
43
64.25
89.16
114.04
154. 3
177.44
21
27.8
45
67.20
93 32
119.20
161. s
185.19
22
29
47
70.15
97.48
124.44
168.7
192.94
23
30.2
49
73- 1
lOI . 64
129.6s
175.9
200.69
24
31.4
51
76.0s
105.80
134-80
183. 1
208.44
25
32.6
53
79
109.96
140.04
190.3
216.19
26
33.8
55
81.9s
114. 12
145-24
197. 5
224.94
27
35
57
84.9
118 28
150.44
204.7
232.19
28
36.2
59
87.8
122.44
155 64
211. 9
240.44
29
37.4
61
90. 75
126.60
160.84
219. 1
248.24
30
38.6
63
93.7
130.76
166.04
226.3
254.94
156
Materials
Approximate Wkiomt pi :r ioo of Macuine Bolts with Square
'! ,iUAR£ Nuts — {Continued)
Length
Poun<i
Pound
I
Pound
Pounds
i
Pounds
Poondf
9*
I
47.63
iW
SO. 10
iH
52.57
81.25
3
S7.6
90.63
137.50
178.00
233. 37
aW
63 44
98.63
149 10
192.87
253 75
3
69.84
106.3
160.75
207.75
372.12
■■458"
3«
7S.93
114.30
171.55
222.62
290.50
483
4
81.77
122.30
182.35
237.50
308.88
S08
4H
87.61
130.30
193.15
232.38
327.25
533
5
93 -45
138.30
203.90
267.25
345 63
SS8
SH
99 46
146.30
214.75
282.13
364.00
583
6
105. 13
154.30
225.65
397.00
382.37
608
16!^
III. 14
162.30
236.35
311.87
399 22
633
7
117. IS
170.30
247. IS
316 75
416.07
6s8
7W
123.16
178.30
257. 95
321.62
432.92
683
8
139.17
186.30
268.75
336.49
449 77
708
9
141. 19
202.30
290.35
366.23
483 47
7S8
lo
153.21
218.30
311.95
395.98
S17.17
808
II
165.23
234-30
333. 55
425.73
SS0.87
858
12
177.2s
250.30
355.15
455.48
584.57
908
13
189.27
266.30
376.75
483.33
618.27
958
14
201.29
282.30
398.35
514.98
651 97
1008
IS
213-31
298.30
419.9s
544. 73
685.67
1058
l6
225.33
314.30
441. 55
574.48
719.37
1108
17
237 35
330.30
463.15
604.23
753 07
11S8
l8
249 37
346.30
484.75
633.98
786.77
I308
19
261.39
362.30
506.33
663.73
610.47
1258
20
273.41
378.30
527.95
693.48
844 17
1308
21
285 . 43
394 30
549 55
723.23
877.17
1358
22
297.45
410.30
571.15
752.98
911-57
1408
23
309.47
426.30
592.75
782.73
945.27
1458
24
321.49
442.30
614.3s
812.48
978.97
IS08
25
333. SI
458.30
635.93
842.23
1012.67
1558
26
345. S3
464.30
657.35
871.98
1046.37
1608
27
357. 55
480.30
679 15
901.73
1080.07
1658
28
369.57
496 30
700.7s
931 48
1113.77
1708
29
381.59
512.30
722.35
961.23
1147.47
1758
30
393.61
528.30
743 95
990.98
1181.17
1808
These weiRhts are for bolts with bolt size nuts, and with heads of diameter equal
to ij-i times diameter of bolt, and thickness equal to }i times diameter of bolt.
Machine Bolts
157
Machine Bolts with Square or Button Heads, Square Nuts
AND Finished Points
Adopted Sept. 20, 1899, to take effect Oct. i, 1899. List prices per 100.
Length,
Diameter, inches
inches
?l6
Vi
}is
%
yie
H
and
H
'A
I
iH
iH
tH
$1.70 $2
.00 $2
.40
$2.80
$3.60
$5.20
$7.20
$10.50
$15.10
$22.50
$30.00
2
1.78 2
.12 2
.56
3
00
3.86
5. 58
7.70
11.20
16.00
23.70
31.50
214
1,86 2
.24 2
.72
3
20
4.12
5.96
8.20
11.90
16.90
24.90
33.00
3
1.94 2
.36 2
.88
3
40
4-38
6.34
8.70
12.60
17.80
26.10
34.50
3H
2.02 2
.48 3
.04
3
60
4.64
6.72
9.20
13.30
18.70
27.30
36.00
4
2.10 2
.60 3
.20
3
80
4.90
7.10
9.70
14.00
19.60
28.50
37.50
4H
2.18 2
.72 3
.36
4
00
5. 16
7.48
10.20
14.70
20.50
29.70
39.00
5
2.26 2
.84 3
.52
4
20
5.42
7.86
10.70
15.40
21.40
30.90
40.50
5H
2.34 2
.96 3
.68
4
40
5.68
8.24
11.20
16.10
22.30
32.10
42.00
6
2.42 3
.08 3
.84
4
60
5.94
8.62
11.70
16.80
23.20
33.30
43.50
6]^
2.50 3
.20 4
.00
4
80
6.20
9.00
12.20
17.50
24.10
34.50
45.00
7
2.58 1 3
■ 32 4
.16
5
00
6.46
938
12.70
18.20
25.00
35.70
46.50
7Vi
2.66 3
.44 4
32
5
20
6.72
9.76
13.20
1S.90
25.90
36.90
48.00
8
2.74 3
.56 4
48
5
40
6.98
10.14
13.70
19.60
26.80
38.10
49.50
9
2.90 3
.80 4
80
5
80
7.50
10.90
14.70
21.00
28.60
40.50
52.50
10
3.06 4
.04 5
12
6
20
8.02
11.66
15.70
22.40
30.40
42.90
55.50
II
3.22 4
.28 5
44
6
60
8.54
12.42
16.70
23.80
32.20
45.30
58.50
12
3.38 4
.52 5
76
7.
00
9.06
13.18
.17.70
25.20
34.00
47.70
61.50
13
... 6
08
7.
40
9.58
13.94
18.70
26.60
35.80
50.10
64.50
14
... 6
40
7
80
10.10
14.70
19.70
28.00
37.60
52.50
67.50
IS
... 6
72
8.
20
10.62
15.46
20.70
29.40
39-40
54.90
70.50
16
... 7
04
8
60
II. 14
16.22
21.70
30.80
41.20
57.30
73.50
17
.
... 7
36
9-
00
11.66
16.98
22.70
32.20
43.00
59-70
76.50
18
.
... 7
68
9.
40
12.18
17.74
23.70
33.60
44.80
62.10
79 50
19
... 8
00
9.
80
12.70
18.50
24.70
35 00
46.60
64-50
82.50
20
... 8
32
10.
20
13.22
19.26
25.70
36.40
48.40
66.90
85. SO
21
13-74
20.02
26.70
37.80
50.20
69.30
88.50
22
14.26
20.78
27.70
39.20
52.00
71.70
91 SO
23
14.78
21.54
28.70
40.60
53.80
74.10
94.50
24
15.30
22.30
29.70
42.00
55. 60
76.50
97.50
25
15 82
23.06
30.70
43.40
57.40
78.90
100.50
26
31.70
44.80
59.20
81.30
103 so
27
32.70
46.20
61.00
83.70
106 . 50
28
33.70
47.60
62.80
86.10
109.50
29
34.70
49.00
64.60
88.50
112.50
30
35.70
so. 40
66.40
90.90
115. SO
Bolts with hexagon heads or hexagon nuts, 10 per cent advance.
If both hexagon heads and hexagon nuts, 20 per cent advance.
Machine bolts with countersunk head, joint bolts with oblong nuts, bolts with
tee heads, askew heads, and eccentric heads, 10 per cent advance.
Bolts with cube heads, 20 per cent advance.
Bolts requiring extra upsets to form the head, 20 per cent advance for each extra
upset.
Special bolts with irregular threads and unusual dimensions of heads or nuts will
be charged extra at the discretion of the manufacturer.
Bolts with cotter pin hole, prices upon application. In ordering bolts with cotte*'
pin hole, state size of hole, and distance from end of bolt to center of hole.
158
Materials
r ■■ T
Bolt Ends and Lag Screws
Bolt Ends Fittku with Squark Nuts*
Adopted Jan. 30, 189s. to take effect Feb. 14. 1895.
List prices pt:r pound.
Fig. 44.
Flu
•45-
Size of
iron,
Length,
Length
of thread.
Price per 1
Size of
iron,
Length,
Length
of thread.
Price
per
inches
inches
inches
pound
inches
inches
inches
pound
9<.
6
I
So. 20 1
1^6
13
4''J
$0.10
%
7
iW
18
iM
14
S
{I
M«
7
lyi
16
iH
IS
5^2
H
8
2'.2
14
iVi
16
6
H
9
3
12
iH
17
6W
?4
10
3H
10
i?4
18
7
li
II
3V^
10
I'A
19
7W
.13
I
12
4
10
2
20
8
.12
• With hexagon nuts, ro per cent advance.
Prices of bolt ends shorter than above standard lengths will be quoted upon appli-
cation.
Weights of Nuts and Bolt Heads in Pounds
159
Coach Screws with * Square or Washer Heads; Gimlet Points
List prices per loo.
Diameter, inches
Length,
inches
and
5^6
%
y^e
H
?i6
and
H
?i
I
1 1/2
2
2}.^
3
3H
4
4!'2
5
sH
6
6H
7
■71^
8
9
lO
II
12
$2.25
2.45
2.65
2.85
3.05
3-25
3-45
3.65
3.85
4 -05
$2.70
2.96
3.22
348
3.74
4.00
4.26
4.52
4.78
5.04
$3.15
3.47
3.79
4. II
4.43
4. 75
S-o?
5-39
5. 71
6.03
6.35
6.67
6.99
7-31
7.95
$3
4
4
4
5
5
5
6
6
6
7
7
8
8
9
9
10
II
.75
.11
■ 47
83
19
55
91
27
63
99
35
71
07
43
15
87
59
31
$6.00
6.50
7.00
7.50
8.00
8.50
9.00
9. SO
10.00
10.50
11.00
II. SO
12.00
13.00
14.00
15.00
16.00
$9.20
9.90
10.60
11.30
12.00
12.70
13.40
14.10
14.80
IS. 50
16.20
16.90
18.30
19.70
21.10
22.50
$15.00
16.00
17.00
18.00
19.00
20.00
21.00
22.00
23.00
24.00
25.00
27.00
29.00
31.00
33.00
$22.00
23.30
24.60
25.90
27.20
28.50
29.80
31.10
32.40
33.70
36.30
38.90
41.50
44.10
Coach screws with hexagon and tee heads, 10 per cent advance.
Weights of Nuts and Bolt Heads in Pounds. Kent
For calculating the weight of long bolts.
Diameter of bolt, in inches
Weight of hexagon nut and head
Weight of square nut and head
H
.017
.021
.057
.069
1/^
.128
.164
.267
.320
H
.43
ss
.73
.88
Diameter of bolt in inches
I
1. 10
1. 31
i'/4
2.14
2.56
3.78
4.42
5.6
7.0
2
8.75
10.50
2H
17
21
3
Weight of hexagon nut and head
Weight of square nut and head
28.8
36.4
i6o
Materials
*j?^^^8 r-a»,8 i^asc- 8
3'ft "2 S. a'fe% S 3 C 2 3, IJIJ
w 9
li w
a .u
w «
0
o
82
»R
^
!?8<8 J?iSR8
52$
f
!?"£
« w
o>
M f? cT'8 5^ s" I^
!^;?
0000 cr>b o «-• ci ^^-rlot*odc^p^J jj
;?s'!^2.!55 8a^&^8sia^8
foftvS SvN'S ^IS2 iC^lJooRS
lOioi/^u^O'O t^t^oooo a>o O ^ N
OO OOOiOi'JOi^OO"^
OJ3
&
•s-fi
R g
s.s
5 ti
3 bj
H
O O O w^ w^ i/^
o% pcaq jspun (saqon;) q;3aaq
•€ -^
Cap Screws
i6i
Fig. 46.
On all screws of one inch and less in diameter, and less than four inches
long, threads are cut f of the length. Beyond four inches, threads are
cut half the length.
Regular cap screws are soft and have ground heads. Special prices
on black heads, extra finished and case hardened screws.
Cap screws with over-sized heads take the list of regular cap screws
with the same-sized heads.
Price of steel screws will be 25 per cent above the price of iron.
U)2
Materials
Drop-Fokged Turn-Buckles
yYithOft Stubs
Fig. 47.
With right and left U. S. Standard thread.
List prices with and without stubs.
Diameter of
stub, inches
Inside opening
Length over all
of buckle.
(including
Each
inches
stubs), inches
y*
3
14
$0.36
^.
3
14
.38
H
S
jgH
• 40
lU
S
19H
.42
Vi
6
21
• 45
Vi
9
24
.56
9^«
6
22
.48
5i
6
23
• SO
5i
9
26
.63
%
6
23
.63
H
9
26
■79
?6
6
23
■ 75
^i
9
26
■94
I
6
23
.88
I
9
26
1. 10
i\i
6
24
1.00
iH
9
27
I2S
iH
6
25
I 25
iM
9
28
I^S6
iH
6
26
1.38
iH
9
29
I 73
iH
6
26
i^So
lyi
9
29
1.88
iH
6
26
1.75
iH
6
27
2.00
1%
6
28
2.25
2
6
29
2.6s
Drop-Forged Turn-Buckles
Drop-Forged Turn-Buckles
163
With One Eye anal One Hook
W!ih Two Eyes
(6)^^^^<I^^^S^)^=^6)
with Two Hooks
Fig. 48.
With right and left U. S. Standard thread.
List prices with either one hook and one eye, two eyes, or two hooks.
Diameter
of
threaded
Inside opening
of buckle, inches
end,
inches
3
5
6
9
12
15
18
24
36
48
72
y*
I0.40
Mb
• 45
?i
to. 65
H
$0.72
So. 85
$0.95
$1.15
5i
.80
• 95
1.05
1.30
$1.55
$2.05
H
1. 10
1.25
1. 00
1.70
2.00
2.6s
J6
1.35
1. 55
1.70
2.10
2.45
3.20
I
1.65
1.8s
2.05
2.50
2.9s
3.80
$4.25
iH
2.10
2.35
2.55
3.05
355
4-55
5.0s
iH
2.65
2.95
3-25
3.90
4.50
5-75
6.40
$8.90
iH
3. IS
3-45
3.80
4.50
5.20
6.60
7.25
10.00
iH
3.70
4.05
4.4s
5.20
5.9s
7-45
8.20
11.20
$14.20
iH
4.65
5.50
6.40
7-25
9.00
9.90
13 40
16.90
1%
S.30
6.40
7.40
8.40
10.40
11.40
15-40
19.40
i^/i
6.50
7.60
8.75
985
12.10
13.25
X7.7S
22.25
2
7.7s
9.10
10.40
11-75
14.40
15-75
21.00
26.30
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Thumb Screws 165
Thumb Screws, Drop-Forged Steel, Threaded, U. S. Standard
Fig. so.
Can be furnished in styles A to F.
List prices per loo.
Diameter,
inches
'/^
>i6 H
5/16
H
Vts
H
9l6
%
H
Threads
per inch
40
24 20
18
16
14
13
12
II
10
f H
$3.20
1-
5.60 $4.10
$4.80
Ss.go
H
3.
40
J. 80 4
30
S.oo
6.10
$7.60
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811.70
?4
3-
5o
too 4
so
S.20
6.40
8.00
10.00
12.40
OJ
I
3.
So
t.2o 4
70
5.50
6.80
8.50
10.60
13.10
$16.00
$23. 10
X
iV4
4-
XI
»-4o 4
90
5. 80
7.20
9.00
11.20
13.80
16.80
24.40
C
i!-^
4-
20
t.6o s
10
6.20
7.60
9.50
11.90
14.60
17.80
23.80
•d
1%
1.80 5
40
6.60
8.10
10.10
12.60
15.50
18.80
27.20
g
2
>oo 5
70
7.00
8.60
10.70
1.^.30
16.40
19.90
28.60
J3
•0
2H
... 6
10
7.40
9.20
11.40
14.10
17.30
21.00
30.10
2H
... 6
so
7.90
9.80
12.10
14.90
18.30
22.10
31.60
a
;3
2%
... 6
90
8.40
10.40
12.80
15.80
19.30
23.30
33.10
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3
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40
8.90
11.00
13 so
16.70
20.30
24.50
34.70
ti
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10.00
12.30
IS- 10
18.50
22.50
27.00
38.10
c
4
11.20
13.80
16.90
20.50
24.80
29.70
41.50
hJ
4V4
15-40
18.70
22.70
27.40
32.70
45 .20
5
17.00
20.70
25.20
30.. 30
36.00
49.60
S^
18.80
22.90
27.80
3330
3960
S4-30
L6
30.40
36.60
43.60
60.00
i66
Materials
Round Ukau Ikon Rivets
Approximate number in one pound.
Diameter of
wire
Length,
inches
W
o
^io
I
2
3
y*
4
5
6
%e
7
8
9
H
154
188
221
2S6
3.M
M
32
42
SI
57
6s'
7S
80
89
108
131
IS9
I8S
21S
278
H
29
37
4S
SO
S7
67
70
78
94
114
138
158
I8S
238
H
26
33
41
4S
SI
S9
63
70
84
lOI
123
139
163
ao8
H
24
30
37
41
46
S4
S7
63
75
91
109
123
I4S
185
I
23
28
34
39
42
49
S2
57
68
82
98
III
131
166
iH
20
26
31
34
39
4S
47
S3
63
75
90
101
119
151
m
19
24
29
32
36
42
44
49
58
69
83
93
109
138
iH
i8
33
37
29
33
39
41
45
54
64
76
86
lOI
127
IW
17
31
3S
38
31
37
38
42
51
59
71
80
94
119
iH
IS
I8
33
24
27
33
34
40
44
55
63
70
83
104
3
13
17
30
22
2S
29
30
35
40
47
S6
62
73
92
2H
12
15
i8
19
22
37
28
33
36
42
SO
S6
66
83
2W
II
14
17
18
20
24
2S
39
33
39
46
SO
60
75
2?<
lO
13
IS
17
19
22
23
36
30
36
43
46
55
67
3
9
13
14
IS
17
21
23
24
28
33
39
43
SI
64
3M
m
II
13
14
16
19
30
33
26
31
36
40
47
59
zVi
8
loH
12
13Vi'
IS
18
19
21
24
29
34
38
44
55
3?4
7H
9?i
11%
12%
14
17
18
20
23
27
32
35
41
52
4
7H
9H
II
12
13
16
17
18
21
25
30
33
38
49
4H
7
8^
I0V2
iiH
12%
IS
16
17
20
24
4V^
6)^
8^4
10
10%
12
14
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16
19
23
4%
6M
8
9V4
10
IlH
13%
14%
15%
18
23
5
6
7H
9
9%
II
13
14
15
17
21
SH
5^4
7K4
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9H
loV^
I2H
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I4V^
16H
20
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SH
7
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9
10
12
13
14
16
19
5^4
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7^4
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9H
iiV^
I2Vi
13H
15
18
6
5
6H
7V^
m
9H
II
12
13
14
17
3VS cents per pound, net.
Dimensions of Standard Wrot Pipe
167
Dimensions of Standard Wrot Pipe
(U
x:
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3
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2.339
2.07
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2.467
2.87s
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2.62
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2.82
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3.441
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3.938
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4.233
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4-434
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4.508
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4.733
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5.04s
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6.06s
6.62s
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1.26
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7.023
7.62s
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1.36
7.54
7.02
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7.981
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8^332
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1.46
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7.98
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8.937
9.62s
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9.324
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8.93
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10.018
10.75
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1.68
10.645
10.02
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11.75
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11.639
11
12
12
12.75
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■ 375
8
12.433
I22%4
1.90
12.633
12
13
13.25
14
14
375
8
13 675
13* %4
1.98
13.875
13.25
14
14.2s
15
15
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8
14^668
142^^2
2. IS
14.869
14.2s
IS
15.2s
16
16
• 375
8
15 662
152^2
2.21
15.863
15 25
16
16.25
17
17
.375
8
16.656
162^2
2.30
16.856
16.25
17
17.25
18
18
.375
8
17 65
1721/^2
2.40
17.85
17-25
18
18.25
19
19
• 375
8
18.644
18* •^4
2.50
18.844
18.25
19
19.25
20
20
.375
8
19 637
19?6
2.59
19 837
19 .25
20
20.25
21
21
• 375
8
20.631
20H
2.72
20.831
20.25
Taper of conical tube ends ^4 inch in diameter in 12 inches.
Contributed by Louis H. Frick. No. 74, Extra Data Sheet, Machinery, October,
1907.
Seamless drawn brass and copper tubes are made by American
Tube Works, Boston, Mass.; Ansonia Brass and Copper Co., Ansonia,
Conn., office 19 and 21 Cliff St., New York; Benedict & Burnham Mfg.
Co., Waterbury, Conn., oflSce 13 Murray St., New York; Randolph &
Clowes, Waterbury, Conn., and Bridgeport Brass Co., Bridgeport,
Conn. The following sizes are kept in stock, in 12 feet lengths, by
Merchant & Co., 517 Arch St., Philadelphia. The five columns signify
as follows:
A = outside diameter of tube in inches.
i6S
Mali-rials
B = thickness of side by Stubs' (or Birmingham) gauge. When
seamless tubes are ordered to gauge number, it is un<ierst<xxi thai this
gauge is intended unless otherwise s|)eiiried.
C = thickness of sides of tube in decimals of an inch.
D = weight, in pounds per lineal fo<jt, of brass tube for columns A,
B and ('. n'or loiipir. .nld one tiinetcenth).
Tubes will be furnished hard, unless ordered annealed or soft.
.1
yj
C
U
.1
B
C
1
1.
2\<l
B
r
.109
/>
w
i8
.049
.11
m
13
09s
1.68
13
J. 03
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II
120
2.10
2',i
10
.134
3.68
96
17
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072
1.40
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14
083
2 44
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17
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■25
l94
14
083
1. 61
2H
13
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3.18
W
17
.058
• 29
I?4
13
09s
1.82
2H
10
■ 134
3.87
Mo
17
.058
•34
iVa
II
120
2.27
294
14
.083
2 57
H
i6
.06s
■ 42
m
IS
072
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29«
12
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3 37
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• SI
m
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294
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4 07
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m
13
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1.96
2>A
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• 70
1-6
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120
2 41
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4.26
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4 8s
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1. 12
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3'/4
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8.72
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Merchant & Co. supply sizes up to 7 inchis ouij-idc <>r inside diameter,
and up to 16 inches inside diameter, of other gauges as well as those given
in the table; also tubes of special shapes, such as square, triangular,
octagonal, etc.; and bronze tubes.
They also have in stock, in lengths of 12 feet, the following sizes of
seamless brass and copper tubing, made of same outside diameter as
standard sizes of iron piping, so as to be used with the same fittings as
the iron pipe.
A = nominal inside diameter of iron pipe, in inches. For actual
inside diameters.
B = outside diameter of iron pipe and of seamless tube, in inches.
C = inside diameter of seamless tube, in inches.
D = weight per foot of bra^s pipe. cols. B and C. For copper, add
one-nineteenth.
Tin and Zinc
169
A
B
C
D
A
jB
C
£>
A
B
C
D
H
1%2
M
.28
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1. 15
2
2^
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3Ma
8.00
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1^6
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2.55
4
4!^
45^
12.24
TIN AND ZINC
The pure metal is called block tin, — When perfectly pure (which
it rarely is, being purposely adulterated, frequently to a large proportion,
with the cheaper metals lead or zinc), its specific gravity is 7.29; and its
weight per cubic foot is 455 pounds. It is sufficiently malleable to be
beaten into tin foil, only Hooo of in inch thick. Its tensile strength is
but about 4600 pounds per square inch; or about 7000 pounds when made
into wire. It melts at the moderate temperature of 442° F. Pure block
tin is not used for common building purposes; but thin plates of sheet
iron covered with it on both sides constitute the tinned plates, or, as they
are called, the tin, used for covering roofs, rain pipes and many domestic
utensils. For roofs it is laid on boards.
The sheets of tin are united as shown in this Fig. First, several
sheets are joined together in the shop, end for end, as at tt, by being first
bent over, then hammered
flat, and then soldered. ^t
These are then formed into
a roll to be carried to the
roof, a roll being long
enough to reach from the
peak to the eaves. Dif-
FiG. 51.
ferent rolls being spread up and down the roof are then united along
their sides by simply being bent as at a and s, by a tool for that purpose.
The roofers call the bending at .y a double groove, or double lock; and the
more simple ones at t, a single groove, or lock.
To hold the tin securelj^ to the sheeting boards, pieces of the tin 3 or 4
inches long, by 2 inches wide, called cleats, are nailed to the boards at
about every 18 inches along the joints of the rolls that are to be united,
and are bent over with the double groove 5. This will be understood
from y, where the middle piece is the cleat, before being bent over. The
nails should be 4-penny slating nails, which have broader heads than
common ones. As they are not exposed to the weather, they may be of
plain iron.
lyo MaU-riaLs
Miidi use is made of what is called leaded tin, or terncs, for roofing.
It i.i simply sheet iron coated with lead, instead of the more costly metal
I in. It is not Jis durable as the tinned sheets, but is somewhat cheaper.
The best plates, Iwth for tinning and for terncs, are made of charcoal
iron, which, being tough, bears bending better. Coke is used for
I hcaper plates, but inferior as regards bending. In giving orders, it is
inii>ortant to specify whether charcoal plates or coke ones are required;
also whether liniicd plates, or tcriics.
Tinned and leaded sheets of IJesscmcr and other cheap steel are now
much used. They are sold at ai>out the price of charcoal tin and teme
plates.
There are also in use for roofing, certain compound metals which resist
tarnish better than either lead, tin, or zinc but which are so fusible as to
be liable to be melted by large burning cinders falling on the roof from a
neighboring conflagration.
A roof covered with tin or other metal should, if possible, slope not
much less than five degrees, or about an inch to a foot; and at the eaves
there should be a sudden fall into the rain-gutter, to prevent rain from
backing up so as to overtop the double-groove joint s, and thus cause
leaks. When coal is used for fuel, tin roofs should receive two coats of
paint when first put up, and a coat at every 2 or 3 years after. Where
wood only is used, this is not necessary; and a tin roof, with a good pitch,
will last 20 or 30 years.
Two good workmen can put on, and paint outside, from 250 to 300
square feet of tin roof, per day of 8 hours.
Tinned iron plates are sold by the box. These boxes, unlike glass, have
not equal areas of contents. They may be designated or ordered either
by their names or sizes. Many makers, however, have their private
brands in addition; and some of these have a much higher reputation
than others.
Sizes and Weights of Lead Pipes
Sizes and Weights of Lead Pipes
171
Inner
diameter.
Thickness,
Weight per
Inner
diameter.
Thickness,
Weight per
inches
inches
foot, ounces
inches
inches
foot, pounds
H
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I
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4.7s
4
H
16.0
iM
.10
2.0
4
Me
21.0
iM
.12
2.5
4
3/i
2S.O
iH
.14
3.0
4H
Me
14.0
iH
.16
3.7s
4H
H
18.0
iH
•19
4-75
5
H
20.0
iH
.25
6.00
S
%
31.0
173
Materials
(<-A>j
8
e
<
&
-
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S)
2;r.;. .• ■ ' T
(»
to
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it
8
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o
« « « «
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1
X
o
" * * "t.^ "^~ M ^ 'm *« "ri" n "i^
«
or^ •!»» M (-X .>\ -^ .(jv n rt^ md^ w*\
MMMf«r«f«r«}^
:?:
:?
c* « •
M M M M M
>~i
« e « «
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— rt .-WN 1,-. p-s or- t«.v w- o"-^ r-^ ofs -^.
•^
i?t ^oe rt""vflo nJ2 V— ^ sf* ^ saD s^
M |»N M rt^ O^ wv (•js .^s. ^ ,iX ^yv
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ts.
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r-N CN r-."^ rts f,^ ^N MS r^ Ks .Js
fej
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i
250
500
I.OOO
2,0O0
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4.000
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8,ooo
12,000
i6,ooo
3O.0OO
1
w M <i fo ^ %n*o 00 o
Chains and Cables
173
Chains and Cables
(United States Navy Standard.)
Load in
pounds
A
B
c
D
Pounds per
foot
Ultimate
Working
Inches
Inches
Inches
Inches
Vi
}i
I?l6
25^2
.875
3.360
670
M«
iMe
iH
^%2
1. 000
5,040
1,000
H
iM
1%
^H2
1.70
7,280
1,460
Ji6
1%
2Ha
l%2
2.00
10,080
2,020
H
llM6
2%
Il^2
2.50
13,440
2,690
9i8
i^/i
2H
115^2
3.20
16,800
3,360
H
2H6
3
l2%2
4.12s
20,720
4,140
iMa
2!4
3M
l2Ji2
5.00
25,200
5,040
H
2)^
3V^
l3H2
S.87S
30,240
6,050
1^8
2IM6
3%
2%2
6.70
35,280
7,060
li
2ji
4
2%2
8.00
40,880
8.180
1^6
3M6
4?i
215^2
9.00
47,040
9.410
I
3'/4
4H
2l%2
10.70
53.760
io,7SO
iHe
3?i6
4^/i
22J^2
11.20
60,480
12,100
iH
3%
Si-i
223^2
12.50
68.320
13,660
1^6
3H
S8/i6
3?^2
13.70
76.160
15,230
iH
aH
sH
3%!
16.00
84.000
17,000
iMe
4%
6H
3i%2
16.50
91 ,840
18,400
ili
49-16
6H
3%
18.40
101,360
20,300
iji«
4%
61 Me
3^2
19.70
109,760
21.900
iH
5
7
33^2
21.70
120,960
24,200
174 Materials
Chain End Link and Narkow Siiackle
O \(U.S r^avy
^Jf Standard)
Standord Heiagonal Nut
anol Head.
Fig. 54.
A
/I.
B
C
D
£
Ins.
F
Ins.
C
Ins.
H
Ins.
Ins.
K
L
I^
M
Ins.
N
Ins.
0
Ins.
Ins.
Ins.
Ins.
Ins.
Ins.
91 8
96
i'/6
3^
24
94
94
iHs
9l8
iV4
i96
Mil
29i
T^
2H8
294
iHs
9l8
m
i96
9l8
296
27^
74
'H8
>^8
aM
496
4H
3
3H
3H
1^8
V4
1J6
Mn
3
3H
2H
1^18
y*
i^
Mb
3^i
3Mi
2' Mb
iH
191 8
Vi
7V4
7'^
Mb
34
4
7/6
I
2J6
sM
3%
iH
191 8
91 8
2H
2!^
Mb
3M
i4
^V*
s94
4V6
iV*
1>H8
9l8
2^
296
M
44
496
96
34
'M«
lH8
3918
6
496
iH
i'Mb
91 8
2V^
296
V4
44
s
96
394
I
iH
,3^4
6H
496
iH
2M8
96
3
294
M
4H
596
96
3J4
iM«i
1^8
374
674
47/6
iV4
2H8
96
3
294
y*
S
S96
96
4
iH
iM
4Vi
7J^
.s'/6
i94
2516
7/1*
3W
3M
9l8
54
6
94
44
1^.
lM8
4%
7H
.■596
i94
2918
7/1 •
3W
3H
9l8
594
64
94
aH
iW
m
4918
8V6
.s94
l7/6
27/8
7/l8
394
34
9l8
6
696
94
494
1^8
iMb
4%
8%
.s74
l7/6
2^6
w
394
3V^
91 8
6K4
694
94
4'/*
1%
iV^
5
8%
6H
2
2«H8
H
4
34
91b
64
74
7/6
sH
I^/iB
l9i8
s9l6
9
6H
2
2lM«
H
4
34
9l8
694
796
7/6
S94
IH
l54
$H
<M
6H
2H
3M8
91 8
4V^
4
96
7
794
7/6
s4
19^8
i'Hb
nH
9%
7H
2H
3H8
91 8
4W
4
96
7H
8
li
s9«
iH
i?4
5' ^8
loH
796
2^
Mt
96
.■>
44
96
74
84
64
I'Me
i'Mb
6
io9i
794
2^
37/18
96
5
44
96
794
894
64
1^4
I'/i
6K4
ii96
8
294
,3'M8
>M6
sVi
S
7/1*
8
94
696
I>M6
I«M8
6^8
11^
8M
294
.3' Mb
>Mb
■SW
$
7.1 8
84
996
64
1^4
2
6>Me
iiH
8^
294
.3' Mb
'Mb
.s!^
5
7/1*
84
996
i4
694
i»5<«
2M«
67/6
12
894
294
3' Mb
>Mb
SW
5
7/1*
894
gi'A
i4
674
No. 33, Supplement to Machinery, June, 1904.
Table for Eye Bolts
175
Table for Eye Bolts
(Contributed by H. A. H.)
/
..-^
::^
J3
T3
01
g
(i
"£
B 0
■3
•W N
•a '5
^ v^ -^. lU
0 ^
3 r»
£
M^
1 r-^ '
^S| 0
J3
0 S
§i
1 ^SJ 1
^i t
-^
•^ S-
i^p
"o
u
4)
4J 0
J3 II
o>§
5-a
Fig. ss.
J3
B
3
lU
a;
2;
A
B
c
D
E
F
G
W
C/3
.375
2
.75
.625
.1875
.375
.25
16
677
750
.5
2.125
I
.75
.25
.5
.3125
13
1.257
1. 172
.62s
2.25
1. 25
I
.3125
.625
.4375
II
2,018
2,296
■ 75
2.375
I 4375
1. 125
.3125
.6875
.5
10
3.020
3.000
.875
2.5
1.6875
1.375
.375
.75
.62s
9
4.194
4.687
I
2.75
1.875
1.5
.4875
.875
.75
8
5.509
6,7So
1. 125
2.875
2. 125
1.625
.5
I
.8125
7
6,931
7.921
1.25
3
2.375
1.75
■ 5
I.I2S
.875
7
8,899
9.188
1. 375
3.125
2.62s
1.87s
.5625
I. 1875
I
6
10,541
12,000
i-S
3-25
2.75
2
.625
1.25
1.062s
6
12,938
13.546
1.625
3.375
3
2.125
.6825
1-375
1. 125
5.5
15,149
IS.187
1-75
35
3.23
2.25
.75
1.5
1.25
5
17.441
I8.7SO
I 875
3.625
35
2.375
.8125
1.62s
I. 3125
5
20.490
20,671
2
3-75
3.75
2.5
■ 875
1.75
1.375
4-5
23,001
22,686
176
Materials
SrROf-Ki T WiiKi i.s loK Okuinary Link Chains
ff-4
Section E-F.
Pitch Chain Sheave.
a" =,33. (HOtte Pag.S02-I)
di-y.. i^y--:,
Fig. 56.
Sprocket Wheels for Ordinary Link Chains
177
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K
jg »t^ « f*' pf ■■#♦■•■ w- -rf\ w- w^, ws .rfv .x •rf^
M
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Transmission or vStanding Cables
Pliable Hoisting Rope
With 6 strands of 19 wires each.
179
Trade
num-
ber
Diam-
eter
Cir-
cum-
ference
in
inches
Weight
per foot
in lbs.
with
hemp
center
Breaking
strain in
tons of 2000
pounds
Proper
working
load in
tons of 2000
pounds
Circumfer-
ence of
Manila
rope of
equal
strength
Minimum
size of
drum or
sheave in
feet
Iron
Steel
Iron
Steel
Iron
Steel
Iron
Steel
I
2
3
4
5
6
7
8
9
10
loH
10!.^
loH
loa
10J6
2H
2
m
i^
m
m
1
H
H
9ia
H
Me
H
6?^
6.0
S-S
S.o
4-75
4.38
4.0
3.S
3.13
2. 75
2.25
2.0
1.63
1.5
1.38
1-25
8.00
6.3
5.25
4.10
3.65
3.00
2.5
2.0
1. 58
1.20
0.88
0.60
0.44
0.35
0.29
0,26
74.0
65.0
54.0
44 -o
39.0
33.0
27.0
20.0
16.0
11.5
8.64
5.13
4.27
3.48
3.00
2.50
155. 0
125.0
106.0
86.0
77.0
63.0
52.0
42.0
33.0
25. 0
18.0
12,0
9.0
7.0
5.5
4-5
15.0
13.0
no
9.0
8.0
6.5
55
4.0
3.0
2.5
1.75
1.25
0.7s
0.5
0.38
0.25
31.0
25.0
21.0
17.0
15.0
12.0
10. 0
8.0
6.0
5.0
35
2.5
1.5
1.0
0.7S
0.5
14.0
13.0
12.0
II. 0
10. 0
9-5
8.5
7-5
6.5
5. 5
4.75
3.7s
3.5
3.0
2.7
2.5
15.0
14.0
13.0
12.0
II. 0
9.5
8.S
7.0
5.7s
5.0
4.5
3-75
3.5
13.0
12.0
10.0
8.5
7.5
7.0
6.5
6.0
5 25
4.5
4.0
35
2.75
2.25
2.0
IS
8.S
8.0
7 25
6.25
5.75
55
5.0
45
4.0
3.5
3.0
2.2s
1. 75
IS
I 25
1.0
Transmission or Standing Cables
With 6 strands of 7 wires each.
II
1.5
4.63
3.37
36.0
62.0
9-0
13.0
10. 0
13.0
13.0
8.5
12
1.38
4.25
2.77
30.0
52.0
7.5
10. 0
9.0
12.0
12.0
8.0
13
1. 25
3.75
2.28
25.0
44.0
6.25
9.0
8.5
II. 0
10. 75
7.2s
14
T.I3
3.37
1.82
20.0
36.0
5.0
7-5
7.5
10. 0
95
6.25
IS
I.O
3.0
1.5
16.0
30.0
4.0
6.0
6.5
9.0
8.5
5-75
16
0.88
2.62
1. 12
12.3
22.0
3.0
4-5
5. 75
8.0
7.S
SO
17
0.75
2.38
0.88
8.8
17.0
2.25
3.5
4.75
7.0
6.75
4.S
18
0.69
2.13
0.70
7.6
14.0
2.0
3.0
4-S
6.0
6.0
4.0
19
0.63
1.88
0-57
5.8
II. 0
1.5
2.25
4.0
5.5
5. 25
35
20
0.55
1.63
0.41
41
8.0
I.O
1.75
3.25
4.7s
4.5
3.0
ai
o.S
1.38
0.31
2.83
6.0
0.75
1.5
2.75
4.0
4.0
2.5
23
0.44
1. 25
0.23
2.13
4.5
0.50
1. 25
2.5
35
3.2s
3.35
23
0.38
1. 13
0.9
1. 65
4.0
I.O
2.25
3-25
2.75
3.0
24
0.31
1.0
0 16
1.38
3.0
0.75
2.0
2.75
2.5
1.75
25
0.28
0.88
0.13
1.03
2.0
0.5
1. 75
3.35
2.25
1.5
I So
Materials
locofion /&/■ Mor/murn Aiomtnf.
« <■ If
■Dc-
9 i'i
••vf.
+ft^
■i"
■i-
\ CS eknofts ctnltr of span,
[ CH dtnofts ctnftrof^arifi/of looKtt.
I Iff, dtnofti fifariet f Joa€i txfjactnf to CO.
ft lY- tofal load and f1 - momtnf.
For rf a /vatifnt/rn p/art cs m/drrat/
bffirft" IT/, and CO and /r'nd M untttr
HTf,. ror reactions, Pfl^ and ftr'
tV' Rj. For maximum moment ff'/fj
l>h-(»'il,* '^U), or s!n<e Oc-Ot,, ft-
Jivo yVheels Eqt/a//c/ Loadecf.
Oiaqram of i ^
mofntnfs for\ j;
three pos/fion^
Ot/oaa.
Diagram of
shear tot/)
tr/ree/9 on span}
Oogram of
maximum
momen ts
of antj point I
of ttte beam, i
Diaaram of ','" thete tm> diagrams dotted
maximum \~~asff sfo-r confiruatioa,^
Shear otant/
point of beam.\
For B- or exceeds O.SBSSL, /^' ^■
and /fr' Z ^Orfj)-
.notation: >lll yo/ues ini/xtus ondpovnas.
IV- fata/ food. >^ - /oadon one xrf>»t/.
I • /engfffi of Sflon. B • tr/ni/ ^se.
K Rj • left reaction. />r ' rignf reactior).
If- irrfica/jfiear -reaction rteartsf fo
file pair} f under cortsiderafior}.
Df'disfance to front xrfreet i ^^
Or • distance fo rear rrfiet/ ' . "^
coming on from tfit /eft ftff -nioment
under front whei/, one rrtreel on ffit span,
lifl' moment under frcnf irfieef xriffi boffi
tvneels on the sparj. ft^/ " moment undkr rwar
trheel, one t*fieel on the span, firt - momen f
under rear nfieef, boffi fhee/s on the span.
JC " ralue of Or for Mrt " maximum.
M- maximum momerrf, Z- section modu/t)S.
Si, • stress due fo bertdirxf.
Mf,-^'a-Of). >iri-'^[a-Dr). fff!- fri^§ia-^¥).
MiTX'^(i.-Dr-§) For ralues of S /ess fhan
O.SeS8L. x-^.^a„dM.Vj^(,-A)^.
Z.gors,.^. ^
For both rrhee/s on the span, ^ - £■ U'£tr-j)
Jrm Hfhee/s E(^uallt/ Loac^d, Ob/r^ue ffeacf/'orr.
i !
flotation: Same asabore trith addition of; a 'ong/t of ff>e rrocfion
nith team, /i- cross sec fionat area of beam. 7' thrust or
! ""j^ mfh Deam. />• cross secr/onaf area or oeam. r-rnrvsr
, Y~A — ^l^^-^V'^yf P"" "''* '" obUque reaction. S- direct s/ress At fo T
^ M; -_;■'/- ■^'^■^l (tension or compression).
n
=tt^
l-f,(Dr * |;, or 7' = (Or * f ; cot a
S-Jl-fi^(Orf§), or S-z^(Orr§)cota.
fiff, ffr,, 3C, M and So - soma as abort.
SfS^.wi^;^ ^ ^(^-PliiSI), or
, , W ,(Drf''iB)cot ex . Dr(L-Dr-''iB/.
StS^'lf -j^ -e 2L ''
SfSi,-amaximi/mHher7/:^-£^r^-Jl-^cofat^-£.
~For light xreighf T- beams j • about j depth efbeorn.
Figs. 57, 58, 59.
Modulus of Elasticity i8i
Modulus of Elasticity
The modulus of elasticity of any body is the ratio, within the elastic
limit, of the stress per unit of area to the stretch per unit of length.
. Let S = stress per square inch, and
L = elongation per unit of length.
S' = total stress.
L' = total elongation.
O = original length.
A = area of cross section in square inches.
E = modulus of elasticity.
Then E = j, which is found to be practically constant, and is a
measure of the resistance which a body can oppose to change of shape.
S'
-J = 5 = stress per square inch, (i)
jr = L = elongation per unit of length
A S S'O ^ , ,
Hence the modulus of elasticity is equal to the total stress, multipHed
by the original length, divided by the area in square inches, multiplied
by the total elongation.
From equation (2),
and since
5' = ^, (3)
^ = S and ^ = L, then 5 = EL; (4)
A 0
or the stress per vmit of area is equal to the modulus multiplied by the
elongation per unit of length. *
From (3),
^ EA E ^^^
5
and ^ ^ E' ^^^
or the elongation per unit of length equals the stress per unit of area
divided by the modidus.
1 82
Materials
Table of Moduli of Elasticity and of Elastic Limits for
Different Materials
The values here given are approximate averages compiled from many sources.
Authorities differ considerably in their data on this subject.
Material
Modulus or
coefficiency
of elasticity
Stretch or compression
in a length of lo feet,
under a load of
1000 lbs. per
sq. in.
I ton per
sq. in.
Ash
Beech
Birch
Brass, cast
Brass wire
Chestnut
Copper, cast
Copper wire
Elm
Glass
Iron, cast
Iron, cast, average
Iron, wrought, in either bars
sheets or plates
Iron bars, sheets, average
Iron wire, hard
Iron wire ropes
Larch
Lead, sheet
Lead wire
Mahogany
Oak
Oak, average
Pine, white or yellow
Slate
Spruce
Steel bars
Steel bars, average
Sycamore
Teak
Tin, cast
Lbs. per
sq. in.
1,600,000
1,300,000
1,400,000
9,200,000
14,200,000
1,000,000
18,000.000
18,000,000
1,000,000
8,000,000
12,000,000
to
23,000,000
17,500,000
18,000,000
to
40,000,000
29,000,000
26,000,000
15,000,000
1,100,000
720,000
1,000,000
1,400,000
1,000,000
to
2,000,000
1,500,000
1,600,000
14,500,000
1,600,000
29,000,000
to
42,000,000
35,500,000
1,000,000
2,000,000
4,600,000
Ins.
.07s
.092
.086
.013
.009
.120
.007
.007
.120
.015
.010
to
.005-
.007
.006
to
.003
.004
.005
.008
.109
.167
.120
.085
.120
to
.060
.080
.075
.008
■07s
.004
to
.003
.003
.120
.060
.026
Ins.
.168
.207
.192
.029
.019
.269
.015
.015
.269
.034
.022
to
.012
■ 015
.015
to
.007
.009
.010
.018
.244
.192
.269
to
.154
.179
.168
.018
.168
.009
to
.006
.007
.269
.134
Table of Deflections
183
Table of Deflections
The formulae are based on the assumplion that the increase of deflec-
tion is proportional to the increase of load.
The values of the letters in the table are as follows:
d = deflection of beam in inches.
W = weight of extraneous load in pounds.
w = weight of clear span of beam in pounds.
I = clear span of beam in inches.
E = modulus of elasticity in pounds per square inch.
/ = moment of inertia of cross section of beam in inches.
Moduli of Elasticity of Various Materials
Materials
Brass, cast . . .
Brass wire
Copper
Lead
Tin, cast
Iron , cast ....
Iron, wrought
Steel
Marble ,
Slate
Glass
Ash
Beech
Oak
Pine, longleaf.
Walnut
Moduli
9,170,000
14,230,000
15,000,000 to 18,000,000
1,000,000
4,600.000
12,000.000 to 27,000,000 (?)
22,000,000 to 29,000,000
26,000,000 to 32,000,000
25,000,000
14,500,000
8,000,000
1,600,000
1,300,000
974.000 to 2,283,000
1,119,000 to 3,117,000, 1,926,000
306,000
1 84
Materials
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Modulus of Rupture
185
From the table, it is found that for beams of similar cross section and
of same material, and within the elastic limit, the load and deflections
(neglecting the weight of the beam itself) are as follows:
Deflections Under Given Extraneous Loads
With same span .
With same span and breadth . . .
With same span and depth
With same breadth and depth. .
Inversely as the breadths and as the cubes of
the depths
Inversely as the cubes of the depths
Inversely as the breadths
Directly as the cube of the span
Extraneous Loads for a Given Deflection
With the same span .
With the same span and breadth .
With the same span and depth
With the same breadth and depth.
Directly as the breadths and as the cubes of
the depths
Directly as the cubes of the depths
Directly as the breadth
Inversely as the cubes of the spans
Modulus of Rupture
The modulus of rupture is the total resistance, in pounds per square
inch, of the fibres of a beam farthest from the neutral axis; and is 18
times the center breaking load in pounds, of a beam of the given material,
I inch square by i foot span. The values of the modulus of rupture,
which is usually denoted by "C," may be obtained from the following
table of transverse strengths, by multiplying the values therein by 18.
One-third part of any of these constants (except those for
wrought iron and steel) may be taken in ordinary practice as about the
average constant for the greatest center load within the elastic limit. The
loads here given for wrought iron and steel are already the greatest
within elastic limits.
Transverse strengths, in pounds
&SS
6^
^3
WOODS
Ash:
English
Amer. White (Traut.)...
Swamp
Black
Arbor VtUe, Amer
Balsam, Canada
Beech, Amer
Birch:
Amer. Black
Amer. Yellow
Cedar:
Bermuda
Guadaloupe
Amer. White or Arbor
Vitae
Chestnut
Elm:
Amer. White
Rock, Canada
Hemlock
650
650
400
600
250
350
850
S50
850
400
600
250
4SO
650
800
Soo
Hickory:
Amer
Amer. Bitter nut
Iron Wood, Canada
Locust
Lignum Vita
Larch
Mahogany
Mangrove:
White
Black
Maple:
Black
Soft
Oak:
English
Amer. White (by Traut. ) . . .
Amer. Red, Black, Basket.
Live
Pine:
Amer. White (by Traut.). . .
Amer. Yellow* (by Traut.).
800
800
600
700
650
400
7SO
650
SSO
750
7SO
SSO
600
850
600
450
soo
i86
Malrri.ils
Transverse slrengths, in ptjunds — {Continued)
Pine:
Amer. Pitch* (by Traut.)
Clcornia*
I'oplar
I'oon
.Spruce:
(By Traut.)
Black
Sycamore
Tamarack
leak
Walnul
Willow
Metals
Brass
Iron, cast:
1500 to 2700. average
Common pig
Castings from pig
Employed in our tables
For castings 2'/^ or 3 ins. thick. .
Iron, wrought, 1900 to 2600, average
Wrought iron does not break;
but at about the average of 2250
pounds its elastic limit is reached.
Steel, hammered or rolled; elas-
ticity destroyed by 3000 to 7000.
Under heavy loads hard steel
snaps like cast iron, and soft steel
bends like wrought iron.
Stones, etc.
Blue stone flagging, Hudson River.
Brick:
Common, 10 to 30, average
Good Amer. pressed, 30 to so,
average
Caen Stone
Cement, Hydraulic:
English Portland, artificial,
7 days in water
1 year in water
Portland, Kingston, N. Y., 7
days in water
SSO
8so
5SO
700
4SO
SSO
Soo
400
750
S.SO
350
8so
2100
2000
2300
2025
1800?
2250
Cement Hydraulic:
Saylor's Portland, 7 days in
water
Common U. S. ccmcnti, 7
days in water
The following hydraulic ce-
ments were made into prisms, in
vertical mould.s, under a pressure
of 32 pounds per .square inch, and
were kept in sea water for I year.
Portland Cement, English, pure,
I year old
Roman Cement, Scotch, pure
American Cements, pure, average
about
Granite:
so to ISO, average
Quincy
Glass, Millville, New Jersey,
thick flooring (by Traut.)
Mortar:
Of lime alone, 60 days old
I measure of slacked lime in
powder, i sand
I measure of slacked lime in
powder, 2 sand
\farble:
Italian, White
Manchester, Vt., White
East Dorset, Vt.. White
Lee. Mass., W'hite
Montgomery Co., Pa., Gray. . . .
Montgomery Co., Pa., Clouded.
Rutland, Vt., Gray
Glenn's Falls, N. Y., Black. . . .
Baltimore, Md., White coarse . .
Oolites, 20 to so
Sandstones:
20 to 70, average
Red of Connecticut and New
Jersey
Slate, laid on its bed, 200 to 450,
average
100
100
116
95
III
86
103
14a
70
I5S
103
35
45
45
• Trautwine.
Moment of Inertia 187
Moment of Inertia
The moment of inertia of the weight of a body, with respect to any
axis, is the algebraic sum of the products obtained by multiplying the
weight of each elementary particle by the square of its distance from
the axis.
If the moment of inertia with respect to any axis be denoted by /; the
weight of any elementary particle by w; and its distance from the axis
by r; the sum of all the particles by S, then / = X{wr^).
The moment of inertia of a rod or bar of uniform thickness, with
respect to an axis perpendicular to the length of the rod, is
W
(?-)
in which W equals the weight of rod, 2 / equals length and d equals the
distance of the center of gravity of the section from the axis.
For thin circular plates with the axis in its own plane, when r equals
the radius of the plate,
For circular plate, axis perpendicular to the plate,
/ = wl-+d^
Circular ring, axis perpendicular to its own plane,
'r^ + r"
= w{^-
+ d^
r and r' being the exterior and interior radii of the ring.
Cylinder, axis perpendicular to the axis of the cylinder,
r = radius of base and 2 / = length of the cylinder.
By making d equal to o in any of the above formulae, the moment of
inertia for a parallel axis passing through the center of gravity is found.
The term moment of inertia is also used in respect to areas, as the
cross section of beams under strain.
In this case, / = 2(ar)^, in which a is the elementary area and r its
distance from the center.
i88
Materials
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Formula; for Transverse Strength of Beams 189
Formulae for Transverse Strength of Beams
P = load at middle.
W = total load distributed uniformly.
I = length, b = breadth, d = depth in inches.
E = modulus of elasticity.
R = stress per square inch of extreme fibre.
/ = moment of inertia.
C = distance between neutral axis and extreme fibre.
For breaking load of circular section replace bd- by 0.59 d^.
For good wrought iron the value of R is about 80,000; for steel about
120,000. For cast iron the value of R varies greatly. Thurston found
45,740 for No. 2 and 67,980 for No. i.
IQO
Miilcrials
General Formulie for TranBverae Strength, Etc.
The following table gives the values (jf H', etc., without introducing
the modulus of elasticity or the moment of inertia.
Formulae for Round anu Rectangular Solid Beams
t^2
1^^
c.s;
•^I§
F
•b^
J^R.
ON
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li
■I
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558
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^■>
CHAPTER V
ACCELERATION OF FALLING BODIES
The change in velocity of a falling body which occurs in a unit of time
is its acceleration.
That due to gravity is 32.16 feet per second, in one second and is
denoted by g.
Let t = number of seconds during which a body falls.
V = velocity acquired in feet per second at the expiration of
/ seconds.
u = space fallen through in each second.
h = total space fallen through in t seconds.
2k
Then
32.16, t = V2 gh = 8.02V/J =
« = - = 2- = 16.08, P = = ;: ,
2 2 2 g 64.32
t =-= =y-^ = ^r = 0.24938 Vh.
g 32.16 T 8 V
The table below gives the values of ft, v and », for values of / up to ten
seconds.
Space fallen
Velocity
Space fallen
Time in
through in
acquired in
through in
seconds.
feet in
feet per
feet in
I
time t.
second at end
each second,
h
of time /,
V
u
I
16
32
16
2
64
64
48
3
I4S
96
80
4
257
129
113
5
402
161
145
6
S8o
193
177
7
789
22s
209
8
1030
257
241
9
1303
290
273
10
1609
322
306
191
102
Mechanics
The Rraphicil method of ascertaining the values of /, r, 14 an<I A is
easily rememhcrtd and is often of service.
In the lrianj;Ie, Fig. 61, let the vertical divisions on
the left of the per|)en(li(:ular repreM;nt the numl>er of
seconds through which the body falls = /.
Lei the base of each small triangle equal the velocity
at the end of the first second = 32.16. Then the
number of bases on each of the horizontal lines at
I, 2, 3, etc., multiplied by 32.16 will equal the ac-
quired velocity for the corresponding time = v.
Let the area of each small triangle = 16.08. Then
the number of such areas between o and any hori-
zontal line multiplied by 16.08 will equal the height in feet fallen through
in the number of seconds corresponding to that line = //.
And the number of small triangles between each pair of horizontal
lines, multiplied by 16.08 will equal the number of feet fallen through io
each second = 11.
t = 1, 2, 3, 4, 5, 6.
V = 32.16 X I, 2, 3, 4, 5, 6.
h = 16.08 X I, 4, 9, 16, 25, 36.
« = 16.08 X I, 3, 5, 7, 9, II.
Fig. 61.
Thus:
Fig. 62.
Parallelogram of Forces
If two forces are applied to the same point, their resultant will be
represented in intensity and direction by the diagonal of a [jarallelo-
gram of which the adjacent sides represent the
intensities and directions of the given forces.
Let AB and AC represent, in intensity and
direction, any two forces applied to the point
A; then AD will correspondingly represent
their resultant.
Conversely, if AD be the known force acting at i4, it may be resolved
into two components, in any direction in the same plane; which com-
ponents will be the adjacent sides of a parallelogram having AD for its
diagonal.
Parallelopipedon of Forces
If three forces, not in the same jjlane, act on the same p>oint, they may
be represented by the edges of a parallelopipedon and the diagonal
through the point of application is their resultant.
Height Corresponding to a Given Acquired Velocity 193
Height Corresponding to a Given Acquired Velocity
Velocity,
Height,
Velocity,
Height,
Velocity,
Height,
V
h
V
h
V
h
Feet per
second
Feet
Feet per
second
Feet
Feet per
second
Feet
■25
.0010
34
17.9
76
89.8
• SO
.0039
35
19.0
77
92.2
.75
.0087
36
20.1
78
94.6
1. 00
.016
37
21.3
79
97.0
1.25
.024
38
22.4
80
99.5
I. so
-03S
39
23.6
81
102.0
I-7S
.048
40
24.9
82
104.5
2.0
.062
41
26.1
83
107. 1
2.5
.097
42
27.4
84
109.7
30
.140
43
28.7
85
112.3
35
.190
44
30.1
86
1150
4.0
.248
45
31.4
87
H77
4.S
.314
46
32.9
88
120.4
S-O
.388
47
34.3
89
123.2
6.0
■ 559
48
35.8
90
125 9
7.0
.761
49
37.3
91
128.7
8.0
•994
so
38.9
92
131 .6
9.0
1.26
51
40.4
93
134.5
10. 0
1^55
52
42.0
94
137.4
II. 0
1.88
53
43.7
95
140.3
12.0
2.24
54
45.3
96
143 3
130
2.62
55
47 ■©
97
146.0
14.0
3.04
56
48.8
98
149.0
iS-o
3.49
57
50.5
99
152.0
16.0
3.98
58
52.3
100
155 0
17.0
4.49
59
54.1
105
171. 0
18.0
5.03
60
56.0
no
188.0
19.0
5.61
61
579
"5
205.0
20.0
6.22
62
59 8
120
224.0
21.0
6.85
63
61.7
130
263.0
22.0
7.52
64
63.7
140
3040
23.0
8.21
65
65.7
ISO
350.0
24.0
8.94
66
67.7
175
476.0
25. 0
9.71
67
69.8
200
622.0
26.0
10. 5
68
71-9
300
1.399 0
27.0
11.3
69
74.0
400
2,488.0
28.0
12.2
70
76.2
500
3.887.0
29.0
13. 1
71
78.4
600
5.597 -o
30.0
14.0
72
80.6
700
7,618.0
31 0
14.9
73
82.9
800
9.952. 0
32.0
159
74
85^i
900
12.593. 0
330
16.9
75
87.5
1000
IS. 547.0
194 Mechanics
The Lever
f^
The lever is a solid bar of any form, siipixjrled at a fixwi point, alx)Ut
which it may turn freely.
I ^ -] The fixed point is the fulcrum. There arc
|f| r pi three orders of levers. In those of the first
order the j)oints of applicaticm of the |X)\ver
and resistance are on opposite sides of the
fulcrum.
In the second order the resistance is ap-
plied between the fulcrum and the power.
In the third order the power is applied
l)ctwcen the fulcrum and the resistance.
« In any order ^'''- ^4-
j-^ "^ _—_ , ^^^ weight IF multiplied by the distance
'^ >L WF from the fulcrum must equal the
^Ll power P multiplied by PF, to establish
Fig. 65. .1., •
■^ equilibrium.
Whatever may be the shape of the lever, the power or resistance acts
at the end of a line drawn through the fulcrum and perpendicular to the
line of direction of the power or resistance. This perpendicular is called
the lever arm of its corresponding force, and the product of the lever arm
and its force is called the moment of that force. When the moments are
equal the forces are in equilibrium.
If one moment exceeds the other, rotation will occur about the ful-
crum in the direction of the force having the greater moment.
The Wheel and Axle
This is simply such an application of the lever of the first order, that
the power and resistance may act through greater distances; the radius
of the wheel is the lever arm of the power and that of the drum the lever
arm of the resistance.
When the resistance is a weight, it will be raised if the moment of the
power is the greater and vice versa.
The Inclined Plane
If a force P acts in the direction of
AB, to overcome the resistance R, then
P :R::a -.b.
• • " = -r- and K = — .^.^ ,,
b a Fig- 60.
Center of Gravity 195
The Wedge
The wedge is simply a double inclined plane, placed !„
back to back. k-- a --m
If the force applied to a wedge be represented by P ■ \ 1 /
and the resistance to be overcome by R, the base of the \ 1 /
wedge by a and its length by 6; then b \ ; /
P : R : : a : b P = -7- and R = — •. V/
Center of Gravity
The center of gravity of a body is that point through which the effort
of its weight always passes. If a body be suspended from any point,
the direction of the line of suspension will pass tlirough its center of
gravity.
Therefore, the center of gravity of any body may be determined by
finding the intersection of the hnes of suspension passing through points
not on the same vertical hne.
The center of gravity of two bodies is on a line joining their respective
centers of gravity and the distances from the center of gravity of either
body to that of both of them (combined) are inversely proportional to
the weights of the bodies respectively.
To find the center of gravity of any irregular plane surface, divide it
into triangles of any convenient areas. Find the center of gravity and
the area of each triangle. Then assuming any coordinate axes X and
Y, multiply the area of each triangle by the abscissa of its center of gravity
and divide the product by the sum of the areas of all the triangles. The
quotient is the abscissa of the center of gravity of the entire figure. Find
its ordinate in the same way; then the point determined by this abscissa
and ordinate is the center of gravity of the figure.
This method is precisely that shown by Fig. 61, Machinery Supplement
No. 5.
In addition to the formulae taken from Machinery Supplement No. 5,
others are given as follows:
Semiellipse
The center of gravity of a semiellipse is on the semiaxis perpendicular
to the base and at a distance from the base equal to the product of that
semiaxis and the decimal 0.4244.
iq6 Mrclianics
The Center of Gravity of Solids of Uniform Density
Throughout
Sphere and spheroid at center of the l)ody.
Hemisi)hcrc on the radius perpendicular to the base and at W its
ienplh from the base.
Spherical Sector. — On the radius passing through the center of the
circle cut from llic sjihere by the sector and at a distance from the center
of the sphere, eciual to three-f(jurths of the diiTerence between the radius,
and one-half the rise of the sector. Or G. representing the distance from
center of sphere to center of gravity, R = radius of sphere and // the
rise of the sector; then G = ^ilR )•
Spherical Segment
,, (.2 K - II)-
^-^' zR-n
Spherical Zone
Take the difference between ihc two segments whose difference is
the zone. Find the center of gravity of each segment; then, by inverse
proportion, find that of their difference.
Frustrum of a Cone
Let G = distance from base to center of gravity measured on
the axis.
A = area of large end.
a = area of small end.
H = height of frustrum measured on the axis.
Aa + 3a\
Aa + a J
Then c^nfA + ^^^+sa
4 V ^ + VAa + ,
The center of grav-ity of a paraboloid is on the axis and at a distance
from the vertex ecjual to two-thirds that from vertex to base.
A body suspended from center of gravit)^ has no tendency to rotate.
Center of gravity of regular figures is at geometrical center; of a triangle
two-thirds distance from any angle to middle of opposite side; of semicircle
2 CT
on middle radius, 4244 r from center; of sector — j- from center; of seg-
3*
c3
ment, from center (where c = chord and a = area); of cone or
12 a
pyramid, V* distance from center of base to apex a, a^, at = areas of
respective triangles.
Center of gra\ity of two bodies, x = — r— r^
W + W
Radius of Gyration
197
General formulae x =
y =
aiXi + OiOCi + 03^:3
^1 + 02 + fls
Oiyi + (Jiji + flays
fli + (h + fls
.— /-..
0-
\L1
<X,-f
-s^r::::^,
\
v-^n
:)\
OX,-
\ ,^^ ■
-<'
:i^
^ i^-
^
(7
Y
Fig. 68.
Fig. 69.
Volume of a solid generated by the revolution of a surface about an axis
in the same plane with it = area of the surface X circumference de-
scribed by its center of gravity.
Moment of Inertia
Moment of inertia of rotating body = products of weights of particles
X squares of distances from the axis = / = Wiri^ + Wir:^ + w^^, etc.
K'l, W2, etc. = weights of particles; n, h, etc. = distances from axis in
same units as the volumes of the particles of which weights are taken.
Radius of Gyration
Center of gyration of rotating body is point at which weight may be
assumed concentrated. Radius of gyration = k = distance from center
f
For circvdar disc, k = — ;=. For
V2
of rotation to center of gyration
circular ring, k
1899.)
IB} + r^
(No. s Supplement to Machinery, Sept.,
Specific Gravity of Gases
Air = I.
Hydrogen 0.069
Marsh gas o ■ SS9
Steam o. 623
Carbonic oxide o. 968
Nitrogen 0.971
Olefiant gas o. 978
Oxygen i . 106
Sulphuretted hydrogen i . 191
Nitrous oxide i • 527
Carbonic acid i • 529
Sulphuric acid 2 . 247
Chlorine 2 . 470
iqS
Mechanics
Specific C.RvWITy of Various Substances
Wat.T - I.
Substancui
Average
s[)ecific
Kravity
Air at 60' F. under pressure of one atmosphere weighs
Hi ft part as much as water at 60* F
Alcohol
Ash, American, white, dry
Aluminum
Antimony
Asphaltum
Basalt
Bismuth
Brass:
Copper and zinc, cast
Copper and zinc, rolled. . .
Bronze, copper 8, tin I
Brick, pressed
Brick, common, hard
Brick, soft
Box wood
Carbonic acid
Charcoal, of pines and oaks.
Chalk
Clay, dry. in lump, loose
Coke:
Loose
A heaped bushel 35 to 42 pounds. A ton occupies
from 40 to 43 cubic feet.
Cherry, dry
Coal:
Anthracite
Anthracite, broken, loose
Bituminous ,
Bituminous, broken, loose
• A heaped bushel weighs from 70 to 78 pounds.
A ton occupies from 43 to 48 cubic feet.
Cement:
Rosendale. ground, loose
Rosendale, struck bushel ,
English Portland
French Portland
Copper, cast
Copper, rolled
Diamond
Earth:
Dry loam, loose »
Dry loam, shaken
Dry loam , moderately rammed
Loam, moist, loose
Loam, moist, shaken
Soft mud
Elm, dry
Ebony
o 00123
0.834
0.61
2.6
6 70
14
29
9 74
8.1
8.4
8.5
o 96
0.00187
0.672
IS
I 35
8.7
8.9
3-53
0.56
Specific Gravity of Various Substances 199
SPEcrFic Gravity of Various Substances — {Continued)
Substances
Fat
Flint
Feldspar
Glass
Glass, common window
Granite
Gneiss, common
Gypsum, plaster Paris
Greenstone, trap
Gravel
Gold, pure
Gutta percha
Hornblende, black
Hydrogen is 14!-^ times lighter than air and 16 times
lighter than oxygen
Hemlock, dry
Hickory, dry '.
Iron, cast
Iron, pure
Iron, wrought, rolled
Iron, sheets
Ivory
Ice
India rubber
Lignum Vitae, dry
Lard
Lead
Limestones and marbles
Lime, quick
Lime, quick, ground loose, per struck bushel.
Mahogany:
Dry, San Domingo
Dry, Honduras
Maple, dry
Marbles, see Limestone
Masonry:
Granite or limestone
Granite or limestone rubble
Brick, ordinary quality
Mercury at 32° F
Mercury at 212° F
Mica
Mortar, hardened . . .
Mud:
Dry
Moist
Wet. fluid
Naphtha
Nitrogen
Oak live, dry
Oak white
Oak, red and black.
Average
specific
gravity
• 93
2.6
2.6s
2.98
2.52
2.72
2.69
2.27
3.0
19 258
■ 4
.85
7.218
7-77
7.69
7-73
1.82
.92
■93
1-33
• 95
11.38
2.7
IS
13- 62
13.38
2.93
1.63
.001194
•9S
.77
Average
weight per
cubic foot
in pounds
S8.o
162.0
166.0
186.0
157 -o
170.0
168.0
141. 6
187.0
90 to 106
1204.0
61. 1
203.0
.00527
25.0
53 -o
450.0
485.0
480.0
485.0
114 .0
57.4
58.0
83.0
59-3
709.6
168.0
95.0
S3.0
53.0
35.0
49 o
165.0
154.0
125.0
849.0
836.0
183.0
103.0
80 to no
no to 130
104 to 120
52.9
.0744
59 3
48.0
32 to 45
200
Mechanics
SpEcmc Gravity of Various Substances — (Continual)
Substances
Average
specific
gravity
Avcraiic
wdKht per
cubic foot
in pounds
Oil:
Whale
Olive
Linseed
Palm
Petroleum
Turpentine
Rape seed
Sunflower
Oolites
Ores:
Copper, vitreous
Copper, pyrites
Copper, Cornish
Iron, chromate
Iron, pyrites
Iron, magnetic
Iron, red hematite :
Iron, brown hematite
Iron, specular
Iron, spathic
Iron, ironstone
Lead, carbonate
Lead, galena
Tin, Cornish
Zinc, calamine
Oxygen
Peat, dry
Pine, white, dry
Pine, yellow, northern
Pine, yellow . southern
Pitch
Plaster Paris
Powder, blasting
Porphyry
Platinum
Quartz, pure
Ruby and sapphire
Rosin
Salt:
Coarse, Syracuse struck bushel, s6 pounds. . . .
Coarse, Turk's Island struck bushel, 76 to 80.
Coarse, Liverpool struck bushel, so to ss
Sand, dry and loose, average 98
Sand, wet
Sand stones
Serpentines
Snow:
Freshly fallen
Wet and compacted
Sycamore, dry
Shales, red or black
Slate
.92
.92
■ 94
.969
.860
.87
.914
.926
129
344
4S2
OS7
789
9
00
029
218
81
863
20
22
45
525
00136
.40
■ 55
.72
■ 15
.176
.0
73
■ 5
■ 65
9
57 3
57 3
.0846
20 to 30
25. o
34 3
45 -o
717
62.3
170.0
1342 o
165.0
68.6
45.0
62.0
42.0
goto 106
118 to 129
151 o
162.0
5 to 12
15 to 50
37.0
162.0
175 o
Specific Gravity of Various Substances 201
Specific Gravity of Various Substances — {Continued)
Substances
Average
specific
gravity
Silver
Soapstone (steatite)
Steel
Sulphur
Spruce, dry
Spelter, zinc
Tallow
Tar
Trap
Topaz
Tin
Water:
Distilled at 32° F., barometer 30"
Distilled at 62° F., barometer 30"
Distilled at 212° F., barometer 30"
At 60° F. a cubic inch of water weighs .03607 pounds
or .57712 ounces, avoirdupois
Sea
Dead Sea
Wax, bees
Wines
Walnut, black, dry
Zinc
Zircon
Asbestos
Acid:
Acetic
Carbolic
Hydrochloric
Nitric
Sulphuric
Barytes
Brick:
Common
Fire
Clay, fire
Carbon, graphite
Manganese
Magnesium
Nickel
Potassium
Phosphorus
Silicon
Stone (building)
Titanium
Tungsten : . .
Uranium
Vanadium
10.5
2.73
7.8s
2.0
.4
7.0
• 94
l.o
3.0
3.5s
7-35
1.028
1.240
•97
.998
.61
7.0
4.45
Average
weight per
cubic foot
in pounds
655.0
170.0
490.0
125.0
25.0
437.5
58.6
62.4
187.0
459 -o
62.417
62.355
597
64.08
60.5
62.3
38.0
437. 5
• 993
I 063
i^o65
1.270
1.554
1.970
4.86
1.90
2.2
2.16
2.S85
8.01
2.04
8.80
.865
1.863
2.493
2.9
5.3
19.26
18.4
5.5
499 •o
548.7
202
Mechanics
Mil. OF Physical Constants
Name
Aluminum. . .
Antimony —
Arsenic
Bismuth
Calcium
Carbon
Chlorine
Chromium. . .
Copper
Gold
Hydrogen —
Iodine
Iron
Lead
Magnesium...
Manganese . . .
Mercury
Molybdenum.
Nickel
Nitrogen
Oxygen
Phosphorus. .
Platinum
Potassium
Silicon
Silver
Sodium
Sulphur
Tellurium
Titanium. . . .
Tin
Tungsten ....
Uranium
Vanadium. . .
Zinc
Sym-
bol
Al
Sb
As
Bi
Ca
C
CI
Cr
Cu
Au
H
I
Fe
Pb
Mg
Mn
Hg
Mo
Ni
N
O
P
Pt
K
Si
Ag
Na
S
Te
Ti
Sn
W
U
V
Zn
Atomic
weight
27.3
123. 0
74 9
207 S
39 9
11.97
35.36
52.4
63.3
196.2
i.o
126.53
55. 9
206.4
23-94
54-8
199.8
95.8
S8.6
14.01
15.96
30.94
196.7
39 04
28.0
107.66
23 o
31.98
128.0
48.0
117 8
184.0
180.0
51.2
64.9
Specific
heat,
water
214
0508
0814
0308
170
214
0952
0324
2963
0541
"4*
0314
25
122
0317
0722
109
244
21S
190
0324
166
2029
0570
293
202
0474
0562
0334
Specific
gravity,
water
6.7
5. 95
9 74
1 578
2 35
2.43
6.8
8.90
19 258
4.94
7.80
11.38
1.70
8.0
13.62
8.64
8.90
1.83
21.53
.865
2.49
10.50
.972
2.00
6.65
5.3
7.35
17.50
18.40
5 54
7.00
Specific
gravity,
air
- I
Melting
point
.069
.971
.106
(5.50)
1182* P.
1973"- 1 1 34* P.
774* P.
497'-484" P.
>Pt.
1994' P.
20IS° P.
225* P.
I9oo'-279o'' P.
6i7°-588'' P.
1139° P-
2240° P.
39° P-
26io» P.
lis" F.
3150° P.
144 5°- I 36° P.
2574° P.
1732° P.
207 7°-i9o° P.
226" P.
700° P.
4000° P.
442°-4I7* F.
>Mn
4300° P.
773"-754'' P.
Latent
heat of
fusion
28s
40.0
33. as
43 o
16.0
88 69
II. o
509
68.0
9.06
24.00
16.0
128.0
23.0
32.0
16.86
19.0
25 6s
48.36
Cast iron specific heat at 212° F. is .109.
" " " 572° F. is .140.
" " " 2150° F. is .190.
Table of Physical Constants
Table of Physical Constants
203
Substances
Air
Ox^'gen
Nitrogen
Hydrogen
Carbon monoxide
Carbon dioxide
Marsh gas
defiant gas (ethylene) . . .
Aqueous vapor
Ammonia
Nitrous monoxide
Nitrous dioxide
Sulph. hydrogen
Sulph. dioxide
Chlorine
Bromine vapor
Carbon bisulphide vapor .
Hydrochloric acid
Sulphuric acid
Alcohol
Glycerine
Turpentine, oil
Air = I
Specific
gravity
1 . 1056
.4713
.0692
.9670
1.5210
.5527
.9672
.6220
.5894
1. 5241
1.0384
I . 1746
2.2112
2.4S02
5. 4772
2.6258
I . 2596
Specific heat at
constant pressure
For
equal
weight,
water
= 1
.2377
.2175
.2438
3.4090
.2450
.2169
• 5929
.4040
.4805
.5084
.2262
.2317
.2432
.1544
.1210
.0555
.1569
.1882
■ 335
.700
.450
.426
For
equal
volumes
.2377
• 2405
.2368
.2359
.2370
.3307
.3277
.4106
.2989
.2996
.0447
.2406
.2857
.3414
.2965
.3040
.4122
.2333
Specific
heat at
constant
volume
Pounds
per
cubic
foot
.1689
.1550
.1730
2.4060
.1730
.1710
.4670
.3320
.080728
.089210
.078420
.005610
.078100
.123430
.044880
.079490
Cubic
feet
per
pound
12.387
11.209
12.752
178.230
12.804
8.102
22.301
12.580
204 Mechanics
Weight oi Air Ki-.QtTRi.D for Combustion of Coal
Substances
Pounds of
air
B.t.u. from
combustion
of one pound
12.30
JS.oo
18.00
15.60
14.500
61.524
24.021
21.524
18,260
defiant gas
Boiling Points at Sea Level
Water 100
Alcohol 78.
Ether 34-
Carbon bisulphide 46.
Nitric acid (strong) 120.
Sulphuric acid 326.
Oil turpentine 157.
Mercury 350.
Aldehyde 20.
Combining Equivalents
Oxygen 8.0 "C.
Hydrogen i .0
Nitrogen 140
Carbon 6.0
Sulphur 8.0
Phosphorus 10.33
Chlorine 35 . 5
Iodine 25.4
Potassium 39-1
Iron 28.0
Copper 31.7
Lead 103. S
Silver 108.0
Bromine 80 o
Sodium 23.0
Fluorine 190
Lithium 70
Rubidium 85.4
Lineal Expansion for Solids
205
Lineal Expansion for Solids at Ordinary Temperature
FOR 1° F.
Solids
Aluminum, cast
Antimony, cryst
Brass, cast
Brass, plate
Brick
Bronze (copper, 17; tin, 2H; zinc, i). .
Bismuth
Cement, Portland (mixed), pure
Concrete: cement, mortar and pebbles
Copper
Ebonite
Glass, English flint
Glass, hard
Glass, thermometer
Granite (gray, dry)
Granite (red, dry)
Gold, pure
Iron (wrought)
Iron (cast)
Lead
Marbles, various J .
Masonry, brick w
Mercury (cubic expansion)
Nickel
Pewter
Plaster, white
Platinum
Porcelain
Silver, pure
Slate
Steel, cast
Steel, tempered
Stone, sand, dry
Tin
Wedgewood (ware)
Wood, pine
Zinc
Zinc 8 \
Tin I
From 1° F.
Length
00001234
00000627
00000957
0OOOIOS2
00000306
00000975
00000594
0000079s
00000887
00004278
00000451
00000397
00000499
00000438
00000498
00000786
00000648
00000556
00001571
00000308
00000786
00000256
00000494
00009984
00000695
00001129
00000922
00000479
00000200
00001079
00000577
00000636
00000689
00000652
00001163
00000489
00000276
00001407
00001496
Coefficient
of expansion
from 32° to
212° F.
.002221
.001129
.001722
.001894
.000550
.001774
.001755
.001070
.001430
.001596
.007700
.000812
.000714
.000897
.000789
.000897
001415
.001166
.001001
. 002828
.000554
.00141S
.000460
.000890
.017971
.001251
.002033
.001660
.000863
.000360
.001943
.001038
.001144
.001240
.001174
.002094
.000881
.000496
.002532
.002692
Cubical expansion or expansion of volume equals lineal expansion multiplied by 3.
The coefficient of expansion from 32° to 212° F. divided by 100 gives the lineal
expansion for corresponding solid for 1° C.
The expansion of metals above 212° F. is irregular and more rapid.
2o6 Mechunics
Furnace Temperatures
M. Lc C'hatclicr finds ihc mcllinj; heal of while cast iron 2075" F.,
and ihal of gray cast iron al 2226° V. Mil<i sled melts at 2687" F., semi-
mild at i^si" !•'. and hard steel at 2570° F.
Tiie furnace for hard |x)rcclain al the end of the Ijakin^ has a heal of
^498° F. The heat of a normal incandescent lamp is 3272° F., but it
may 1)0 pushed beyond 3812° F.
The following arc some of the temi)cratures delermlned by Professor
Roberts-Austin.
TcH-ton Opcn-hcarth Furnace {Woolwich Arsenal)
Temperature of steel, 0.3 per cent carbon, pouring into ladle. . . 2993° F.
Temperature of steel, 0.3 per cent carbon, pouring into large
mold 2876° F.
Reheating furnace, Woolwich Arsenal, temperature of interior. . 1 706° F.
Cupola furnace, temperature of No. 2 cast iron pouring into
ladle 2912° F.
Determinations by M. Lc Chalelier. Bessemer Process.
Six-ton Converter
Bath of slag 2876° F.
Metal in ladle 2984° F.
Metal in ingot mold 2876° F.
Ingot in reheating furnace 2192° F.
Ingot under the hammer 1976° F.
Open-hearth Furnate {Siemans) Semi-mild Steel
Fuel gas near gas generator 1328° F.
Fuel gas entering into bottom of regenerator chamber. . . 752° F.
Fuel gas issuing from regenerator chamber 2192° F.
Air issuing from regenerator chamber 1832° F.
Chimney Gases
Furnace in perfect condition 590° F.
Opcn-ltearth Furnace
End of the melting of pig charge 2588° F.
Completion of conversion 2732° F.
Fownes Elementary Chemistry gives relative conductivity of metals
as follows: silver 1000
Copper 736
Gold 532
Brass 236
Tin 14s
Iron 119
Steel 116
Lead 85
Platinum ' 84
German silver 63
Bismuth 18
Measurement of Heat
207
MEASUREMENT OF HEAT
Unit of Heat
The British thermal unit (B.t.u.) is the quantity of heat required to
raise the temperature of one pound of pure water one degree Fahrenheit
at 39.1° F.
The French thermal unit, or calorie, is the quantity of heat recjuired to
raise the temperature of one kilogram of pure water one degree Centi-
grade at 4° C, which is equivalent to 39.1° F. The French calorie is
equal to 3.96S British thermal units; one B.t.u. is equal to .252 calories.
Mechanical Equivalent of Heat
This is the number of foot pounds equivalent to one B.t.u. Joule's
experiments gave the figure 772, which is known as Joule's equivalent.
Recent experiments give higher figures and the average is now taken
to be 778.
Heat of Combustion in Oxygen of Various Substances
Substance
Hydrogen to liquid water at 0° C
Hydrogen to steam at 100° C
Carbon (wood charcoal) to carbonic acid (CO2); ordinary
temperatures
Carbon graphite to CO2
Carbon to carbonic oxide, CO
Carbonic oxide to CO2 per unit of CO
CO to CO2 per unit of C = 2H X 2403
Marsh gas, CHi to water and CO2
defiant gas, C2H4 and water and CO2
Heat units
Cent.
Fahr.
( 34,462
62,032
] 33,8oS
60,854
( 34.342
61,816
28,732
51,717
( 8,080
14.544
{ 7,900
14,220
1 8,137
14,647
7,901
14.222
2,473
4,451
( 2,403
4.325
< 2,431
4.376
( 2,38s
4.293
S.607
10,093
( 13,120
23,616
< 13,108
23.594
( 13,063
23.S13
( 11,858
21.344
< 11,942
21,496
1 11,957
21.523
If one pound of carbon is burned to CO2, generating 14,544 B.t.u., and the CO2
thus formed is immediately reduced to CO in the presence of glowing carbon, by the
reaction CO2 + C = 2 CO, the result is the same as if the two pounds of C had been
burned directly to 2 CO, generating 2 X 445i = 8902 heat units; consequently
14,544 — 8902 = 5642 heat units have disappeared or become latent and the reduction
of CO2 to CO is thus a cooling operation.
Kent, 456.
208
Heat
RADIATION OF HEAT
Relative Rauiating anu kKFLtcriNc; Power of Ditkerent
Substances
Substances
LAinpblack
Water
Writing paper
Ivory, jet, marble
Ordinary glass
Ice
Cast iron, bright polished
Mercury, about
Wrought iron, polished. . .
Zinc, polished
Steel, polished
Platinum, polished
Tin
Brass, cast, dead polish...
Brass, bright polished . . . .
Copper, varnished
Copper, hammered
Silver, polished, bright. . .
Kaaiating
or abaorb-
Reflect inc
power
mg power
100
0
lOO
0
98
2
93 to 98
7 to 3
90
10
8S
IS
25
7S
23
77
23
77
19
81
17
83
24
76
IS
8S
II
89
7
93
14
86
7
93
3
97
Experiments of Dr. A. M. Mayer give the following: The relative
radiations from a cube of cast iron, having faces rough, as from the
foimdry, planed, drawfiled and polished; and from the same surfaces
oiled, are as below (Professor Thurston).
Surface
Rough . . .
Planed . . .
Drawfiled
Polished . .
Oiled
Dry
100
100
60
32
49
20
45
18
Relative Nonconducting Power of Materials
RELATrvE Heat-Conducting Power of Metals
209
Metals
Conduc-
tivity
Metals
Conduc-
tivity
Silver
1000
981
84s
811
677
66s
641
608
628
Wrought iron
436
Gold
Tin
Steel
397
380
Platinum
359
287
Aluminum
Lead
Zinc
Antimony, cast, horizontal. . .
Antimony, cast, vertical
Bismuth
192
61
Zinc, cast, vertical
Relative Nonconducting Power of Materials
(Professor Ordway)
Substance i inch thick. Heat applied
310° F.
Pounds of
Solid
water heated
matter in
Air
10° F. per
I square
included,
hour through
foot I inch
parts in
I square
thick, parts
1000
foot
in 1000
8.1
56
944
9.6
50
9SO
10.4
20
980
10.3
185
81S
9-8
56
944
10.6
244
756
13.9
119
881
35.7
506
494
12.4
23
977
42.6
285
71S
13.7
60
940
lS-4
ISO
8so
I4S
60
940
20.6
253
747
30.9
368
632
49 0
81
919
48.0
0
1000
62.1
527
471
13.0
14.0
21.0
21.7
18.0
18.7
16.7
22.0
21.0
27.0
Loose wool
Live geese feathers
Carded cotton wool
Hair felt
Loose lampblack
Compressed lampblack
White-pine charcoal
Anthracite coal dust
Loose calcined magnesia
Compressed calcined magnesia ....
Light carbonate of magnesia
Compressed carbonate of magnesia
Loose fossil meal
Ground chalk
Dry plaster of Paris
Fine asbestos
Air, alone
Sand
Best slag wool
Paper
Blotting paper, wound tight
Asbestos paper, wound tight
Straw rope, wound spirally
Loose rice chaff
Paste of fossil meal with hair
Paste of fossil meal with asbestos . .
Loose bituminous coal ashes
Loose anthracite coal ashes
axo Heat
Professor Ordway states that later cxpcnments made with still air
gave results which differ little from cotton wool, hair felt or compressed
lampblack. Asbestos is one of the poorest conductors.
IIkat-Conducting Powkr of Covering Materials
(J.J. Coleman)
Mineral wool loo Charcoal 140
Hair fell 117 Sawdust 163
Cotton wool 122 Gas works breeze 230
Sheep's wool 136 Wood and air sjiacc 280
Infusorial earth 136
Boiling Points at Atmospheric Pressure
Ether, sul|)huric 100° F. Average sea water 213.2° F.
Carbon bisulphide 118° F. Saturated brine 226° F.
Ammonia 140° F. Nitric acid 248° F.
Chloroform 140° F. Oil of turpentine 315" F.
Bromine 145° F. Phosphorus 554° F.
Wood-spirit 150° F. Sulphur 570° F.
Alcohol 173° F. Sulphuric acid 590° F.
Benzine 176° F. Linseed oil 597° F.
Water 212° F. Mercury 676° F.
The boiliag points of liquids increase as the pressure increases.
Table of Equivalent Temperatures
Table of EqinvALENX Temperatures, Centigrade to
Fahrenheit
Rule to change the values: Fahr. = " C. + 32°
Cent. = (F. - 32°)
Degrees
Degrees
Degrees
Degrees
Degrees
Cent.
Fahr.
Cent.
Fahr.
Cent.
Fahr.
Cent.
Fahr.
Cent.
Fahr.
— 10
+14.0
22
71.6
54
129.2
86
186.8
190
374
- 9
+15. 8
23
73.4
55
131. 0
87
188.6
195
383
- 8
+17.6
24
75.2
56
132.8
88
190.4
200
392
- 7
+19-4
25
77.0
57
134.6
89
192.2
205
401
- 6
+21.2
26
78.8
58
136.4
90
194
210
410
- 5
+23 0
27
80.6
59
138.2
91
195.8
21S
419
- 4
+24.8
28
82.4
60
140.0
92
197.6
220
428
- 3
+26.6
29
84.2
61
141. 8
93
199.4
22s
437
— 2
+28.4
30
86.0
62
143.6
94
201.2
230
446
— I
+30.2
31
87.8
63
145.4
95
203.0
235
455
0
+32.0
32
33
89.6
91.4
64
65
147.2
149.0
96
97
204.8
206 6
240
245
464
+ I
33.8
473
2
35.6
34
93.2
66
150.8
98
208.4
250
482
3
37.4
35
95.0
67
152. 6
99
210.2
255
491
4
39-2
41.0
36
37
96.8
98.6
68
69
154.4
156.2
100
212
260
265
Soo
5
105
221
S09
6
42.8
38
100.4
70
158.0
no
230
270
518
7
44-6
39
102.2
71
159.8
"5
239
275
527
8
46.4
40
104.0
72
161. 6
120
248
280
536
9
48.2
41
105.8
73
163.4
I2S
257
285
545
10
50.0
42
107.6
74
165.2
130
266
290
554
II
SI. 8
43
109.4
75
167.0
I3S
275
295
563
12
S3. 6
44
III. 2
76
168.8
140
284
300
572
13
SS.4
45
113. 0
77
170.6
145
293
30S
S8l
14
S7.2
46
114. 8
78
172.4
150
302
310
590
IS
59-0
47
116. 6
79
174.2
155
3"
31S
599
16
60.8
48
118. 4
80
176.0
160
320
320
608
17
62.6
49
120.2
81
177.8
16S
329
32s
617
18
64.4
SO
122.0
82
179.6
170
338
330
626
19
66.2
SI
123.8
83
181. 4
175
347
335
63s
20
68.0
52
125.6
84
183.2
180
3S6
340
644
21
69.8
S3
127.4
85
185.0
185
36s
345
6S3
Data Sheet No. S3, The Foundry, November, 1909.
Heat
Tahi-k of Kquivalent Tkuperatures, Centigrade to
Kaurenueit — {CotUinucd)
Degrees
Degrees
Degrees
Degrees
Cent.
Fahr.
Cent.
Fahr.
Cent.
Fahr.
Cent.
Fahr.
Cent.
Fahr.
3SO
662
, -J
1238
830
1526
990
1814
3SS
671
51S
'.'.iy
'>7S
1247
83s
1 535
995
1823
360
680
S20
968
680
1256
840
1544
IQOO
1833
36s
689
52s
977
68s
126s
845
1553
1005
1841
370
698
530
986
690
1274
8so
1562
lOIO
1850
37S
707
535
995
695
1283
855
1571
lois
i8S9
380
716
540
1004
700
1292
860
IS80
1020
1868
38s
725
545
1013
70s
1 301
86s
1589
1025
1877
390
734
5SO
1022
710
1310
870
1598
1030
1886
395
743
555
1031
7IS
1319
875
1607
1035
189s
400
752
560
1040
720
1328
880
1616
1040
1904
40s
761
565
1049
725
1337
88s
1625
I04S
1913
410
770
570
1058
730
1346
890
1634
1050
1933
41S
779
S7S
1067
735
1355
89s
1643
loss
1931
420
788
580
1076
740
1364
900
l6s2
1060
1940
425
797
58s
1085
745
1373
905
1661
106s
1949
430
806
S90
1094
750
1382
910
1670
1070
1958
435
81S
595
1 103
755
1391
915
1679
I07S
1967
440
824
600
1112
760
1400
920
1688
1080
1976
445
833
605
1121
765
1409
925
1697
1085
198s
450
842
610
1130
770
1418
930
1706
1090
1994
455
851
615
1139
775
1427
935
1715
1095
2003
460
860
620
1148
780
1436
940
1724
1 100
30I2
465
869
62s
"57
78s
1445
945
1733
lios
2021
470
878
630
1166
790
1454
9SO
1742
IIIO
2030
475
887
635
1175
795
1463
955
I7SI
1115
2039
480
896
640
1 184
800
1472
960
1760
1 120
2048
485
905
645
1 193
80s
1481
96s
1769
1125
20S7
490
914
650
1202
810
1490
970
1778
1 130
2066
495
923
655
J2II
815
1499
975
1787
1I3S
2075
Soo
932
660
1220
820
1508
980
1796
1 140
20S4
S05
941
66s
1229
82s
1517
98s
180S
"45
1 1 50
2093
2102
Data Sheet No. 54. The Foundry, November, 1909.
Strength of Materials
Comparison of Thermometer Scales
213
Centi-
grade
Reaumur
Fahren-
.heit
Centi-
grade
Reaumur
Fahren-
heit
Centi-
grade
Reaumur
Fahren-
heit
-30
—24.0
—22.0
14
II. 2
57.2
58
46.4
136.4
-28
-22.4
-18.4
16
12.8
60.8
60
48.0
140.0
-26
—20.8
-14.8
18
14.4
64.4
62
49.6
143.6
-24
—19.2
— II. 2
20
16.0
68.0
64
51.2
147-2
—22
-17.6
- 7.6
22
17.6
71.6
66
52.8
150.8
—20
— 16.0
- 4.0
24
19.2
75.2
68
54-4
154-4
-18
-14.4
- 0.4
26
20.8
78.8
70
56.0
158-0
-16
-12.8
3-2
28
22.4
82.4
72
57.6
161. 6
-14
— II. 2
6.8
30
24.0
86.0
74
59 2
l6s-2
— 12
- 9-6
10.4
32
25.6
89.6
76
60.8
168.8
-10
- 8.0
14.0
34
27.2
93-2
78
62.4
172.4
- 8
- 6.4
17.6
36
28.8
96.8
80
64.0
176.0
- 6
- 4.8
21.2
38
30.4
100.4
82
65.6
179.6
- 4
- 3.2
24.8
40
32.0
104.0
84
67.2
183.2
— 2
- 1.6
28.4
42
33.6
107.6
86
68.8
186.8
0
0.0
32.0
44
35.2
III. 2
88
70.4
190.4
2
1.6
35.6
46
36.8
II4.8
90
72.0
194.0
4
3.2
39-2
48
38.4
118. 4
92
73.6
197.6
6
4.8
42.8
50
40.0
122.0
94
75-2
201.2
8
6.4
46.4
52
41.6
125.6
96
76.8
204.8
10
8.0
50.0
54
43.2
129.2
98
78.4
208.4
12
9.6
53.6
S6
44.8
132.8
100
80.0
212.0
No. 21, Supplement to Machinery, June, 1903.
Strength of Materials
(From notes on Machine Design, by permission of the author, Prof. Chas. H.
Benjamin, Cleveland, O.)
Kind of metal
Ultimate strength
Elastic
limit,
tension
Modu-
lus of
rupture,
trans-
Ten-
Com-
Shear-
sile
pression
ing
verse
55, 000
38,000
45,ooo
28,000
40,000
50,000
40,000
25,000
45.000
35.000
22,500
30,000
60,000
100,000
50,000
32,000
90,000
90,000
80,000
50,000
120,000
60,000
Un-
18,000
75.000
25,000
certain
36,000
36,000
42,000
16,000
38,000
125,000
18,000
18,000
12,000
24,000
75,000
24,000
30,000
36,000
100,000
85,000
132,000
58,000
43,000
20,000
28,000
13,000
14,000
Modu-
lus of
elastic-
ity,
tension
Wrought iron, small bars
Wrought iron, plates
Wrought iron, large forgings. .
Steel, O. H. plate
Steel, Bessemer
Steel, machinery
Steel, crucible or tool
Cast iron
Malleable castings
Steel castings
Brass castings
Copper castings
Bronze, gun metal
Bronze, 10 Al, 90 Cu
Bronze, phosphor
Aluminum castings
20,000,000
25,000,000
25,000,000
28,000,000
29,000,000
40,000,000
18,000,000
30,000,000
9.000,000
15,000,000
10,000,000
14,000,000
11,000,000
214
StrcnKlh of Malrriuls
Mauri.il
Steel wire. . .
Iron wire... .
Copper wire .
Brass wire
Bronze wire ...
German silver.
Woods:
Ash
Beech ....
Elm
Hemlock.
Hickory
Maple
Oak (white) . . . .
Oak aive)
Pine (white) . . .
Pine (yellow)...
Spruce
Walnut (black).
Tension | Comprcs-
per srjuarc sion per
inch square inch
Brick (pressed).
Granite
Limestone
318.823
S9.246
97.908
^-.'Kl^
46.494
81,114
98.578
78.049
81. 735
92,224
11,000
17.207
ii.Soo
18,000
13.500
8,700
12.800
18,000
10,500
10,250
19.500
11.000
IS.900
14.500
I2,S0O
6S0O
7700
S300
8000
6800
7000
6850
S40O
8500
5700
8000
Tons per
square foot
40
300
30O
1200
250
1000
Shear per
square
inch
6280
S223
2750
604s
728s'
4425
8480
24SO
S73S
S25S
Also
Properties of Air 21$
Strength of Lime and Cement Mortar
Tensile Strength, Pounds per Square Inch
Age 7 days.
Lime mortar 8
2o per cent Rosendale 8.5
^ 20 per cent Roseland 8.5
30 per cent Rosendale 11
30 per cent Portland 16
40 per cent Rosendale 12
40 per cent Portland 39
60 per cent Rosendale 13
60 per cent Portland 58
80 per cent Rosendale 18.5
80 per cent Portland 91
100 per cent Rosendale 23
100 per cent Portland 120
Coefficient of Friction
If two bodies have plane surfaces in contact and the plane of contact
be inclined so that one body just begins to slide upon the other, the angle
made by this plane with a horizontal plane is called the angle of repose.
The coefficient of friction is the ratio of the ultimate friction to the
pressure perpendicular to the plane of contact, and is equal to the
tangent of the angle of repose.
Thus, if R denotes the friction between the surfaces, Q the perpendicu-
lar pressure and F the coefficient of friction. Then
F = ^ and i? = FQ.
Centrifugal Force
In a revolving body the force expended to deflect it from a rectilinear
to a curved path is called centrifugal force and is equal to the weight of
the body multiplied by the square of its velocity in feet per second,
divided by 32.6 times the radius; or, if F equals centrifugal force, W
equals weight of body, V equals velocity in feet per second and R equals
the radius, then F = ^r^. If N equals the number of revolutions
32.10 K
per minute, the formula is reduced to F = .000341 WN^R.
Properties of Air
Air is a mechanical mixture of the gases, oxygen and nitrogen; 21
parts oxygen and 79 parts nitrogen by volume, or 23 parts oxygen and
77 parts nitrogen by weight. The weight of pure air at 32° F. and 29.9
barometer, or 14.6963 pounds per square inch; or 21 16.3 pounds per
2l6
Air
square foot is .0807^8 pouiuis. The volume of one pound is 12.387 cubic
feet.
Air e-xjiands 1/41JI.2 of its volume for every increase of 1° I"., and its
volume varies inversely as the pressure.
Volume, Density and Pressure of Air at \'mi r Temperatures
(D. K.Clark.)
Volume at atmospheric
Pressure at constant
pressure
Density, lbs.
vol
umc
per cubic foot
at atmospherii
Fahr.
Cubic feet
Comparative
pressure
1 iJUllilM ji'-I
* ■Jln)MIiillVe
in I pound
volume
square inch
pressure
0
11.583
.086331
13.96
.881
32
12.387
'.M.5
.080728
13 86
943
40
12.S86
.958
.079439
14 08
938
SO
12.840
.977
.077884
14 36
■ 977
62
13.141
1. 000
.076097
14.70
1. 000
70
13.342
l.ois
.074950
14.92
i.ois
80
13. 593
1.0.34
.073565
IS. 21
1.034
90
13 845
1.054
.072230
IS 49
I 054
100
14.096
I 073
.070942
IS. 77
1.073
no
14 344
1.092
.069721
16.05
1.093
120
14.592
I. Ill
.068500
16.33
I. Ill
130
14.846
1. 130
.067361
16 61
1. 130
140
IS 100
I 149
.066221
16.89
1. 149
ISO
15. 351
1. 168
.065155
17.19
1. 168
160
IS 603
1. 187
.064088
17. SO
1. 187
170
15.854
1.206
.063089
17.76
i.ao6
180
16.106
1.226
.062090
18.02
t.236
2CX3
16.606
1.264
.060210
18.58
1.264
210
16.860
1.283
.O.S93I3
1S.86
1.283
212
16.910
1.287
.059135
18.92
1.287
Pressure of the Atmosphere per Square Inch and per
Square Foot at Various Readings of the Barometer
Rule. — Barometer in inches X .4908 = pressure per square inch;
square inch X 144 = pressure per square foot.
pressure per
Barometer,
inches
Pressure per
square inch,
Pressure per
square foot.
Barometer,
inches
Pressure per
square inch,
Pressure per
square foot.
pounds
pounds
pounds
pounds
28.00
13.74
1978
29.75
14.60
2102
28.25
13.86
1995
30.00
14 72
2119
28.50
13.98
2013
30.25
14 84
2136
28.75
14. II
2031
30.50
14.96
2154
29.00
14.23
2049
30.75
IS. 09
2172
29.25
14. 35
2066
31 00
15.21
2190
29.50
14-47
2083
Properties of Air
217
Babometric Readings Corresponding with Different
Altitudes ( Kent.)
Altitude,
feet
Reading of
barometer,
inches
Altitude,
feet
Reading of
barometer,
inches
0
68.9
416.7
767.7
1 122 I
1486.2
1850.4
2224.5
2599-7
2962.1
3369-5
30-00
29.92
29.52
29-13
28.74
28.35
27-95
27-55
27.16
26.77
26.38
3763.2
4163-3
4568.3
4983.1
5403.2
5830.2
6243.0
6702.9
7152.4
7605.1
8071.0
25.98
25.59
25.19
24.80
24.41
24.01
23.62
23.22
22.83
22.44
22 04
Horse Power Required to Compress One Cubic Foot of
Free Air per Minute to a Given Pressure (Richards.)
Air not cooled during compression; also the horse power required, supposing the
air to be maintained at constant temperature during the compression.
Gauge
Air not
Air at
pressure
cooled
constant
temperature
100
.22183
■14578
90
.20896
.13954
80
.19521
•13251
70
.17989
.12606
60
.164
.11558
50
.14607
.10565
40
.12433
.093667
30
. 10346
.079219
20
076808
.061188
10
.044108
.036944
5
.024007
.020848
3l8
Air
Horse Power Required to Deliver One Cubic Foot of
Air per Minute at a Given Pressure (Richard*.)
Air not cooled during compression; also the horse power required, supposing the
air to be maintained at constant temperature during the compression.
GauRc
prcssiiri'
Air not Air at
coolcl constant
temperature
loo
t 7.517 I
i.}8oi
9°
1.4883
99387
80
1.25779
8S28
70
1 03683
72651
60
.83J44
S8729
so
.64291
46s
40
.46271
34859
30
.31456
24086
20
.181279
14441
10
.074106
06069
-^
.032172
027938
In computing the above tables an allowance of 10 per cent has been
made for friction of the compressor.
Pressure of Water
219
Pressure of Water
Pressure in Pounds per Square Inch for Different
Heads of Water (Kent.)
At 62° F. I foot head 0.433 pound per square inch, 0.433 X 144 = 62.352 pounds
per cubic foot.
Head.
feet
0
I
2
3
4
S
6
7
8
9
0
0.433
0.866
1,299
1-732
2.165
2.598
3.031
3 464
3.897
10
4330
4.763
5.196
5. 629
6.062
6.495
6.928
7.361
7-794
8 227
20
8,660
9 093
9.526
9 959
10.392
10.825
11.258
I I. 691
12.124
12.557
30
12.990
13.423
13.856
14.298
14.722
15 155
15.588
16.021
16.454
16.887
40
17320
17 . 753
18.186
18.619
19 052
19 485
19.918
20.351
20.784
21.217
50
21.650
22.083
22.516
22.949
23.382
23.819
24 . 248
24 . 681
25.114
25.547
60
25.980
26.413
26 . 846
27 279
27.712
28.145
28.578
29 on
29.444
29.877
70
30.310
30.743
31.176
31.609
32.042
32.47s
32.908
33.341
33.774
34.207
80
34 640
35 073
35 506
35 939
36.372
36.805
37.238
37.671
38 . 104
38.537
90
38.970
39 403
39 836
40.269
40.702
41.13s
41 568
42.001
42.436
42 867
Head in Feet of Water, Corresponding to Pressures in
Pounds per Square Inch (Kent.)
I pound per square inch 2.30947 feet head, i atmosphere 14.71 pounds per square
inch 33.94 foot head.
Pres-
sure
0
3
4
5
7
8
9
0
2.309
4-619
6.928
9-238
11.547
13.857
16.166
18.476
20.78s
10
23-0947
25.404
27-714
30.023
32-333
34.642
36.952
39.261
4I-S70
43.880
20
46- 1894
48-499
50,808
53.118
55.427
57.737
60.046
62.356
64-665
66.975
30
69.2841
71-594
73 903
76.213
78.522
80.831
83-141
85 . 450
87.760
90.069
40
92.3788
94.688
96.998
99 307
101.62
103.93
106 . 24
108.55
110.85
113 16
50
IIS. 4735
117-78
120.09
122.40
124.71
126.02
129.33
131-64
133-95
136.26
60
138.5682
140.88
143.19
145.50
147.81
150.12
152.42
154-73
157 04
159 35
70
161.6629
163.97
166.28
168.59
170.90
173.21
175.52
177-83
180.14
182.45
80
184.7576
187.07
189.38
191.69
194.00
196.31
198.61
200.92
203.23
205.54
90
207.8523
210.16
212.47
214.78
217.09
219.40
221.71
224.02
226.33
228.64
Electrical and Mechanical Units
Equivalent Values of Electrical and Mechanical Untis
Uniu
Equivalent value in other uoita
I kilowatt hour -
i.ooo watt hours.
1 . 34 horsc-powcr hours.
2,654,200 (I. lbs.
3,600,000 joules.
3.412 heal units.
367,000 kilogram metres.
.23s lb. carbon, oxidized with perfect efficiency.
3.53 lbs. water cvap. from and at 21a" F.
22.75 lbs. of water raised from 62* P., to 3I2* F.
I horse-power hour =
.746 K.W. hours.
1.980,000 ft. lbs.
2,545 heat units.
273,000 kilogram metres.
.175 lb. carbon oxidized with perfect efficiency.
2.64 lbs. water evap. from and at 212° F.
17 lbs. of water raised from 62° F. to 212* F.
I kilowatt =
1,000 watts.
1.34 horse power.
2,654,200 ft. lbs. per hour.
44.240 ft. lbs. per minute.
737-3 ft. lbs. per second.
3,412 heat units per hour.
56.9 heat units per minute.
.948 heat unit per second.
.2275 lb. carbon oxidized per hour.
3.53 lbs. water evap. per hour from and at 212" F.
I horse power =
746 watts.
.746 K.W.
33,000 ft. lbs. per minute.
550 ft. lbs. per second.
2,545 heat units per hour.
42.4 heat units per minute.
.707 heat unit per second.
.175 lb. carbon oxidized per hour.
2.64 lbs. water evap. per hour from and at 212" F.
I joule =
I watt second.
.000000278 K.W. hour.
.102 k.R.m.
.0009477 heat units.
.7373 ft. lbs.
1 foot pound =
1.356 joules.
.I383k.g.m.
.000000377 K.W. hour.
.001285 heat unit.
.0000005 H.P. hour.
Equivalent Values of Electrical and Mechanical Units 221
Equivalent Values of Electrical and Mechanical
Units — {Continued)
Units
I watt per square inch =
Equivalent Value in Other Units
I joule per second.
.00134 H.P.
3.412 heat units per hour.
■ 7373 ft. lb. per second.
.003s lb. of water evap. per hour.
44.24 ft. lbs. per minute.
8.19 heat units per sq. ft. per minute.
6,371 ft. lbs. per sq. ft. per minute.
.193 H.P. per sq. ft.
I heat unit =
I. OSS watt seconds.
778 ft. lbs.
107.6 kilogram metres.
.000293 K.W. hour.
,000393 H.P. hour.
.0000688 lb. of carbon oxidized.
.001036 lb. water evap. from and at 212°
I heat unit per
square foot per
minute =
. 122 watts per square inch.
.0176 K.W. per sq. ft.
.0236 H.P. per sq. ft.
I kilogram metre =
.233 ft. lbs.
.0000036s H.P. hour.
.00000272 K.W. hour.
.0093 heat unit.
I pound carbon
oxidized with perfect
efficiency =
14,544 heat units.
I . II lbs. of anthracite coal oxidized.
2.5 lbs. dry wood, oxidized.
21 cubic ft. illuminating gas.
4.26 K.W. hours.
5.71 H.P. hours.
11,315,000 ft. lbs.
15 lbs. water evap. from and at 212° F.
I pound water
evaporated from
and at 212° F. =
.283 K.W. hour.
.379 H.P. hour.
965.7 heat units.
103,900 k.g.m.
1,019,000 joules.
751,300 ft. lbs.
.0664 lb. of carbon oxidized.
CHAPTER \1
ALLOYS
An alloy is a combination \)y fusion of two or more metals. The com-
l)ination may be a chemical one; generally, however, there is an excess
of one or more of the constituents.
Metals do not unite indiCferently, but have certain affinities; thus
zinc ;ind lead do not unite, but either will mi.x with silver in any pro-
portion.
Alloys arc generally harder, less ductile and have greater tenacity than
the mean of their components. The melting point of an alloy is as a rule
below that of any of its components, and it is more easily o.xidized.
The specific gravity of an alloy may be greater, equal to, or less than
the mean of its components.
In alloys of copper and tin the maximum tensile and compressive
strength is afforded by a mixture containing 82.7 per cent copper and
17.3 per cent tin. The minimum strength is shown by a composition
of 62.5 per cent copper and 37.5 per cent tin.
Alloys of Copper axd Tin
Mean composition by analysis
Tensile
strength in
pounds per
square inch
Elastic
limit in
pounds per
square inch
Crushing
strength in
Copper
Tin
pounds per
... .n inch
12.760
24.580
28.540
29.430
32.980
22,010
5.585
2,201
1. 455
3.010
6.775
6.390
6.450
4.780
•^.soi;
11.000
10.000
19.000
20.000
97.89
92.11
87. IS
80.95
76.63
69.84
65.34
56.70
44.52
23.35
11.49
8.57
3 72
1.90
7.80
12.75
18.84
23 24
29.88
34.47
43.17
55.28
76.29
88.47
91 39
96 31
34.000
42.000
53.000
78.000
22.010
S.S85
2.201
1.455
3.010
6.775
3.500
3.500
2.750
144.000
147.000
84.700
35.800
10,100
9.800
9.800
6,400
Composition of Alloys in Common Use in Brass Foundries 223
Alloys of Copper and Zinc
Mean composition by analysis
Copper
Zinc
97.83
1.88
82.93
16.98
76.6s
23.08
71.20
28.54
66.27
33.50
60.94
38.65
55. IS
44.44
49.66
SO. 14
47.56
52.28
43-36
56.22
32.94
66.23
20.81
77.63
12.12
86.67
4.35
94-59
0
100.00
Tensile
strength in
pounds per
square inch
27,240
32,600
30,520
30,510
37.800
41,065
44,280
30,990
24,150
9,170
1.774
9,000
12.413
18,06s
5.400
Elastic limit
per cent of
breaking load
in pounds per
square inch
26.1
84.6
29.5
25. r
40.1
44.00
54 5
100. o
100. o
100. o
100. o
100. o
100. o
75 o
Crushing
strength in
pounds per
square inch
75.000
78,000
117,400
121,000
Composition of Alloys in Common Use in Brass Foundries
(American Machinist.)
Alloys
Admiralty metal
Bell metal
Brass (yellow)! . .
Bush metal
Gun metal
Steam metal. . . .
Hard gun metal.
Muntz metal. . . .
Phosphor bronze
_ j metal.
B"2'"g solder.
Copper,
Zinc,
Tin,
Lead,
lbs.
lbs.
lbs.
lbs.
1 87
S
8
16
4
16
8
5
64
8
4
4
32
I
3
20
I
1.5
I
16
2.5
60
40
92
8.0
90
10. 0
16
3
50
50
For parts of engines on naval
vessels.
Bells for ships and factories.
For plumbers, ship and house
work.
Bearing bushes for shafting.
For pumps and hydraulic work.
Casting subjected to steam pres-
sure.
For heavy bearings.
For bolts and nuts, forged. Valve
spindles, etc.
Phos. tin for valves, pumps and
general work.
Phos. tin for cog and worm wheels,
bushes and bearings.
Flanges for copper pipe.
Solder for above flanges.
2 24
Alloys
Alu)ys of Coppeh, Tin and Zinc
: ii{inal mixture
Tensile
strength per
Cu
Sn '
Zn
iquare inch
yo
5
S
23.660
fis
5
10
28.840
85
10
5
35.680
Ho
5
15
37.560
80
10
10
32. 8 JO
75
5
20
34.960
75
7-5
17 5
39.300
75
10.0
15.0
Mfioo
75
15.0
10.0
28/XX3
75
20.0
50
27.660
70
SO
25 0
32.940
70
7.5
22.5
32.400
70
10. 0
20 0
26.300
70
ISO
15.0
27.800
70
20.0
10. 0
12,900
67.5
2.5
30.0
45.850
67.5
50
27. 5
34.460
67.5
7.5
25.0
30.000
65.0
2.5
32.5
38.300
65.0
50
30.0
36.000
65.0
10. 0
25.0
22.500
65.0
15.0
20.0
7.231
65.0
20.0
IS.o
2.665
60.0
2.5
375
57.400
60.0
S-O
35.0
41.160
60.0
10. 0
300
21.780
60.0
iS.o
25.0
18.020
58.22
2.3
39 48
66,500
55.0
0.5
44. 5
68.500
55 0
5.0
40.0
27.000
55 0
10. 0
35.0
25,460
50.0
50
45.0
23,000
Above tables from report of U. S. Test Board. Vol. II, 1881.
Copper-Nickel Alloys
(German Silver.)
Constituents
German silver.
Nickel silver. .
Copper,
lbs.
SI. 6
50.2
75.0
Nickel,
lbs.
25.8
14.8
Tin.
lbs.
22.6
31
25.0
Zinc,
lbs.
31.9
Delta Metal
Useful Alloys of Copper, Tin and Zinc
225
Alloys
U. S. Navy Dept., journal boxes, and guide
gibs
Tobin bronze
Naval brass
Composition, U.S. Navy
Gun metal
Tough brass for engines
Bronze for rod boxes
Bronze subject to shock
Bronze for pump castings
Red brass
Bronze, steam whistles
Bearing metal
Gold bronze
Copper,
Tin,
Zinc,
lbs.
lbs.
lbs.
6
I
.25
82.8
13.8
3-4
58.22
2.3
29.48
62.0
I.O
37 0
88.0
lO.O
2.0
92.S
S.o
2.5
91.0
7.0
2.0
85.0
SO
10,0
83.0
2.0
ISO
76. 5
II. 8
II. 7
82.0
16.0
2.0
83.0
iS.o
IS
88.0
10. 0
2.0
87.0
4.4
4.3
81.0
17.0
89.0
8.0
30
86.0
14.0
74.0
9.5
9S
98. S
2.1
S.6
Other Metals
.S lead.
4.3 lead.
2.0 antimony.
7.0 lead.
2.8 lead.
Tobin Bronze
Constituents
Pig metal,
per cent
Copper
Zinc
59.00
38.40
2.16
.11
.31
Tin
Tensile strength (cast) 66,000 pounds.
Delta Metal
Constituents
Per cent
Constituents
Per cent
.1 to 5
So.oto6s
49.9 to 30
.1 to 5
Tin
Zinc
Zinc
1.8 to 45
Copper
This metal is said to be very strong and tough.
236
Alloys
Aluuinum
Bronze
Aluminum,
per cent
Copper,
per cent
Tensile strcnifth,
pounds per square
inch
11
lo
75
5.0
89
90
92 S
9S o
89,600 lo 100,800
73,930 to 89,600
s6floo to 67,200
33.600 lo 40.3»
Analysis ok Bearing-Metal Alloys
Metal
Camelia metal
Anti-friction metal
White metal
Salgee anti-friction
Graphite bearing metal
Antimonial lead
Cornish bronze
Delta metal
Magnolia metal
American anti-friction metal
Tobin bronze
Graney bronze
Damascus bronze
Manganese bronze
Ajax metal
Anti-friction metal
Harrington bronze
Hard lead
Phosphor bronze
Extra box metal
Copper
70. ao
1.60
77.83
92 39
Trace
59 00
7S.80
76.41
90.52
81.24
5573
97.72
76.80
Tin
4
25
98
13
9
91
14
38
9
60
2
37
2
16
9
20
10
60
9
58
10
98
97
10
92
8
00
Lead Zinc
14-75
87 92
I. IS
67-73
80.69
12.40
S-io
83 55
78.44
.31
15 06
12.52
7.27
88.32
94.40
9.61
IS 00
85. 57
Tr.ce
.98
38.44
42.67
Anti-
mony
16.72
id.83
16.45
18.60
11.93
6.03
IlTMl
.07
Trace
.65
68
Phos.
■94
.20
Results of Tests for Wear
Metal
Standard
Copper-tin
Copper-tin, second experiment,
same metal
Copper-tin, third experiment,
same metal
Arsenic bronze {
Copper Tin Lead Phos. Arsenic
79.70
87.50
89.20
79.20
Composition
10.00
12. so
10.00
10.00
Rate
of
Wear
100
148
147
143
IIS
Belting
227
Concerning the preceding table Dr. Dudley remarks: "We began to
find evidences that wear of bearing metal alloys varied in accordance
with the following law. That alloy which has the greatest power of dis-
tortion without rupture will best resist wear."
Alloys Contalning Antimony
Various analyses of Babbitt metal.
Metal
Babbitt metal
Babbitt metal for light duty
Babbitt, hard -j
Britannia i
White metal
Parson's metal
Richard's metal
Penton's metal
French Navy
German Navy
Tin
so
89.3
96.0
88.9
4S-S
8S.7
81.0
22.0
85.0
86.0
70.0
16.0
7-S
85.0
Copper
1.8
4.0
3.7
15
i.o
2.0
10. o
SO
2.0
4-5
so
7.0
7-5
Anti-
mony
S
8.9
8.0
7-4
13.0
10. 1
16.0
62.0
lo.o
1.0
15.0
Zinc
2.9
1.0
6.0
79.0
87. S
Lead
2.0
10. 5
Belting
Trautwine gives the ultimate strength of good leather belting at
3000 pounds per square inch.
Jones and Laughlin give the breaking strength per inch of width,
Me thick, of good leather belting as follows:
In the solid leather 675 pounds.
At the rivet holes of splices 362 pounds.
At the lacing holes 210 pounds.
Safe working load 45 pounds per inch of width for single belts, equiva-
lent to speed for each inch of width of 720 feet per minute per horse power.
The efficiency of the double belt compared to that of a single belt is as
10 is to 7.
Making D = diameter of pulley in inches.
R = number of revolutions per minute.
W = width of belt in inches.
H = horse power that can be transmitted by the belt;
then for single belts,
„ D X RXW.
u = »
2750
228
an<J for double belts,
// =
Belling
DXKXW
1925
For WiuTu of Belt in Inches
Single belt
H X 2750
DXR
Double belt
W =
II X 1925
DxR
Revolutions per minute
H X27SO
DXW
R =
H X 192s
DxW
Diameter of pulley
H X 2750
irxR
H X 1925
WxR
These formulae are for open bcUs and pulleys of same diameter. If
the arc of contact on the smaller pullej' is less than 90 degrees, use the
following constants for those given in above formulae.
Degrees
contact
Single belt
Double belt
90
II2}4
120
135
ISO
157)^
6080
4730
4400
3850
i4io
3220
4250
3310
3080
2700
2390
2250
Belt Velocity or Circumferential Speed of Pulleys 229
Belt Velocity or Circumperential Speed or Pulleys
fc
Revolutions per minute
.2-0
3
Oh
SO
60
70
80
90
100
no
120
130
140
150
160
170
Velocity in feet per minvite
6
78. S
94.2
no
126
141
157
173
1 88
204
220
235
251
267
7
91.7
no
128
146
165
183
201
220
238
256
275
293
312
8
105
126
146
167
188
2IO
230
231
272
293
314
335
356
9
118
141
i6s
188
212
236
259
282
306
330
353
377
400
10
131
157
183
209
235
262
288
314
340
366
392
419
445
12
IS7
188
220
2S2
282
314
346
377
408
440
471
502
534
14
183
220
256
293
330
366
403
440
476
513
550
586
623
16
209
251
293
335
377
419
460
502
544
586
628
670
71a
18
230
282
330
377
424
471
S18
S65
612
6S9
707
754
801
20
262
314
366
419
471
524
576
628
681
733
785
838
890
22
288
345
403
460
518
576
634
691
749
806
864
921
979
24
314
377
440
S02
565
628
691
754
817
880
942
loos
1068
26
340
408
476
545
622
681
749
817
885
953
I021
1089
IIS7
28
380
440
S13
586
659
733
806
880
953
1026
HOC
1173
1246
30
393
471
S50
628
706
78s
864
942
1022
1 100
1 178
1256
I33S
32
419
S02
586
670
754
838
921
loos
1089
1173
1257
1340
1424
34
445
534
623
712
801
890
979
1068
IIS7
1246
1335
1424
1513
36
471
56s
659
754
848
942
1037
1131
I22S
1319
I4I4
IS08
1602
40
523
628
733
837
942
1047
1152
1256
I36I
1466
I57I
1675
1780
48
628
754
879
1005
1131
1257
1382
IS08
1633
I7S9
188s
2010
2136
54
707
848
989
1131
1272
1414
TS5S
1696
1838
1979
2120
2262
2403
60
785
942
1099
1256
1414
1571
1728
1885
2042
2199
2356
2513
2670
66
864
1036
1209
1382
1550
1728
1900
2073
2246
2419
2592
2764
2937
72
942
1131
1319
IS08
1696
188s
2073
2262
2450
2639
2827
3016
3204
78
102 1
I22S
1429
1633
1838
2042
2245
2450
26S5
2859
3063
3267
3472
84
1099
1319
1539
1754
1978
2199
2419
2639
2859
3079
3298
3518
3738
Contributed by W. J. Phillips, No. 117, extra data sheet, Machinery, October, 1909.
23°
Belting
Belt Velocity or Circumferential Speed of Pulleys
— (Continued)
Revolutions per minute
180
190
200
210
220
230
260
270
380
290
300
■3
Velocity in feet per minute
6
282
298
311
330
346
361
377
392
408
424 440
4SS
471
7
330
348
367
38s
403
421
440
458
477
495
S13
531
SSO
8
377
398
419
440
461
481
S03
523
545
565
586
607
628
9
424
447
471
495
518
542
S6S
588
613
630
660
683
707
10
471
497
524
549
576
6ca
628
654
681
707
733
759
785
12
560
597
628
6S9
691
722
754
78s
817
848
880
911
942
14
6S9
696
733
769
806
843
880
916
953
989
1026
1063
1 100
16
754
796
838
879
921
963
1005
1046
1089
1 131
1173
1214
1257
18
848
895
942
989
1037
1084
1 131
1178
1225
1272
1319
1366
1414
20
942
995
1047
1099
1152
1204
1256
1309
I36I
1414
1466
1518
1571
22
1037
1094
1 152
1209
1267
1325
1382
1440
1497
1 555
1612
1670
1738
24
1 131
1194
1257
1319
1382
1445
1508
1671
1633
1696
1759
1822
1885
26
1 22s
1293
1361
1429
1497
1565
1633
1 701
1770
1838
1906
1974
2043
28
1319
1393
1466
1539
1613
1686
1759
1832
1906
1979
2052
2126
2199
30
1413
1492
IS7I
1649
1728
1806
1885
1963
2042
2120
2199
2277
2356
32
1508
1592
1675
I7S9
1843
1927
2010
2094
2178
2252
2345
2429
2513
34
1602
1691
1780
1869
1958
2047
2136
2225
2314
2403
2492
2S8I
2670
36
1696
1 791
1885
1978
2073
2168
2262
2326
2450
2545
2639
2733
2827
40
1885
1989
2094
2199
2304
2513
2618
2723
2827
2932
3037
3141
3246
48
2262
2387
2513
2639
276s
2890
3016
3142
3267
3393
3518
3644
3769
54
2545
2686
2827
2969
31 10
3251
3393
3534
3676
3817
3959
4100
4240
60
2827
2984
3141
3298
3456
3613
3770
3927
4084
4251
4398
4555
4712
66
3110
3283
3455
3628
3801
3974
4147
4319
4492
4665
4838
5010
5183
72
3392
3581
3770
3958
4147
4335
4524
4713
4900
5059
5278
5466
5654
78
3676
3880
4084
4288
4492
4696
4900
5059
5309
5513
5717
S92I
6125
84
3958
4178
4398
4618
4838
5058
5277
5497
5717
5937
6157
6377
6597
Contributed by W. J. Phillips, No. 117, extra data sheet, Machinery, October, 1909.
Rules for Calculating Speeds and Diameters of Pulleys 231
Rules for Calculating Speeds and Diameters of Pulleys
Proposed speed of grinding spindle being given, to find proper speed
of countershaft.
Rule. — Multiply the number of revolutions per minute of the grinding
spindle by the diameter of its pulley and divide the product by the
diameter of the driving pulley on the countershaft.
Speed of countershaft given, to find diameter of pulley to drive grind-
ing spindle.
Rule. — Multiply the number of revolutions per minute of the grinding
spindle by the diameter of its pulley and divide the product by the number
of revolutions per minute of the countershaft.
Proposed speed of countershaft given, to find the diameter of pulley
for the lineshaft.
Rule. — Multiply the number of revolutions per minute of the counter-
shaft by the diameter of the tight and loose pulleys and divide the
product by the number of revolutions per minute of the lineshaft.
Table of Grinding Wheel Speeds
Revolutions
Revolutions
Revolutions
Diameter
per minute
per minute
per minute
of wheel ,
for surface
for surface
for surface
inches
speed of
speed of
speed of
4000 feet
5000 feet
6000 feet
I
15.279
19,099
22,918
2
7,639
9.549
I I, 459
3
5,093
6.366
7,639
4
3,820
4,775
5,730
S
3.056
3.820
4,584
6
2.546
3.183
3,820
7
2,183
2.728
3,274
8
1. 910
2,387
2.865
10
1.528
1,910
2,292
12
1.273
1,592
1,910
14
1.091
1,364
1,637
16
955
1,194
1.432
18
849
1,061
1.273
20
764
955
1. 146
22
694
868
1,042
24
637
796
955
30
509
637
764
36
424
531
637
The revolutions per minute at which wheels are run is dependent on
conditions and style of machine and the work to be ground.
Data Sheet, No. 52, The Foundry, October, 1909.
232
Flanycd Fillings
Rules for Obtaining Surface Speeds, etc.
To 6nd surface speed in feet per minute, of a wheel.
/?«/<•. — Multiply the circumference in feel by its revolutions per
minute.
Surface speal anrl fliamctcr of wheel bcini; K'i^'en, to find number of
revolutions of wheel spindle.
Ride. — Multiply surface speed in feet per minute by 12, and divide
the product by 3.14 times the diameter of wheel in inches.
Formulae for Dimensions of Cast Iron, Fljuiged Fittings
To unlhstand Hydraulic Pressures of 50, wo and 2ou Pounds per
Square Inch
A.
,<.... J — ^>| ^ K— -J -•:>1
Fig. 70.
Diameter of opening A
^, . , , . r, A (pressure in lbs. per sq. inch) ,
Thickness of pipe B= -^^ — ^ ■ + .1325 '"•
3(X30
- B C
Thickness of flange C= - — Radius of fillet Z) = -approximately.
Center to face of flange,
tee and cross E= — f- 2 C, or next half-inch.
2
Center to face of flange;
-f 2 C, or next
bends, up to 90° F and G = tang. ( ' ' j ( ~ )
half inch.
Center to face of flange,
45° Y H = tang. 67^" X (H + 2C, or next half-inch.
Face to face of flange,
45° Y / = tang. 22^° X (^l + 2 C + //, or next
half inch.
Diameter of flange /= standard. Number and size of bolts.. . .
A' = standard.
Formulae for Dimensions of Cast Iron, Flanged Fittings 233
Diameter of bolt circle . . . L = standard.
Radius on center line of
{Fo.a-i^)
bends, up to 90° M and A'' = —f r — Use first quar-
tang.-^-j
ter inch below.
Note. — J and L are alike for 50 and 100 lbs., as both are computed for 100 lbs. Con-
tributed. No. 43, Data Sheet, Machinery, April, 1905.
CHAPTKR \'II
USEFUL INFORMATION
Shrinkage of Castings vlh Foot
(By F. G. Walker.)
Metals
Pure aluminum
NickeJ aluminum casting alloy
■' Special Casting Alloy," made by the Pittsburg Reduo
tion Co
Iron, small cylinders
Iron, pipes
Iron, girders, beams, etc
Iron, large cylinders, contraction of diameter at top
Iron, Large cylinders, contraction of diameter at bottom.
Iron, large cylinders, contraction in length
Cast iron
Steel
Malleable iron ,
Tin
Britannia ,
Thin brass castings
Thifk brass castings
Zinc
Lead
Copper
Bismuth
Fractions
Decimals
of an inch
of an inch
>W4
.3031
9io
.1875
'W«
.1718
H«
.0625
H
.I3S0
H*
.1000
Vu
.312s
H*
.7813
Wa
.0940
H
.1350
M
.3500
H
.1350
Ma
.0833
W2
.03135
>M4
.1670
?fc
.1500
M.
.3135
Ho
.3x25
M«
.1875
Hi
.1563
Data Sheet, No. 34, The Foundry, January, 1909.
234
Rapid Conversion of Gross Tons
235
This Table Has Been Arranged for the Rapid Conversion
or Gross Tons and Fractions Thereof into Pounds
Equivalent of gross tons (2240 pounds) in pounds.
Tons
Pounds
Tons
Pounds
Tons
Pounds
Tons
Pounds
15
33.600
24
53.760
33
73.920
42
94,080
I5>/4
34,i6o
24^4
54,32°
33'/4
74,480
42H
94.640
I5'-2
34.720
24W
54 ,880
33i4
75,040
42)-^
9S,2oo
15^-4
35,280
24^4
55,440
33%
75,600
42H
95,760
16
35,840
25
56,000
34
76,160
43
96,320
l6'/4
36,400
25)4
56,560
341/4
76,720
43)4
96,880
leyz
36,960
25H
57.120
34I/4
77,280
43)'^
97,440
16M
37.S20
25?4
57.680
34%
77.840
43?4
98,000
17
38,080
26
58,240
35
78,400
44
98,560
nV*
38,640
261.4
58,800
35H
78,960
44 H
99,120
nH
39,200
26K2
59,360
35H
79,520
44 V^
99.680
i7?4
39,760
26?4
59,920
35?4
80,080
44%
100,240
18
40,320
27
60,480
36
80,640
45
100.800
isyi
40,880
27!'4
61,040
361/4
81,200
451/4
Toi,36o
181/4
41,440
27K2
61,600
361/^
81,760
45^4
101,920
i8?4
42,000
27?4
62,160
36%
82,320
45%
102,480
19
42,560
28
62,720
37
82,880
46
103,040
195 -i
43,120
281.4
63,280
37)4
83,440
46)4
103,600
19'^
43,680
28M2
63,840
37H
84,000
46V4
104,160
19U
44,240
28?4
64,400
37?4
84,560
46%
104,720
20
44,800
29
64,960
38
85,120
47
105,280
20^
45,360
295-4
65,520
381/4
85,680
47)'4
105,840
20l/^
45,920
29'/4
66,080
381/4
86,240
47)4
106,400
20^4
46,480
29M
66,640
38?4
86,800
47?4
106,960
21
47,040
30
67,200
39
87,360
48
107,520
21 W
47,600
30 M
67,760
39V4
87,920
48)-4
108 .oSo
211.4
48,160
301/4
68,320
39V4
88,480
48)-4
108,640
2I?4
48,720
30?4
68,880
39?4
89,040
48%
109,200
22
49,280
31
69,440
40
89,600
49
109,760
22I.4
49,840
31 «
70,000
40 1/4
90,160
491/4
110,320
22M2
50,400
31 H
70,560
40)4
90,720
49'/^
110,880
22?4
50,960
31 ?4
71,120
4o?4
91,280
49%
111,440
23
51,520
32
71,680
41
91,840
SO
112,000
23I4
52,080
32 H
72.240
41)4
92,400
SoVi
112,560
2M
52,640
32).4
72,800
4I>/2
92,960
5oi/^
113.120
23%
53,200
32%
73.360
41%
93,520
50%
113.680
Data Sheet No. 2, The Foundry, September, 1907.
236
Useful In forma I ion
Window Glass
Table of NuMutK of Panes in a Box
Size-
Panes
Size
Panes
Size
Panes
Size
Panes
Size
Panes
in
tea
in
to a
in
to n.
in
ton
in
toa
inches
box
inches
box
inches
9
inches
box
8XIO
90
14X20
26
20X42
34X48
5
8X12
7S
14x24
22
20x48
8
34x60
4
9x13
67
14x36
14
22XJO
11
-•H • (Ij
7
36x40
5
9x14
S7
16x18
25
22x36
9
28X42
6
36x44
S
10X12
60
16x20
23
22X42
8
28X56
S
36x48
4
10X16
AS
16x24
19
22X48
7
30X34
7
36x54
4
12x14
43
16x36
13
24X30
10
30X42
6
36x60
3
12x18
34
18X20
20
24X36
9
30X48
5
40x54
3
12X20
30
18X24
17
24X42
7
30X60
4
40x72
3
12X24
25
18x36
11
24X48
6
32X42
6
44x50
3
14X16
32
20x24
IS
26x36
8
32X48
S
44X56
3
14X18
29
20X30
12
26x42
7
32X60
4
Box Strapping
i
Fig. 71.
Improved Trojan Box Strapping
A soft steel continuous band, without rivets, which allows the nail to
be driven anywhere. The surface is studded or embossed, as illustrated,
which not only protects the head of the nail, but stiffens and strengthens
the strap. Edges are perfectly smooth. Put up in reels of 300 feet.
Width W H
Per reel $x.oo 1.25
150
I m.
2.00
Fire Brick axid Fire Clay
An ordinary fire i)ritk measures 9 by 4'i by 2^^ inches, contains
101.25 cubic inches and weighs 7 pounds. Specific gravity, 1.93. From
650 to 700 pounds of fire clay are required to lay 1000 bricks. The
clay should be used as a thin paste and the joints made as thin as
possible.
Fire Clays 237
Analysis of Fire Clays
New Jersey Clays: Per cent
Silica 56 . 80
Alumina 30 . 08
Peroxide of iron i . 12
Titanic acid i • iS
Potash o . 80
Water and organic matter 10. 50
100.4s
Pennsylvania Clays:
Silica 44-395
Alumina 33-558
Lime trace
Peroxide of iron i . 080
Magnesia o. io8
Alkalies o. 247
Titanic acid i . 530
Water and organic matter 14-575
95-493
Stourbridge Clays:
Silica 40 . 00
Alumina 37- 00
Magnesia 2 . 00
Potash 9 . 00
Water 12. 00
100.00
Stourbridge Clays:
Silica 70 . 00
Alumina 26.60
Oxide of iron 2 . 00
Lime i . 00
Magnesia trace
100.00
Fire brick should have a light buff color and when broken present an
imiform shade throughout the fracture. Bricks weighing over 7 to 7.5
pounds each contain too large a percentage of iron.
Useful Information
Velocity of light is 185,844 miles per second.
Velocity of sound at 60° F. is 11 20 feet per second.
The semiaxis of the earth at the poles is 3949.555 miles.
The terrestrial radius at 45° latitude is equal to 3936.245 miles.
Radius of a sphere equal to that of the earth is 3958.412 miles.
Quadrant of the equator is equal to 6224.413 miles.
238
Useful Information
Quudrani of llic meridian 6214.413 miles.
One (icK'rcc of the Icrrcslriai meridian is 69.049 miles.
One degree of longitude on the e(|uator equals 69.164 miles.
.\ degree of longitude upon i)arailel 45 c(|uals 48.988 miles.
A nautical mile e(|uals 1.153 statute miles and is equal to one minute
of longitude uiK)n the ec|uator.
Length of a pendulum Ijeating seconds in vacuum at sea level al New
York is 39.1012 inches.
Length of a pendulum beating seconds in vacuum at the equator is
39.01817 inches.
Mean distance of the earth from the sun is 95,364,768 miles.
Time occupied in transmission of light from the sun to the earth is
8 minutes, 13.2 seconds.
Force Required to Pull Nails from Various Woods
Kind of wood
White pine .
Yellow pine.
White oak.
Chestnut..
Laurel ....
Size of
nail
8d
9d
2od
sod
6od
8d
10 d
sod
6od
8d
20 d
6od
sod
6od
9d
20 d
Holding-power per square inch
of surface in wood, pounds
Wire nail Cut nail
167
318
940
6si
450
455
477
347
363
340
69s
755
596
604
1340
1292
1018
664
1179
1221
Mean
662
1216
683
Trautwine gives the holding power of 6 d nail driven one inch into oak as 507 pounds;
beech, 667 pounds; elm, 327 pounds; pine (whito), 187 pounds; ?6 inch square spikf
driven 4'/^ inches into yellow pine, 2000 pounds; oak, 4000 pounds; locust, 6000
pounds; I'i inch square spike in yellow pine. 3000 pounds; 9)6 square spike six inches
in yellow pine, 4873 pounds. In all cases the nails or spikes were driven across the
grain. When driven with the grain the resistance is about one half.
Weights per Cubic Inch of Metals
239
Weights per Cubic Inch of Metals
Lbs.
Cast iron o. 263
Wrought iron o. 281
Cast steel o. 283
Copper 0.3225
Brass o-3037
Zinc 0.26
Lead 0.4103
Mercury o . 4908
Temperatures Corresponding to Various Colors
(Taylor & White.)
Color
Dark blood red, black red
Dark red, blood red, low red
Dark cherry red
Medium cherry red
Cherry, full red
Light cherry red, bright cherry red
Scaling heat,* light red
Salmon, orange, free scaling heat . .
Light salmon, light orange
Yellow
Light yellow
White
Temperature,
degrees F.
990
1050
1 175
1250
1375
ISSO
1650
172s
182s
1975
2200
* Heat at which scale forms and adheres, i.e., does not fall away from the piece
when allowed to cool in air.
240
Useful Information
Iron Ores
Iron is usually found as an ore in one of the following classifications,
oxides, carbonates and sulphides.
The following table gives the subdivisions of these classes and an idea
of the general composition and character of the different varieties.
Oxides
Carbonates
Sulphides
Component
parts
Anhy-
drous:
Red
hematite
Hy-
d rated:
Brown
hematite
Magnetic
30-70
I5-5S
0- I
0- 2
O-IO
0- 5
0-2S
0- 5
0- 2
0- 2
0- 5
Includes:
f rank-
Unite or
spiegel-
eisenand
load
stone.
o-so
20-60
1-25
O-IO
0- 5
0-2S
0- 5
35-40
Usually
absent
0- 5
Clay
iron
stone
O-IO
.V-4S
0- 2
I -10
I-IO
I-IO
2-25
20-3S
0- 3
0- 2
0- 4
Black-
band
Pyrites
S0-90
Usually
absent
0- 2
0- 2
I-IO
0- 5
1-30
0- 5
0- 3
0- I
S-20
Includes:
bog iron
ore, lake
ore and
limonite
44 28
Ferric oxide
Ferrous oxides
Manganese oxide . . .
60-95
0- 5
0- 2
0- I
0- 5
0-3
I-2S
0- 2
0- 3
0- I
0- S
1. 18
3.34
Carbon dioxide
Phosphoric anhy-
dride.
4907
Water
2.75
.38
Zinc
.22
Includes:
specular
micace-
ous and
kidney
ores.
CHAPTER VIII
IRON
Physical Properties
Atomic weight 55.9
Specific gravity 7 . 80
Specific heat o.ii
Melting point 2600° F.
Coefficient of Hnear expansion o. 0000065 per 0° F.
Thermal conductivity 11. 9 Silver 100
Electric " 8.34 Mercury i
Latent heat of fusion 88 B.t.u.
Pure iron is termed ferrite.
In the presence of manganese, chromium, etc., hard carbides (double
carbides) are formed, known as cementite.
A mixture of ferrite and cementite is called pearlite.
PearUte often consists of alternate layers of ferrite and cementite and
in this condition, from its peculiar iridescence, is termed pearlite.
As carbon increases, ferrite is replaced by pearlite.
Pearlite is not found in hardened steels.
In steels saturated with carbon, a point fixed by Professor Arnold as
.89 per cent carbon, the whole structure is represented by pearlite.
Steels containing less than .89 per cent carbon are known as unsatu-
rated; those having over .89 per cent carbon as supersaturated. These
degrees refer distinctly to iron-carbon steels; for the double carbides the
point of saturation is slightly lowered.
Cementite is a hard and brittle compound, but when interspersed with
ferrite in the form of pearlite, its brittleness is somewhat neutralized by
the adjacent ferrite.
A steel containing well laminated pearlite possesses high ductility
but less tenacity than when found unsegregated.
Pig Iron
Pig iron contains from 92 to 96 per cent metallic iron; the remainder
is mostly composed of silicon, sulphur, phosphorus and manganese in
greatly varying amounts. Cobalt, copper, chromium, aluminum, nickel,
sodium, titanium and tungsten appear in some brands in minute quan-
tities.
241
242 Iron
Specific gravity of cast irf)n is variously given at 7.08, 7.15 and 7.40.
Atomic weight of iron, 55.84.
Specific heat from 32° to 212° F., 0.129 Bystrom.
" " " " at 572° !•'., 0.1407 "
" " " " at 2150° r., 0.190 Oberhoffer.
Latent heat of fusion, 88 B.l.u.*
Total heat in melted iron, 450 B.t.u.
Critical temperature, 1382° F., StupakofT.
Coeflicienl of linear expansion for 32° F., 0.000006.
" " " " at 1400° F., 0.0000 1 00.
Weight per cubic foot, 450 pounds.
Weight per cubic inch, 0.2604 pounds.
3.84 cubic inches, i pound.
Grading Pig Iron
The usual practice of furnaces has l>een to grade by fracture.
The grades are designated, Nos. i, 2, 3, 4 or gray forge; mottled and
white.
No. I. — Soft; open grain; dark in color. Used for thin, light
castings. Does not possess much strength; has great softening
properties; is mixed advantageously with harder grades; carries large
percentage of scrap.
No. 2. — Harder, closer, stronger and color somewhat lighter than No. i .
No. 3. — Harder, closer, stronger and lighter in color than No. 2;
and inclines to gray.
No. 4 (Gray forge). — Hard, strong, fine grained and light gray color.
Mottled. — Hard, verj' strong and close grained. Color presents mot-
tled or imperfectly mingled gray and white colors.
U7///e. — Hard and brittle, breaks easily under sledge but has high
tensile strength; color white.
No. I iron running in the spout of the cupola displays few sparks.
In the ladle its surface is lively and broken, sometimes flowery.
Nos. 2 and 3 present similar appearances but less marked.
Hard irons running from the cupola throw out innumerable sparks;
in the ladle the surface is dull and unbroken; if disturbed the reaction
is sluggish.
One cannot safely be guided by the appearance of the fracture of the
pig; as when melted it may produce a casting of an entirely different
character than that indicated.
• Harker and Oberhoffer have found that the specific heat of iron increases in
about the same ratio up to within the region of the critical point (1382° F.). After
this it remains practically constant.
Grading Pig Iron
243
This method of grading is entirely unreliable as to chemical constit-
uents (and physical characteristics) ; the degree of coarseness of fracture,
which affects the grade more than any other property, may be due
entirely to the rate of cooling.
Two pigs from the same cast may produce two grades; pigs from
different beds of the same cast may vary as much as i per cent in silicon
and .05 in sulphur.
The character of pig iron is often greatly affected by the accidents of
the furnace.
Irons produced from the same furnace at different times, from identical
mixtures, may differ greatly in their constituents, by reason of different
thermal conditions existing in the furnace at the time the ores were
melted.
Grading by fracture is so unreliable that most foundrymen specify the
characteristics required.
The following specifications are from Mr. W. G. Scott of the
J. I. Case Threshing Machine Co., Racine, Wis.
No.
Si,
not less
than
s,
not over
P,
not over
Mn,
not less
Total
carbon
2.50
1.95
1.35
.03
.04
.05
.60
.70
.80
• 50
.70
90
Below these figures for silicon, or .005 above for sulphur means re-
jection.
Special pig irons
Silver gray
Ferro-silicon
Manganese
pig
3.00 to 5 SO
.04
.90
.30
2.50
7.00 to 12.50
.04
Over 2.50
.04
.70
.goto 2.50
In calling for charcoal irons, silicon is asked for from .30 to 2.75;
sulphur not over .025; phosphorus not over .250; manganese not over
.70; carbon with range of from 2.50 to 4.50.
Phosphoric pig irons, for small thin castings, silicon not under 1.50;
phosphorus not under i.oo; sulphur not over .055; manganese from .30
to .90; carbon not under 3.00.
244
Iron
Duscd on a sliding scale for silicon and sulphur and a minimum (or carbon. ( Mar-
shall.)
No. I Foundry Pig Iron
Carbon content
Total carbon over 3.20
Graphitic carbon over 2.7s <
An increase of .lo silicon for every .003 sulphur.
.Silicon with sulphur
1.70
.010
1.80
.013
1.90
.016
2.00
.019
2.10
.02a
2.20
.oas
2.30
.038
2.40
.031
2. SO
.034
2.60
.037
2.70
.040
2.80
043
2.90
.046
3.00
.050
No. 2 Foundry Pig Iron
Silicon with sulphur
1.20
.005
to
to
2.20
.055
Carbon content
Total carbon over 3 00
Graphitic carbon over 2 . so ■
An increase of .10 silicon for every .005 sulphur.
Silicon with sulphur
1.20
.cos
1 30
.010
1.40
.015
ISO
.oao
1.60
.02s
1.70
.030
1.80
.03s
1.90
.040
2.00
.045
2.10
.oso
3.20
•OSS
Foundry Pig Iron
No. 3 Foundry Pig Iron
245
Silicon with sulphur
.70
.005
to
to
1.70
.055
Carbon content
Total carbon over 2 . 75
Graphitic carbon over 2.00 -^
An increase of . 10 silicon for every .005 sulphur.
Silicon with sulphur
.70
.005
80
.010
90
•CIS
00
.020
10
.02s
20
.030
30
.035
40
.040
so
• 045
60
.050
70
■05s
No. 4 Foundry Pig Iron — (Gray Forge)
Silicon with sulphur
.50
.025
to
to
1.50
• 07S
Carbon content
Silicon with sulphur
Total carbon over 2.00
Graphitic carbon over i . 25 •'
An increase of .10 silicon for every .005 sulphur.
246
Iron
The wide variation in silicon and sulphur which may occur in irons
graded by fracture is shown in the Transactions of the American Foundry-
mcn's /Vssocialion, Cleveland Convention; wherein appears a statement
as to the ran^e of those elements, in the same grades of iron, made by
. the same furnace.
No. I X varies in silicon from 1.13 to 3.40 per tent.
" " " sulphur " 0.013 to 0.053 per cent.
No. ;! X " " silicon " 0.67 to 3.30 per cent.
" " " sulphur " o.oi to 0.049 P*^"" cent.
No. 3 Plain " " silicon " 1.05 to 3.21 per cent.
" " " sul|)hur " o.oi to 0.069 per cent
After long consideration, a committee of the .\merican Foundrymen's
Association, appointed to suggest a uniform system of grading, submitted
the following report, which was adopted at the Cincinnati Convention,
May, 1909.
AMERICAN FOUNDRYMEN'S ASSOCIATION
Standard Specifications for Foundry Pig Iron
Adopted by tlie American Foutidry men's Association in Convention,
Cincinnati, May 20, igog.
It is recommended that foundry pig iron be bought by analysis, and
that when so bought these standard specifications be used.
Percentages and Variations
In order that there may be uniformity in quotations, the following
percentages and variations shall be used. (These specifications do nc^t
advise that all five elements be specified in all contracts for pig iron, but
do recommend that when these elements are specified that the following
percentages be used.)
Silicon
Sulphur
Total carbon
(.25 allowed either way)
(maximum)
(minimum)
1 .00 (La) Code.
0.04
(Sa) Code.
3.00 (Ca) Code.
I. so (Lc)
0.0s
(Se)
3.20 (Ce)
2.00 (Li)
0.06
(Si)
3-40 (Ci)
J. SO (Lo)
0.07
(So)
3.60 (Co)
3.00 (Lu)
0.08
(Su)
3.80 (Cu)
0.09
(Sy)
O.IO
(Sh)
Standard Specifications for Foundry Pig Iron
247
Manganese
Phosphorus
(.20 either way)
(.ISO either way)
.20 (Ma) Code.
.20 (Pa) Code.
.40 (Me)
.40 (Pe)
.60 (Mi)
.60 (Pi)
.80 (Mo)
.80 (Po)
1.00 (Mu)
1. 00 (Pu)
1. 25 (My)
1. 25 (Py)
I. SO (Mh)
I. so (Ph)
Percentages of any element specified half way between the above shall
be designated by addition of letter "X" to next lower symbol.
In case of phosphorus and manganese, the percentages may be used
as maximum or minimum figures, but unless so specified they will be
considered to include the variation above given.
Sampling and Analysis
Each car load, or its equivalent, shall be considered as a unit in
sampling.
One pig of machine-cast, or one-half pig of sand-cast iron shall be taken
to every four tons in the car, and shall be so chosen from different parts
of the car, as to represent as nearly as possible the average quality of the
iron.
An equal weight of the drilUngs from each pig shall be thoroughly mixed
to make up the sample for analysis.
In case of dispute, the sample and analysis shall be made by an inde-
pendent chemist, mutually agreed upon, if practicable, at the time the
contract is made.
It is recommended that the standard methods of the American
Foundrymen's Association be used for analysis. Gravimetric methods
shall be used for sulphur analysis, unless otherwise specified in the
contract.
The cost of the resampling and reanalysis shall be borne by the party
Base or Quoting Price
The accompanying table may be filled out and may become a part of
the contract: "B," or base, represents the price agreed upon for a pig
iron running 2.00 in silicon (with allowed variation 0.25 either way), and
under 0.05 sulphur. "C" is a constant differential to be determined
upon at the time the contract is made.
248
Iron
Silicon percentages allow .2S variation cither way. Sulphur percentages are maxi-
inuiii.
B+6C
< 00
13 + 5 <
B+4C
B + jC
Sulphur— .04
B + 2C
Sulphur — .OS
B+sC
B + 4 ( ■
B + 3C
B + 2C
B + C
Sulphur — .06
B4-4C
B + V-
M i . (■
n-i-r
B
Sulphur — .07
B+3C
B + --
B-C
Sulphur — .08
B + 2C
B + (
B-2C
Sulphur — .09
B + C
B
15 - r
n - J c
B-3C
Sulphur — .10
B
B-C
B-2r
D-3C
B-4C
Silicon
2.00
I -75
I. so
1 -'S
I 00
Sulphur — .04
B + C
B
B-C
B-2C
B-aC
Sulphur — .05
Base
B-C
B-2C
B-3C
B-4C
Sulphur — .06
B-C
B-2C
B-3C
B-4C
B-sC
Sulphur — .07
B-2C
B-3C
B-4C
B-sC
B-6C
Sulphur — .08
B-3C
B-4C
B-sC
B-6C
B-7C
Sulphur — .09
B-4C
B-sC
B-6C
B-7C
B-8C
Sulphur — .10
B-sC
B-6C
B-7C
B-8C
B-9C
(This table is for settling any differences which may arise in filling a
contract, as explained under Penalties and Allowances, and may be used
to regulate the price of a grade of pig iron which the purchaser desires,
and the seller agrees to substitute for the one originally specified.)
Penalties
In case the iron, when delivered, does not conform to the specifications,
the buyer shall have the option of either refusing the iron, or accepting
it on the basis as shown in the table, which must be filled out at the time
the contract is made.
Allowances
In case the furnace cannot for any good reason deliver the iron as
specified, the purchaser may at his option accept any other analysis
which the furnace can deliver. The price to be determined by the Base
Table herewith, which must be filled in at the time the contract is made.
Machine- Cast Pig Iron
Pig iron is usually cast in sand beds. The casting machine has of late
years been adopted by some furnaces and the statement is made that
machine-cast pig, aside from the freedom from sand, possesses other
important advantages. That it is more uniform in character; affords
Machine-Cast Pig Iron
249
greater certainty as to its chemical composition; is cleaner and melts
more readily.
Machine-cast pig presents a closer grain and is harder than iron cast
in sand, by reason of the greater percentage of combined carbon.
Upon remelting, this difference disappears and the castings show the
same analysis.
Mr. A. L. Colby, chemist of the Bethlehem Iron Co., gives the follow-
ing statement regarding an experiment, made to determine the influence
of the mould upon pig iron.
"One half of a cast was poured into sand moulds and the other half
into iron. Equal quantities of drillings from six pigs, selected from
different parts of that portion of the cast which had been cast in sand
were taken; and similar drillings were obtained from that portion of the
cast which had been taken to the casting machine; and each was care-
fully analyzed, with the following results:
Cast No. 7602
Silicon
Manganese
Phosphorus
Sulphur
Total carbon
Combined carbon
Graphitic carbon
Tensile strength per square inch
Sand-cast,
Machine-
cast,
per cent
per cent
3.00
2.99
■ 95
95
• 770
773
.041
041
3.460
3
380
.250
920
3 210
2
460
15,000
41
.000
"The high tensile strength of the machine-cast iron is due almost
entirely to the higher percentage of its combined carbon. Some of the
sand-cast portion of this cast, and some of the machine-cast portion were
melted separately in the same cupola, keeping all smelting conditions
as nearly uniform as possible; and castings from each melt were made,
which were proved by analysis, tensile strength, ability to machine and
appearance of fracture to be as nearly alike as different things, made
from the same iron, ever are."
Regarding this experiment, Mr. W. J. Keep in a communication to
"The Foundry," remarks:
"The experiment shows that a pig iron cast in iron moulds with a very
close grain and high combined carbon and the same iron cast in a sand
pig mould with open grain and low combined carbon, will each, when
remelted in a cupola, make castings exactly alike."
250
Iron
The following report on the test ingots. c;ist with the cxixrimcntal
castings, supports this statement.
Constituents
Sand-cost pig iron ingot
3)^ inches square and
I W feet long
Machine-cast pig iron
ingot 3]ri inches square
and I ^ (cct long
Cast
horizontally,
per cent
Cast
vertically.
per cent
Cast
horizontally,
percent
Cast
vertically.
per cent
Silicon
-• <.'3
.84
.766
.071
3.40
.470
2.9.50
18,000
G2 Fi
2.91 ]
.85 K;
»9S
34
Phosphorus
.769
.064
3.390
.368
3022
16,300
G2 El
077
3.364
.336
3 028
17.000
Gi Fi
764
071
3357
Combined carbon
Graphitic carbon
.357
3 100
17,000
Gi Fi
The coarse open fracture presented by some pig irons, and which under
the old system might cause them to be graded as No. i, may be due to
an excessive amount of manganese and the iron will be hard upon re-
melting. On the other hand, an iron may have a close grain, by reason
of the graphitic carbon occurring in a finely divided condition and be
graded low; when, since it is soft, it should have a much higher grading.
Charcoal Iron
Charcoal iron is graded according to fracture. The grades are desig-
nated by numbers and also as soft foimdrj'; low carbon, 2.5 per cent
total carbon; medium carbon, 3.5 per cent total carbon; and high car-
bon, 4.5 per cent carbon. Purchases are usually made on specifications.
Comparatively little charcoal iron is now used, since its valuable
properties as regards chill and strength may be imparted to coke irons
by use of the ferrometalloids and scrap steel.
Grading Scrap Iron
Machincr}' scrap should be free from burnt iron, wrought iron, steel,
plow points, brake shoes, sash weights, sleigh shoes, chilled iron, stove
l)late and fine scrap; should be broken, into pieces weighing not over
4CX) pounds.
.Approximately, scrap iron varying in thickness from V* inch to i inch,
may be compared with pig iron carrjn'ng from 1.5 per cent to 2 per cent
silicon and .oS per cent sulphur.
Grading Scrap Iron 251
From I inch to 3 inches thick, as compared with pig iron carrying from
I per cent to 1.75 per cent silicon and .08 per cent sulphur. Above 3
inches thick, with an open gray fracture, as ranging in sihcon from .75
to 2 per cent.
In white scrap, silicon is usually very low and sulphur very high.
Burnt iron is worthless except for sash weights and similar castings.
The successful grading of scrap iron can only be accomplished by
experience.
niAP'IKR IX
INFLUENCE OF THE CHEMICAL CONSTITUENTS
OF CAST IRON
Carbon
CoMBiNiiD carbon increases strength, shrinkage, chill and hTdness,
and closes the gram.
Graphitic carbon reduces strength, shrinkage, chill, hardness, and tends
to produce an open grain.
Silicon softens iron by promoting the formation of graphitic carbon.
It decreases shrinkage and strength; increases fluidity and opens the
grain.
Sulphur hardens iron, increases shrinkage and chill; causes it to set
quickly in the ladle ("lose its life"); produces blow holes, shrinkage
cracks and dirty iron.
Phosphorus weakens iron, imparts fluidity, decreases shrinkage and
lowers the melting point.
Manganese in large percentages hardens cast iron. It increases
shrinkage and chill, reduces deflection and tends to convert graphitic
into combined carbon. In small amounts by reason of its power to
remove sulphur and occluded gases, its tendency is to produce sound,
dense castings, without increased hardness or shrinkage.
To raise the strength of castings, increase manganese and reduce
silicon and phosphorus.
To soften iron, increase silicon and phosphorus.
To reduce shrinkage, increase silicon and phosphorus and reduce
sulphur.
To prevent blow holes, reduce sulphur and increase manganese.
To prevent kish (e.\cessivc amount of free carbon), increase scrap or
increase manganese.
[W. G. Scott.]
Properties of the Usual Constituents of Cast Iron
Carbon
Specific gravity (diamond) 3 . 55
(graphite) 2.35
Atomic weight 12.
252
Properties of the Usual Constituents of Cast Iron 253
Specific heat at 212° F 0.198
" " " 1800° F 0-459
" " " 3000° F 0-525
Carbon exists in cast iron as combined and graphitic.
Professor Turner recognizes two different varieties under each of the
general subdivisions, as follows:
I Coarse-grained carbon or graphite.
Fine-grained carbon, called amorphous carbon,
or temper graphite.
„ , . , f Combined carbon.
Combmed ;,,,..,, , , . , „ . ,
, J Missmg carbon, which usually occurs m rela-
carbon | .7 ,, ...
[ tively small quantities in cast iron.
The amount of carbon which may be absorbed by pure iron at high
temperatures is stated differently by different authorities.
Turner places the limit of saturation at 4.25 per cent, and cites Saniter's
experiments as follows:
"At cementation, heat about 1650° F., 2 per cent; by fusion, about
2550° F., 4.00 per cent."
Field states that pure iron at maximum temperatures absorbs 6h
per cent carbon.
Keep gives the saturation of charcoal iron when cold as 4 per cent and
that of anthracite or coke irons as 3.50 per cent to 3.75 per cent.
The saturation point varies according to the temperature.
As iron cools below the temperature of saturation, carbon separates
out in the form of graphitic carbon. At just what temperature this
separation ceases is not definitely known; it is variously stated at
1300° F., 1650° F., and as high as 1800° F.
Since the specific heat of carbon is much greater than that of iron, it
delays the rate of cooling as the temperature falls.
In a mixture containing 96 per cent of iron and 4 per cent of carbon,
the heat evolved by the carbon, during the process of cooling, retards
the rate of cooling one-seventh.
According to Field, an iron containing 6]/^ per cent carbon will dis-
solve no silicon; and one containing 23 per cent of silicon dissolves no
carbon.
Iron having 3 per cent silicon contains approximately 0.3 per cent
combined carbon.
With 2 per cent silicon the combined carbon is 0.6 per cent and with
I per cent silicon 0.9 per cent.
As the carbon separates out in cooling, it changes from combined to
graphitic, producing a softer, weaker iron and one having less shrinkage.
254 Inlliuiuc of the Chemical Const it ucn Is of Cast Iron
Tla- liital rarhon in cast iron varies from :? |>er leiil to 4>i per cent,
a\era^;iiig alioul j.4 i>er leiil.
With silicon as high as S to 10 |>cr cent, the total carbon falls to 2
per cent.
Under the same conditions, the higher the total carlxjn, the s<jfter the
iron. A \ery soft iron may contain as little as i j)er tent combined
carbon with 3.4 to 3.5 per cent graphitic.
An increase of .25 per cent total carbon produces a marked increase
in the softness, and a corres]X)nding decrease in strength and shrinkage.
Combined carbon increases as the grades grow harder.
Ordinarj' soft iron contains from .3 to .5 per cent combined carlx)n.
Strong irons carry- from .45 to .9 per cent.
The harder grades run from .6 to i per cent.
The proportion of combined to graphitic carbon is determined:
First. — By the total carbon present, as the greater the total carbon,
the greater will be the proportion of graphitic to combined carbon.
Second. — By the rate of cooling. Rapid cooling increases the com-
bined and slow cooling increases graphitic carbon.
Third. — By the temperature of the iron when it begins to cool.
The higher the temperature at which the iron is poured, the longer will
be the time elapsed in cooling and the longer the period for conversion
of combined to graphitic carbon.
Fourth. — By the amount and kind of other elements present.
Silicon decreases combined and increases graphitic carbon. With
increased silicon all the combined carbon maj' be changed to graphitic.
An increase of i per cent silicon in cast iron, other conditions remain-
ing the same, will convert from .35 to .47 per cent of combined into
graphitic carbon; and under the same circumstances an increase of
.47 per cent combined carbon will cause a corresponding decrease in
silicon.
Sulphur increases combined carbon as also does manganese.
Phosphorus prolongs the cooling and thereby alTords more time for
the separation of grajAitic carbon.
Loss or Gain of Carbon in Remelting
An iron may gain or lose carbon in passing ihrou;,'!! the cupola.
There is a tendency to loss of carbon in remelting where the carbon and
silicon are high, with hea\y blast and low percentage of fuel.
On the other hand, where the carbon and silicon are low, with low blast
and high percentage of fuel, the tendency is to gain in carbon.
Hard irons melt more readily than soft; the higher the combined
carbon, the lower the melting point.
Loss or Gain of Carbon in Remelting
255
Hard irons hold their shape in meUing. The melted iron runs from
bottom and sides of the pig freely, leaving smooth sm-faces; while
gray irons become soft and drop away in lumps presenting ragged
surfaces.
Hard irojis must be melted hotter than gray for pouring as they set
much more rapidly.
In running from the spout of the cupola and in the ladle, hard irons
throw off great quantities of sparks, and the surface of the iron in the
ladle is dull and inactive when broken; on the other hand, the soft irons
seldom emit sparks and present a lively surface in the ladle, breaking
with innumerable checks, the soft Scotch irons showing peculiar flowery
surfaces.
The diagram given below taken from the report of Prof. J. J. Porter,
"shows the range of combined carbon, which should result for each
-] — I — I — \ — I — \ — \ — \ — r
•* Dothed Lrnes are Percent^ expected on Basis
• of Theory.
Full L ines give Percent; of Combined Carbori
^obtained in Actual Castings of Thicknesses
given (Approximated)
Irons plotted are a// under I Percent Pand
- Mn and 0.10 S, and aiv Cupola Melted.
o = Total Carbon, x = Comb. Carbon.
T^c
^1^
oa-T>: 2?/^/
^°^:~ '•j'-^
ICZ
percentage of silicon (the cooling being normal, i.e., the castings being
neither chilled nor annealed). " The calculations are made on the theory
that I per cent of silicon precipitates from solution .45 per cent carbon
as graphitic carbon.
25^ Influence of the Chemical Constituents of Cast Iron
Tor specified purposes Vroi. Turner gives the following percentages of
combined carbon.
Character o( iron
• .juiwuieU
carbon
•
Extra soft siliceous gray iron
.08
Soft cast iron
Cast iron of maximum tensile strenijth
.47
Cast iron of maximum transverse strength
■ 47
Cast iron of maximum crushing strength
Over 1 .00
Silicon
Full lines show approximately the relation existing Ijetween the
thickness of section, per cent of silicon and per cent of combined carbon,
and are plotted from the actual data there given.
Atomic weight 28 . 4
Specific gravity 2 . 49
Specific heat .20 B.t.u.
Pig iron takes up its silicon in the furnace, and the amount so absorbed
depends largely upon the working temperatures.
Pure iron dissolves about 23 per cent of silicon. By means of the
electric furnace iron is made to absorb as much as 80 per cent. Those
irons containing over 20 per cent are called ferrosilicons; where the
silicon content runs from 5 to 10 per cent they are called high silicon
irons.
Iron always loses silicon in passing through the cupola, and the amount
lost depends upon three conditions.
First. — The amoimt of oxygen coming in contact with the metal in
melting; oxidation increases with the blast.
Second. — Upon the composition of the iron as it is charged into the
cupola, the loss being greater in irons having a high percentage of siUcon
than in those where the silicon content is low. An iron with 4 per cent
silicon may lose as much as 2 per cent in melting, while with one verj- low
in silicon, the loss may be inappreciable.
The afiinity of iron for silicon decreases as the latter increases, hence
the amount oxidized increases with increased silicon.
Third. — The loss of silicon varies also with the percentage of carbon
present, being greater in high than in low carbon irons.
Silicon lowers the solvent power of cast iron for carbon, thereby
reducing the amount of combined carbon and increasing the graphitic.
This influence is the more powerful with the lower percentages of
silicon; the decrease in combined carbon being particidarly rapid as
Silicon 257
the silicon rises from o to .75 per cent; then as the silicon continues to
rise, the decrease in combined carbon grows less and less.
Silicon and carbon each reduce the solubiHty of iron for the other.
The influence of silicon is sometimes rendered less apparent by that
of other variable elements.
Silicon is not of itself a softener of cast iron, nor does it, per se, lessen
shrinkage; but it produces a softening effect and reduces shrinkage by
changing combined into graphitic carbon; the amount used should be
just sufficient to force from solution the amount of carbon desired in the
free state for any particular mixture and to furnish the requisite fluidity.
For every rise of i per cent silicon in cast iron there will be a corre-
sponding drop of .45 per cent in combined carbon and vice versa.
Where iron is melted, very hot sihcon unites to some extent with
sulphur, forming a very volatile sub-sulphide of silicon, thereby re-
ducing the amount of sulphur absorbed by the iron.
By reason of its specific heat, silicon retards the cooling of iron to a
certain extent. It can be made to overcome many difficulties in castings,
and to control the quality and cost of mixtures, where scrap iron is
largely used.
An increase of .2 per cent in silicon decreases shrinkage about .01 inch
per foot.
Very high percentages of silicon decrease the fusibility of iron.
When the percentage of silicon in the casting is above 2 per cent, it has
a weakening influence.
Ferrosilicon is mixed with iron in the ladle for softening and reducing
shrinkage.
Carbide of silicon is sometimes charged with the iron in the cupola.
Regarding the use of silicon. Prof. Turner says: "That at one time
its presence in cast iron, in all proportions, was regarded as injurious;
that there was no accurate knowledge of its influence prior to 1885, when
my first paper on 'The Influence of Silicon on the Properties of Cast
Iron' was published in the 'Journal of the Chemical Society.'"
Summary of Prof. Turner's experiments in the use of silicon.
Characteristics
Per cent silicon
Cast iron yielding maximum hardness
Cast iron yielding maximum crushing strength
Cast iron yielding maximum density in mass
Cast iron yielding maximum crushing tensile and transverse
strength
Cast iron yielding maximum tensile strength
Cast iron yielding maximum softness and general working qualities
-'5^ Inllucncc ul tin (iRniicai i.'uiistitucnts of Cast Iron
The siil)j< lined (hart and table giving the cfTect of silicon on ihe proi)cr-
lies of cast iron taken from I'rof. Turner, show that the influence of
silicon is of a uniform cliaracter as respects crushing, transverse and
tensile strength.
2 3 4 5 6 7
Silicon, percent.
Fig. 73.
2 4 6
Silicon, percent.
Fig. 74.
Chart No. II, showing the hardness of the same series of test bars,
was determined by the "Sclerometer."
The hardness decreased continuously with the additions of silicon until
2.5 per cent was reached, when further additions caused an increase of
hardness.
Tlic addition of silicon to iron free from carbon increases the tensile
strength and hardness. The influence resembles that of combined car-
bon on iron or steel, but is less energetic.
Silicon
259
Effects of Silicon on the Properties of Cast Iron
■4J
Cylin-
ders
-s
a!
Modulus
of
elasticity
u
a
.s §
3
(-.
0
1""
1
0
Chemical a
nalysis
c
0
s
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2
0
c
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a
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0
0
c
0
in
S
v.,
0
0.
s
Lbs.
Lbs.
Lbs.
0
7.560
72
22,720
25,790,000
168,700
2702
1.98
.38
1.60
.19
■ 32
.14
.05
.5
7.510
52
27.580
28,670,000
204,800
3280
2.00
10
I
90
45
.33
.21
.03
I.O
7.641
42
28,490
31,180,000
207,300
3370
2.09
24
I
85
96
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7. 555
3i.i^o
23,500,00c
183,900
3498
2.21
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71
I
37
.30
.05
2.0
7.518
22
3S,i8o
23,560,000
137,300
3446
2.18
62
S6
I
96
.28
.60
.03
2.5
7.422
22
32,760
25,450,000
172,900
3534
1.87
19
68
2
51
.26
.75
.05
3.0
7.258
22
27,390
21,150,000
128,700
2850
2.23
43
80
2
96
.34
.70
.04
4.0
7.183
27
25,280
15,640,000
105,900
2543
2.01
81
20
3
92
.33
.84
■ 03
S.o
7.167
32
22,750
18,720,000
103,400
2342
2.03
6b
37
4
74
.30
• 95
.05
7.5
7.128
42
11,950
14,750,000
111,000
150S
1.86
48
38
7
33
,29
1.36
.03
10. 0
6.978
57
10,630
13,930,000
76,380
1252
1. 81
12
69
9
80
.21
1.9s
.04
* Bars one foot long, one inch square, loaded in the center.
Silicon added to hard iron affects the size of the graphite, since the
freshly precipitated graphite resulting from such addition is smaller than
that found in ordinary soft foundry irons. Consequently, the metal is
closer and stronger.
Prof. Turner favors increasing silicon in a mi.xture of cast iron by the
use of high silicon pig iron, rather than by that of ferrosilicon, as the
latter differs both in fusibility and density from the iron, rendering the
product of the mixture uncertain and irregular. "The ideal method is
for the founder to have a fairly large stock, including several kinds of
iron, each separate kind being a little too hard or a little too soft for the
general run of work, but still not very different from what is required.
By mixing these irons in suitable proportions, it is then easy to obtain
any composition which may be desired, it being assumed, of course, that
the composition of each variety is already kno\vn."
During the period from 1886 to 1888, Mr. Keep made an exhaustive
study of the influence of silicon on cast iron. The results of his researches
as summarized in "Cast Iron" are:
Silicon added to white iron changes it to gray; added to gray iron, low
in silicon, makes the mixture darker.
It is the influence of silicon, not the percentage, which produces desir-
able qualities; and that influence is indirect, acting through the carbon
which the iron contains.
j6o Inllucncc of ihc Chcmiral Conslituenls of Cast Iron
The saturation |Kjint of iron for curljon is lowered hy the addition of
silicn, as the carbon is expelled in the graphitic form and caught between
the grains of the iron prcxlucing a grayer color.
If the total carbon is high, or the combined carbon low, the amount
(if silicon required to produce a particular effect will be torresjxjndingiy
low. Similar cITecLs are produced by a small amount of silicon acting
through a prolonged perio<l, by rcas<jn of slow c<x)ling of large castings,
and by a large amount acting through a short period, as in the rapid
cooling of small castings. Hy regulating the amount of silictjn in the
mixture the state uf carbon as well as the depth of chill can be controlled.
The dilTusion of silicon is very irregular. Mr. Keep found in a number
of experiments that the average variation in diffusion was from .09 to
.24 per cent. This average increases and the diffusion is less and less
complete as the silicon increases, so that any literal determinatives of
silicon are rendered more or less approximative (as showing the per-
centage of silicon in a car load of iron) by the unequal diffusion.
As regards hardness, the addition of 2 to ^M per cent of silicon will
convert all the comliined into graphitic carbon, which it is possible to
change by the use of that clement.
Silicon in itself hardens cast iron, but the softening effect caused by
it in producing the change from combined to graphitic carbon, is such as
to result in decreased hardness, until the amount of silicon added has
reached from 2 to 3 per cent. Further additions are not advantageous.
The beneficial influence resulting from the use of silicon in cast iron is not
confined to decreased hardness. It imparts fluidity and also tends to
produce clear, smooth surfaces on the castings, by reason of the liberated
graphite, in part, interposing itself between the sand and the hot iron.
Sulphur
Atomic weight 32 .
Specific gravit)' 2 . 03
Specific heat o. 2026
Melting point 226° F.
Latent heat of fusion 16.86 B.t.u.
Weight per cubic foot 125 pounds
The sulphur in pig iron is taken up in the furnace, from the fuel and
flux. Its presence is most injurious and causes the foundr>'man more
difficulty than any other element. It makes iron hard and brittle,
increases shrinkage and chill, causes iron to congeal quickly and by
preventing the ready escape of gases, makes blow holes and pin holes.
It increases the combined carbon and reduces silicon.
Sulphur
261
When pig iron is remelted, the percentage of sulphur is always in-
creased, as it takes up from 20 to 40 per cent of the sulphur in the fuel.
Mr. J. B. Neu found in some experiments that as much as 66 per cent
of the sulphur in the fuel was absorbed by the iron in melting.
The sulphur content of the iron at each of three remeltings is given by
Mr. Percy Longmuir as follows:
First
melt
Second
melt
Third
melt
Percent sulphur
.04
.10
.20
The proportion between the total amount of sulphur present in the
fuel, to that absorbed by the iron, is dependent on three conditions.
First. — The quaUty and quantity of flux used.
Second. — The temperature of the melted iron.
Third. — The composition of the fuel and iron.
In a hot working cupola, the proper quantity of flux will remove much
of the sulphur. That present in the fuel as a sulphuretted hydrocarbon
has no appreciable effect upon the percentage retained in the melted iron.
As sulphur combines with iron at low temperatures, a hot cupola tends
to increase the amount carried away by the slag. Where the fuel contains
I per cent or over of sulphur, it may add from .04 per cent to .06 per cent
to the iron and a casting made from iron having only 2 per cent of sulphur
may, when the iron is melted with high sulphur coke, show from .06
to .08 per cent.
A slow melting cupola with low temperature favors the absorption of
sulphur.
An increase of sulphur, the other elements and the rate of coohng
remaining constant, hardens iron by increasing the combined carbon and
also causes greater shrinkage, contraction and chill.
Less change in the percentage of sulphur present is required to harden
or soften cast iron than in that of any other element.
Sulphur shortens the time that iron will remain fluid in the ladle,
"destroj's the life of the iron," and if present to a large extent, makes
the production of sound castings verj^ difficult. The molten iron is
sluggish and sets quickly, thereby enclosing escaping gases, dross, kish,
etc., which cause blow holes and dirty castings.
Where sulphur is present to any considerable extent, the iron must be
poured very hot.
Iron will absorb as much as .3 per cent sulphur with increasing fusi-
bility and decreasing fluidity.
262 Intlui'iKv of tlu- Clu-mu.il Constituents of Cast Iron
An increase ni .01 per tcril of sul|)liur lan neutralize the eflecl of from
.08 to .10 per cent silicon. In coke irons, usually, as the silicon decreases
ihc suljihur increases. To maintain a uniform degree of hardness in
castings the increase of silicon corresi)onding to successive increases of
.01 per cent sulphur should be about as follows:
Sulphur, per cent 01 .02 .03 .04 .05 .06
Silicon, per cent 2.00 2.10 2.20 2.30 2.40 2.50
Sulphur may be largely expelled from cast iron l)y the use of man-
ganese, passing olT in the slag as suljjhide of manganese; the greater the
amount of manganese present, the less sulphur will the iron absorb and,
il is possible, where the manganese is very high, for the iron to lose
sulphur in melting.
From I to 2 per cent manganese, in addition to that carried by the pig
iron, is sometimes used in the ladle, to elTect the removal of sulphur;
care must be e.xercised in this respect, however, as manganese in excess
of that taken up by the sulphur tends to harden the iron.
When the fuel does not contain more than .08 per cent sulphur and
the iron has about .5 per cent manganese, the sulphur in ordinan.- gray
irons will increase about .025 per cent in melting.
The injurious effects of sulphur are largely counteracted by the use of
phosphorus. Other elements remaining constant, an increase of .1
per cent phosphorus produces about the same results in counteracting
the effects of sulphur as does an increase of .25 per cent silicon.
By the use of phosphorus instead of silicon for this purpose, the
fluidity of the iron is greatly increased; gases, dross, etc., can come to
the surface and greater freedom from blow holes, shrink holes, etc.,
results.
Irons with high combined carbon are usually high in sulphur. Long-
muir gives the following as the result of e.xaminations of the sulphur
content for different amounts of combined carbon.
Grade
I
2
3
4
5
Mottled
White
Combined carbon
• SO
.02
2. so
.60
.02
2.30
.80
.04
1.80
1. 10
.08
1 50
1.30
.10
1.20
1.80
• IS
.70
3.00
.20
.30
The sulphur content of pig iron usually runs from .01 to .08 and some-
times higher.
Prof. J. J. Porter concludes his remarks on the effects of sulphur upon
the physical properties of cast iron as follows: "Through the formation
Phosphorus 263
in the iron sulphide of eutectic films, it causes brittleness and weak-
ness, especially to shock. Through its action on the carbon it increases
hardness and may either increase or decrease strength according as the
combined carbon is already too low or too high. It has a great tendency
to cause blow holes, especially near the upper surface of thick castings.
So marked is this effect in pig iron that high sulphur pig may nearly
always be spotted by the presence of blow holes in the top surfaces.
"Sulphur probably has a more detrimental effect on low silicon, or
chill iron, than on the ordinary foundry grades. All of these effects of
sulphur are considerably lessened by the presence of sufficient manganese
to insure its being in the form of MnS, but on the other hand, the segre-
gation of MnS may cause bad places in the casting, apparently due to
dirty iron."
The statements given above are those generally entertained as regards
the deleterious influence of sulphur. They are not, however, entirely
confirmed by the investigations of Prof. Turner and Mr. Keep. The
former remarks that: "We are still in need of exact information as to the
influence of sulphur in cast iron." After a long series of experiments to
determine the injurious effect of sulphur on cast iron, Mr. Keep con-
cludes that the presence of .05 per cent of that element will not exert any
appreciable deleterious influence, and that what little ill effect results
is corrected by a slight increase of siHcon. Such small percentage of
sulphur does not seem to influence the depth of chill, nor does there
appear to exist any relation between the sulphur content and the strength
of an ordinary casting.
"While there is no indication that sulphur is in any way beneficial, on
the other hand, evidence is lacking to show that its influence is ever any-
thing but injurious; and the suggestion arises from the records, that the
prevaiUng opinions regarding the deleterious effects of sulphur are partly
superstitious, due, largely, to laboratory experiments made under con-
ditions never met with in the foundry."
Phosphorus
Atomic weight 3100
Specific gravity i . 83
Specific heat o. 189
Melting point 112° F.
Latent heat of fusion 9 . 06 B.t.u.
Weight per cubic inch . 066
The phosphorus content in pig iron comes mostly from the ore, but
also in part from the fuel and flux.
264 Infliuncc of ihe Chemical Constituents of Cast Iron
Phosphorus weakens cast iron, lowers its melting point, imparts
fluidity, tends to soften and decreases shrinkage.
It has no direct elTect on carbon, but since it prolongs the cooling
of meilcd iron it gives more lime for graphitic carbon to separate
out.
Its influence in imparting fluidity is greater than that of any other
element, hence its presence within moderate limits (i to 1.25 per cent) is
especially desirable for light, thin castings.
After it is once taken up by the iron very little of it escapes, but its
percentage is frequently increased if it exists to any extent in the fuel
or flux used in melting.
Phosphorus largely counteracts the influence of sulphur to increase
combined carbon, shrinkage, contraction and chill. \n increase of
.1 per cent phosphorus in the iron will produce about the same physical
results in counteracting the effects of sulphur, as an increase of .2$ per
cent silicon, all other elements remaining constant.
Where over .7 per cent phosphorus is present in the iron it tends to
make the latter cold short and unless there is necessity for extreme
fluidity the phosphorus content should not exceed i per cent.
By reason of its tendency to increase fusibility, it should be kept as low
as possible in castings required to stand high temperatures.
In machinery castings containing 1.5 per cent phosphorus, the tools
are quickly heated and worn.
Where great strength is required of castings, the phosphorus content
should not exceed .02 per cent.
Where blow-holes are formed in castings, by reason of occluded gases,
phosphide of iron is frequently extruded into them in the shape of
globular masses or shot.
Ferrophosphorus may contain from 20 to 25 per cent phosphorus and
is sometimes used in the ladle where prolonged fluidity is desired.
Prof. Turner states that the presence of 0.5 phosphorus in cast iron
produces excellent results and that where fluidity and soundness are
more important than strength, from i to 1.5 per cent may be permitted;
it should not be allowed in excess of the higher limit. According to
Prof. Porter, the addition of i per cent phosphorus to iron containing
3.5 per cent carbon and 2 per cent silicon approximately:
Lowers the temperature at which freezing begins from 2200° to 2150° F.,
or 50° F.
Lowers the temperature at which freezing ends from 2165° to 1740° F.,
or 425° F.
Increases the temperature range of soUdification from 50° to 375° F.
Manganese 265
Manganese
Atomic weight 55 ■ 00
Specific gravity 8.1
Specific heat .12
Melting point 2250° F.
Latent heat of fusion
Weight per cubic foot 506 . 25 pounds
Manganese is a white metal, having a brilliant crystalline fracture.
It has a strong affinity for oxygen and sulphur, but none for iron; alloys
with iron in all proportions.
The manganese in pig iron comes from the ores. Foundry irons
contain from .2 to 2 per cent manganese.
Manganese pig from 2 to 10 per cent; spiegeleisen from 15 to 40 per
cent; ferromanganese from 50 to 90 per cent.
There is always a loss of manganese in remelting. It escapes by
volatilization; by oxidation, and if sulphur is present, by uniting with
it to a greater or less extent. The amount of loss depends on the amount
of blast and percentage of sulphur present in the fuel.
With I per cent manganese present in the iron the loss of Mn in re-
melting varies from .2 to .3 per cent.
A peculiarity of manganese is that it may impart to pig iron, or castings,
a very open grain, rendering them apparently soft, even though they are
quite hard.
It greatly afifects the capacity of iron to retain carbon; where only
.75 per cent Mn is present in the iron the carbon content may be as high
as 4 per cent.
It decreases the magnetism of cast iron and when present to the extent
of 25 per cent the magnetism disappears.
As the percentage of manganese in iron increases, that of sulphur
decreases.
On the other hand, the higher the manganese, the greater the combined
carbon.
Manganese hardens cast iron, promotes shrinkage, contraction and
chill; but by reason of its affinity for sulphur and its removal of this
element, it may produce effects precisely the opposite of those above
stated. However, if the amount of manganese is greater than that
required for the removal of the sulphur present, the excess causes the
iron to take up more carbon in combination, and hardness results.
Increasing manganese above .75 per cent, the other elements remaining
constant, causes greater contraction and chill on account of its hardening
influence. These effects may be very pronounced in light castings.
266 Inllucnrc of the Chemical Constituents of Cast Iron
On account of its strong alTinity for oxygen it tends greatly to the
removal of oxides and occluded gases, thereby preventing blow-holes.
Manganese pig iron is an ordinary iron, carrying somewhat more
manganese than the ordinary foundry irons.
It is used to raise the coml)ined carbon, to add strength U) the mixture,
to fjrcvcnl blow-holes, to give life to the iron and for the removal of kish.
I'errumanganese comes to the foundry in a fine powder. It is used in
the ladle in the proportion of about i pound to Goo pounds of iron and
acts as a puritier, driving out sulphur, softening the iron where hardness
is due to sulphur and reducing the chance of blow-holes.
WTien used in this way the iron must be very hot, as with dull iron it
does little good. It should be thoroughly incorporated with the iron
Ijy stirring. It must be used with caution, as irons with low silicon and
carbon and high manganese are hard and shrinky.
The use of manganese pig iron in the cupola gives better results, and is
less expensive than that of ferromanganese in the ladles.
It is claimed for manganese that it makes hard iron soft and soft iron
hard.
With respect to the influence of Mn upon chill, Mr. Keep's views are
at variance with those above given. He states that manganese does not
increase chill, but under certain conditions may aid in removing it.
Aluminum •
Atomic weight 27.1
Specific gravity 2 . 65
Specific heat 0.212
Melting point 1 182° F.
Latent heat of fusion 28 . 5 B.t.u.
Weight per cubic foot 165 . 6 pounds
Aluminum is a white metal, resembling silver; very soft and malleable;
has a great affinity for oxj'gen; alloys with iron to an unlimited extent.
It does not occur in pig iron, ^^'hen added to iron in the ladle it
should be thoroughly mixed by stirring.
Its influence on cast iron resembles that of silicon, in producing a
softening effect by the conversion of combined into graphitic carbon.
A white iron to which from .5 to .75 per cent of aluminum has been
added becomes gray.
Aluminum decreases shrinkage and chill, and increases fluidity. By
reason of its aflinity for oxygen it tends to prevent the formation of
blow-holes.
It closes the grain of irons high in graphitic carbon, but may render
them sluggish and dirty. When used in amounts exceeding 1.5 to 2
Titanium 267
per cent it has a weakening influence. Hard irons containing from 1.25
to 1.4 per cent combined carbon are made stronger by the addition of
aluminum. The amount of aluminum wliich may be used varies from
.25 to 1.25 per cent; its action is somewhat uncertain and its alloys with
iron are erratic at times, producing results the reverse of those anticipated.
Nickel
Atomic weight 58.7
Specific gravity 8.8
Specific heat .11
Melting point 2610° F.
Latent heat of fusion
Weight per cubic foot 550 pounds
Nickel is a white metal having a silvery color; it is highly ductile and
does not oxidize readily. Alloys with iron in all proportions. When
used in quantities varying from .5 to 5 per cent, its tendency is to
harden, render more dense and increase the tensile strength of cast iron.
In large amounts it is said to have a softening influence.
Mr. A. McWilliams found that an alloy of white Sweeds iron with 50
per cent nickel gave a soft fine gray metal, even when cast in sections
from I to 3 inches thick, in chills.
Cast iron containing from 25 to 30 per cent nickel resists corrosion.
Nickel is little used in cast iron, except where great strength is re-
quired. It imparts most valuable properties to steel.
Titanium
Atomic weight 48 . 00
Specific gravity 5.3
Specific heat
Melting point 4000° F.
Latent heat of fusion
Weight per cubic foot 330 pounds
Titanium is found in many brands of foundry and Bessemer irons,
running in percentages from a trace to i per cent. It increases the
strength of cast iron to a marked degree. An addition of from .01 to
.06 per cent titanium has shown in test bars an increase of 40 per cent
in transverse strength.
It has a strong affinity for oxygen and nitrogen.
Ferroalloys are made to contain from 10 to 30 per cent titanium.
When ferrotitanium is added to iron in the ladle, it unites with the
oxygen and nitrogen, the resulting oxides and nitrides passing oflE in the
268 Inllucncc of llu- Clumical Conslituenls of Cant Iron
slag; none of llie titanium remains in the iron, except when used in large
quantities; its elTect then is to harden the iron.
I'omicrly titanic irons were carefully avoided and it docs not appear
that fcrrotilanium has as yet been used to any great extent by foundrj'-
mcn.
Investigations by Dr. Richard Moidenke and Mr. G. A. Rossi indicate,
however, that the use of ferrotitanium promises a marked improvement
as regards strength and the removal of nitrogen and oxygen from cast
iron. Mr. Rossi found as the result of his experiments that the addition
of 4 per cent of a lo per cent ferrotitanium to cast iron increased the
transverse and tensile strength from 25 to 30 per cent.
Dr. Moidenke gives the following summary of results obtained by him.
Mixtures
Original iron
plus .05 T
" .loT
" .OS T. and carb.
" .10 '
" .15
Average
Gray
White
Tests
9
4
3
6
6
4
3100
3030
3070
2990
3190
3070
1 «-sts
Lbs.
8
ao3o
II
2400
9
2430
10
2400
10
2520
2430
Increase of strength of treated iron over original 52 per cent — 18 per cent.
From the above summary it appears that the greatest increase in
strength was found in gray iron.
With vanadium and cast iron the Doctor found results directly con-
trary to the above. He calls attention to the fact that the improve-
ment in strength is almost as marked with .05 per cent to .1 per cent
titanium as with .15 per cent, showing that any excess of titanium over
that required to produce oxidation is wasted; hence .05 per cent will
be sufticient for foundry practice.
He found that titanium reduces chill but the chill produced is very
much harder than that made in the usual way.
Titanium is of value as preventing blow-holes and producing sound
castings.
Vanadium
Atomic weight 51.2
Specific gra\'ity 5.5
Specific heat
Melting point 4300° F-
Latent heat of fusion
Weight per cubic foot 344 pounds
Vanadium
269
As a merchantable product this is obtained as ferrovanadium, con-
taining from 10 to 15 per cent vanadium.
The investigations of Dr. Richard Moldenke furnish about all that is
so far known as to the action of this element on cast iron. The follow-
ing table gives a summary of his experiments.
B
gT3
>T3
1-^
Analyses 01 test bars
0 gj
i2 J3
_o
3
(U
S
3
a -d
T3 "!
^n-^
c
g
1
0
>-d
0. "J
a
11
0
%
•d
en
(a
Q
3
hJ
tfi
^
eu
%
^
2
.2 ta s; 5
Burnt gray iron
5
3
0
.05
2.13
2.03
.094
.095
.638 35
370
2
7
1310
2220
.090
.100
70
Burnt iron, white
3
12
0
OS
• SO
.41
.146
.423
.43
.65
II
16
1440
1910
.050
OSS
33
Machinery iron, gray. Melted pig iron.
No scrap
0
2
72
065
668
S4
24
1980
■ 105
•OS
2070
• los
.10
.T. .
2200
.115
IS
2740
.130
0
OS
.05
.10
.10
.15
SO
50
50
'
S4
66
59
59
S6
33
25
36
25
27
61
66
70
75
78
1970
1980
2130
2372
2S30
2360
.100
.100
.100
.090
.120
.100
Remelted car wheels, white. No pig iron
■ 53
122
399
38 •
82
0
.60
138
374
44
85
1470
• 050
.05
2190
• 050
.10
2050
.050
.15
2264
.060
0
2790
.070
.05
.00
.45
096
423
40
36
113
3020
.060
OS
• OS
.50
.66
no
591 I
ISO
25
117
2970
.090
.10
• 45
119
414
500
31
123
2800
• 055
.10
.05
.S3
084
431
74
27
128
3030
.090
15
.42
112
417
40
45
133
2950
.070
■ IS
.SO
• 50
082
374
54
22
137
3920
• 095
SO
40
54
90
105
100
91
106
100
166
270 Inllucnce of ihc Chirnical Conslilucnls of Cast Iron
I lie vimadium alloy used conlaincd:
Nanadium 14. G7 pur cent; (.arbuii 4.36 per cent; silicon 0.18 fwr cent.
The analyses of the lest bars show much more vanadium than was
used. This is attriliutcd to errors arising from the difliculties exijcrienced
in making the experiments on too small a scale.
Dr. Moldenke ci includes: "The results shown in the tabic sjieak for
themselves, and the averages tallied ofT for each table show a remarkable
progression of values. To increase the breaking strength of a test bar
from 2000 up to 2500 for gray iron and 1500 up to 3900 for white iron,
is sufficient to warrant further investigation on the part of every foundry-
man, who has special problems in strength to master."
Thermit
Thermit is a mi.xturc of oxide of iron and aluminum, which when
ignited burns at an intense heat (resulting temperature is said to be
5400° F.) in consequence of the great affinity of aluminum for o.xygen.
This compound is made by the Goldschmidt Thermit Co.
Its use in the foundry is to raise the temperature of dull iron; to keep
the iron in risers fluid, and for the mending of broken castings. A
titanium thermit is also made by same company.
This is used for the introduction of titanium, to remove nitrogen and
oxygen, as well as for its heating eCfect. The claim is made, that cast
iron can be advantageously used in place of steel castings, if titanium
thermit is employed in connection with it. Nickel thermit is used for
the introduction of nickel.
Oxygen
Atomic weight 1 5 96
Speciflc gravity (compared to atmos-
pheric air 3 2 T. and one atmosphere) i 1 056
Weight per cubic foot 624.8 grains
No element, perhaps, causes the foundryman more trouble than
o.xygen. Iron oxidizes very rapidly at high temperatures, in presence of
air. The oxides are readily dissolved in molten iron and the gases
liberated from them in the castings are the frequent cause of cavities and
blow-holes.
Ferrous oxides, produced in the process of smelting, are found to a
greater or less extent in all pig irons. Those irons in which mill cinder
heis been largely used, often contain high percentages of dissolved
oxides.
Nitrogen 271
Frequently the ends of broken pigs present blow-holes in body of the
pig, or worm-holes toward the upper surface. These are certain indi-
cations of the presence of oxygen or sulphur and such iron should be used
carefully.
In remelting in the cupola, as the molten iron passes through the
tuyere zone, more or less oxidation occurs, especially if the bed is high
and the blast strong.
Rusty scrap (fine scrap particularly) furnishes ferrous oxides in large
amounts.
The removal of ferrous oxides may be largely effected in the cupola by
an abundance of hot slag.
Ferromanganese and aluminum are used in the ladle for same pur-
pose.
The most effective deoxidizers are the metals in the order named
below :
Titanium Aluminum
Vanadium Sodium
Magnesium Manganese
Calcium Silicon
Nitrogen
Atomic weight 14.01
Specific gravity (air i) -9713
Specific heat . 244
Weight per cubic foot 548.8 grains
Nitrogen is absorbed from the blast as a nitride, by iron in melting;
and as the metal cools, the gas is liberated.
Very little is known as to the influence of nitrogen upon cast iron; its
effect upon steel is very injurious; as little as .03 per cent causing a great
loss in tensile strength and nearly eliminating ductility. Gray pig irons
show only a trace of nitrogen from .007 to .009 per cent; in white iron
it sometimes runs as high as .035 per cent.
So far as tests have been made it does not appear that, in gray iron,
any relation exists between the quality of the iron and the nitrogen
content.
It has a remarkably strong affinity for titanium, combining with it to
form a nitride, which is insoluble in molten iron and passes off in the slag.
Ground ferrotitanium previously heated is used in the ladle for removal
of nitrogen.
Arsenic and copper are sometimes found in pig iron, but in amounts so
small that the effects produced by them are inappreciable.
272 Inllui-ncc of the Chemical Constituents of C;ist Iron
In concludinK the subject of metalloids, the statement made by Prof.
I'orter ;is to the ;ii)|)ri)ximale intlucncc of the more important ones on
combined carljon must not be omitted.
I [)cr cent silicon decreases combined carbon 45 per cent.
I per rent sulphur increases " " .... 4 . 50 |)cr cent.
I per cent mimnancse " " " 40 per cent.
I per cent phosphorus " " " 17 per cent.
CHAPTER X
MIXING IRON
The mixing of iron for the cupola is done either by fracture or by
chemical analysis.
Mixing by Fracture
The fracture of the freshly broken pig is taken as the index of its com-
position. A dark gray color, with coarse open crystalline grain indicates
a soft iron, and, as a rule, one capable of carrying a large percentage of
scrap. As the color becomes lighter and the grain closer, hardness
increases and less scrap can be used. Very hard irons are mottled or
white and are used for special work.
A broken pig may present a dark fracture with open grain, but with a
fine white streak showing at the outer edges of the fracture. Such an
iron will make hard castings, owing to the presence of too much man-
ganese.
Blow holes and worm holes indicate sulphur or ferrous oxides. Iron
showing these with frequency should be used carefully.
Segregations, much lighter in appearance than the rest of the fracture,
frequently appear. These indicate higher percentages of carbon, sulphur
or manganese at those particular spots and the iron should be used
with care.
Mixing by fracture is uncertain and is liable to produce irregular and
unsatisfactory results.
The foundryman must always proceed cautiously and can only arrive
at the results desired by careful trial. The following mixtures are taken
from West's " Foundry Practice."
Locomotive Cylinders
2600 pounds car wheel scrap.
600 pounds soft pig.
Marine and Stationary Cylifiders
50 per cent No. i charcoal.
50 per cent good machinery scrap.
33 per cent car wheel scrap.
33 per cent good machinery scrap.
33 per cent No. i soft pig.
273
274 Mixing,' Iron
Rolling Mill Rolls
50 pcT cent car wheel scrap.
25 per cent No. i charcoal.
25 per cent No. 2 charcoal.
Smtill Chilled Rolls
1300 pounds old car wheels.
100 pounds No. I charcoal.
300 jjounds steel rail butts.
Killles to Stand Red Heat
1300 pounds No. I charcoal pig.
800 pounds car wheel scrap.
700 pounds good machinery scrap.
Chilled Castings to Stand friction {no strain)
200 pounds white iron.
200 pounds plow points.
1 00 pounds No. 2 charcoal.
100 pounds car wheel scrap.
Ordinary Castings
33 per cent No. i soft pig.
67 per cent scrap.
Tliin Pulleys
66 per cent No. i soft pig.
34 per cent scrap.
Sash Weight
67 per cent scrap tin.
^:i per cent stove scrap.
The advent of the chemist into the foundry offers means to avoid
many of the uncertainties coming from the selection of irons by fracture,
and the more advanced foundrymcn are now mixing their irons by
analysis.
Mixing Iron by Analysis
This method of mixing iron is by no means entirely removed from
uncertainties. The chemist is not yet able to insure the production, from
irons of known chemical composition, of castings of defmite physical
characteristics. Analysis should be supplemented by physical tests.
-Again, while the foundryman may have correct analysis of his pig iron,
if scrap is used to any extent, especially foreign scrap, he must approxi-
mate the elements contained therein.
Mixing Iron by Analysis
275
The statements made on page 307 offer some little assistance, but, in
general, reliance must be placed on experience in this respect. Where
the scrap comes entirely from previous casts, one can readily arrive at
its constituents and much uncertainty is removed.
The qualities necessary for different grades of castings may be sum-
marized as follows:
1. Hollow Ware, Stove Plate, Sanitary Ware. — Require fluidity,
softness; must be high in silicon and phosphorus; low in combined
carbon.
2. Light Machinery Castings. — Require fluidity, softness, strength
and absence of shrinkage. Must be high in total carbon and manganese;
low in sulphur and contain less silicon and phosphorus than grade No. i.
3. Heavy Machinery Castings. — Require softness, strength and low
shrinkage. Should be lower in silicon, phosphorus and graphitic carbon
than No. 2. Higher in combined carbon and manganese; low in sulphur.
4. Castings requiring great strength should be low in silicon, graphitic
carbon, sulphur and phosphorus. Combined carbon should be about
.50 per cent; manganese .8 per cent to i.o per cent.
5. Car Wheels and Chilled Castings. — Require low silicon, phosphorus,
graphitic carbon and sulphur. High combined carbon and manganese.
6. Chilled Rolls. — Require low silicon, graphitic carbon and phos-
phorus. High combined carbon.
The following table is abstracted from "Proceedings of the American
Foundrymen's Association," Vol. X, Part II, which contains the results
of a long series of tests made by their committee to standardize test bars.
The mixtures are not given as being recommended by the committee for
the several purposes, but simply to indicate the practice of some of the
larger American foundries.
Table II
Character of work
Silicon
Sulph.
Phos.
Mang.
Graph,
carb.
Total
carb
Remarks
Ingot moulds
Dynamo frames
Light machinery
Chilled rolls
1.67
1.95
2.04
.85
.72
■97
3.19
1.96
2.49
4.19
2.32
0.91
.032
.042
.044
.070
.070
.060
.084
.081
.084
.080
.044
.218
.095
.405
• 578
.482
• 454
.301
1. 160
.522
.839
1.236
.675
.441
!o6
.00
3.43
3.08
2.99
2.99
.03
2.62
2.36
3.04
4.17
3.41
3.32
3.39
2.88
3-12
Ton heat
60
60
40
15
17
40
38
48
47
67
43
30
30
Car wheel iron
15
20
Heavy machinery . . .
Cylinder iron
Novelty iron
30
10
5
10
Sash weights .
IS
276
Mixing Iron
Table III
Automobile cylinders
Silicon
Sulph.
PhoB.
Mn.
Graph,
carb.
Total
carb.
as per cent chan ,
a. 46
.063
-m
.061
Transverse strength. 2901
At a laler period Pnjf. J. J. Porter, at the request of the .American
Foundrymen's Association, undert<x)k the investigation of the comiX)Si-
tions used for various classes of castings, with a view to formulating
standard mixtures. His report embraces cverj' variety of work and
contains tabulated analyses of several hundreds of mixtures in use.
The averages of the mi.xtures in each class of work, together with those
suggested by Prof. Porter, are subjoined.
Acid-resisting Castings
Mixture
Silicon
Sulphur
Phosphorus
Manganese
Combined
carbon
Total
carbon
Average
Suggested ....
Per cent
2.03
1.00-2.00
Per cent
033
under .05
Per cent
.42s
under .40
Per cent
1. 13
I. 00-1.50
Per cent
Percent
3.3a
3.00-3.50
Agricultural Machinery, Ordinary
Average
Suggested ....
2.33
2.00-2.50
.072
.06-08
.766
.60-. 80
.62
.60-80
• 355
3. 45
Agricultural Machinery, Very Thin
Average
Suggested ....
2.70
2.2S-2.7S
.06s
.06-.08
• 75
.70-. 90
.65
.50-. 70
.20
3 SO
Air Cylinders
Average
Suggested
1.28
I.0O-I.7S
.084
under .09
.401
.30-.S0
.69
.70-. 90
.633
3.45
3.00-3.30
Ammonia Cylinders
Average
Suggested
i.SS
I.0O-I.7S
under .095
under .70
.30-. 50
.70
3 00-3 . 30
Mixing Iron by Analysis
Annealing Boxes for Malleable Casting Work
277
Mixture Silicon
Sulphur
Phosphorus Manganese
Combined
carbon
Total
carbon
Suggested ....
Per cent
.650
Per cent
■ OS
Per cent
.10-. 20
Per cent
.20
Per cent Per cent
2.7s 2. 75
Annealing Boxes, Pots and Pans
Average . . .
Suggested .
Average. . .
Suggested .
Average . . ,
Suggested
Average . .
Suggested ,
Average . .
Suggested
Average..
Suggested
Average . .
Suggested
1.52
I. 40-1. 60
.043
under .06
.38
under .20
.69
.60-1.00
.58
3.29
low
A utomobile Castings
1.93
I 7S-2.25
.059
under .08
.52
.40-. 50
.60-.
Automobile Cylinders
2.15
1.75-2.00
.091
under .08
.643
.40-. 50
.46
.60-. 80
.45
.55-. 65
3.14
3.00-3.25
Automobile Flywheels
2.73
2.25-2.50
.058
under .07
.475
• 40-50
.62s
.50-. 70
Balls for Ball Mills
1. 00
I. 00-1.25
under .08
.30
under .20
■ 50
.60-1.0
low
low
Bed-plates
I. Sis
I.2S-I.75
.07
under .10
.535
.30-. 50
.60
.60-. 80
Bi)iders (see Agricultural Machinery)
Boiler Castings
2.38
2.00-2.50
.065
under .06
.41
under .20
.79
.60-1.00
378 Mixing Iron
Car Castings, Gray Iron (sec Brake Shoes and Car Wheck)
Mixture
Silicon
Sulphur Phosphorus Mangarusc
Combined
carbon
Total
carbon
Average
Suggested . . .
Per cent
2.03
I SO-2 25
Per cent
069
under .08
Per cent
.65
.40-60
Percent
.62
.60-80
Per cent
52
Percent
350
Car Wheels, Chilled
Average
Suggested
,642 .094
.60-. 70 .08-. 10
.38
.30-40
.44
.50-. 60
.80
.60-80
36s
3.SO-3 70
Car Wheels, Unchillcd (see Wheels)
Chemical Castings (see Acid-resisting Castings)
Chilled Castings
Average
Suggested
1.04
•7S-I.25
■ los
.40
.20-. 40
.76
.80-1.20
1.96
3 19
Chills
Average
2.07
I.7S-2.25
.073
under .07
.31
.20-40
.48
.60-1.00
■ 23
2.64
Collars and Couplings for Shafting
Average
Suggested
1.60
I 75-2.00
.04
under .08
■ 5.1
.40-. 50
• 55
.60.-80
.30
3.57
Cotton Machinery (see also Machinery Castings)
Average
Suggested
2.25
2. 00-2. 25
under .09
under .08
.70 .60 .45
.60-. 80 .60-. 80
3.4s
-
Crusher Jaws
Average
Suggested —
1. 10
.80-1.00
.127
.08-. 100
.45
.20-. 40
.92
.80-1.20
3.00
3. 125
Cutting Tools, Chilled Cast Iron
Average
Suggested
1.35
I. 00-1.25
.117
under .08
.60
.20-. 40
.54
.60-.80
.65
3 00
Mixing Iron by Analysis
Cylhiders
See Air Cylinders Ammonia Cylinders
Automobile " Gas Engine "
Hydraulic " Locomotive "
Steam Cylinders
Cylinder Bushings, Locomotive (see Locomotive Castings)
Dies for Drop Hammers
279
Mixture
Silicon
Sulphur
Phosphorus
Manganese
Combined
carbon
Total
carbon
Average
Suggested ....
Per cent
1.40
I. 25-1. so
Per cent
■075
under .07
Per cent
.25
under .20
Per cent
.55
.60-. 80
Per cent
1. 00
Per cent
3-20
low
Diamofid Polishing Wheels
Average
2.70
.063
.30
.44
1.60
2.97
Dynamo and Motor Frames, Bases and Spiders, Large
Average
Suggested
2.02s
2.00-2.50
.o6ss
under .08
• 54
.50-80
■ 49
.30-. 40
.56
.20-. 30
3.73
low
Dynamo and Motor Frames, Bases and Spiders, Small
Average
Suggested ....
2.66
2.50-3.00
.073
under .08
.73
.50-. 80
.45
.30-. 40
.30
.20-. 30
3.4s
low
Electrical Castings
Average
Suggested ....
2.30
2.00-3.00
.068
under .08
.62
■SO-. 80
.48
.30-. 40
.48
.20-. 30
3.6r
low
Eccentric Straps (see Locomotive Castings and Machinery Castings)
Engine Castings
See Bed Plates Engine Frames
Flywheels Locomotive Castings
Machinery Castings Steam Cylinders
Engine Frames (see also Machinery Castings)
Average. . .
Suggested .
I 72
I.2S-2.00
.09
under .09
.60
.60-1.00
28o
Mixing Iron
Fans and Blowers (sec Machinery Castings)
Farm Implements
Mixture
Silicon
Sulphur Phosphorus
,, Combined
Manganese ^^^^^
1
ToUl
carboo
Average
Per cent Per cent
2. OS .078
2 00-2 so .06-08
Percent
78
.S»-.8o
Percent
.455
.60-80
Percent
48
Percent
3 as
Fire Pots
2.S0
2 00-2 so
under .07
under .06
under .20 .90
under .30 60-1.00
low
Flywheels i
see also Automobile Flywheels and Machinery Castings)
1.8s
I.SO-2.2S
•09
under .08
S2S
.40-60
• SS
■ SO-. 70
Suggested
Friction Clutches
2.2s under .15
1.75-2.00 .08-. 10
under .70
under .30
under .70
.50-70
low
Furnace Castings
2.125
2.00-2.50
.0S2
under .06
.40
under .20
.51
.60-1.00
low
Gas Engine Cylinders
Average
1. 18
I. 00-1.75
.082
under .08
.46
.20-. 40
.63
.70-. 90
.93
3 23
Gears, Medium
Average
Suggested ....
1.92
1.50-2.00
• 075
under .09
.47 .576
.40-, 60 .70-. 90
.55
3.79
Gears, Small
2.72
2.00-2.50
.08
under .08
91
.50-70
.80
.60-80
Suggested
Mixing Iron by Analysis
Gears, Heavy
281
Mixture
Silicon
Sulphur
Phosphorus
Manganese
Combined
carbon
Total
carbon
Average
Suggested ....
Per cent
1.38
1.00-1..S0
Per cent
.081
.08-. 10
Per cent
•39
,30- •SO
Per cent
■59
.80-1.0
Per cent
.92
Per cent
3.33
Grate Bars
Average
2.38
2.00-2.50
.08
under 1.06
Suggested —
under .20
.60-1.0
under .30
low
Chilled Castings for Grinding Machinery
Average
Suggested ....
• 50
• 50-. 75
.200
.15-20
■ 45
.20-. 40
I 50
1.5-2.0
3.00
3.00
Gun Carriages
Average
Suggested ....
•97
I. 00-1.25
.05
under .06
.37
.20-. 30
• 46
.80-1.0
.865
2.73
low
Gun Iron
Average
Suggested
1.09
I.0O-I.2S
-OS3
under .06
.32
.20-. 30
.62
.99
.80-1.0
3.o6
Hangers for Shafting
Average
Suggested
1.60
1.50-2.00
.04
under .08
.55
.40-. 50
• 55
.60-. 80
.30
3. 57
Hardware, Light
Average
Suggested ....
2.30
2.25-2.75
.06
under .08
.74
.50-. 80
.76
.SO-. 70
.32
3.39
Heat-resisting Iron
Average
Suggested
1-95
1.25-2.50
.056
under .06
• 52
under .20
.68
.60-1.00
.46
under .30
3.46
low
282
Mixing Iron
Hollow Ware
Mixture
Silicon Sulphur iPhospboriu
Manganese
Combined
carbon
Total
Average
Per cent Per cent
a SI I JO
3.2S-3.7S under .08
Per cent Per cent
.6a .41
so- . 70 . «>- . "70
Percent
.24
Percent
3.18
Avcr.iKi-
Suggested .
Housings for Rolling Mills
I.13S
I.OO-I 25
.08s
under .08
.6s
.20-30
.7S
.80-1.0
low
low
Hydraulic Cylinders, Heavy
Average
Suggested —
I 19
.80-1.20
.084
under .10
39
.20-. 40
.82
.80-1.0
99
3 13
low
Hydraulic Cylinders, Medium
1.67
.071
375 55
.30-. SO .70-90
I 20-1.60
under .09
low
Ingot Moulds and Stools
1.43 ! 046 1 .095 .345
1.2S-1.5O; under .06 under .20 , .60-1.0
i 1
Locomotive Castings, Heavy
Average
Suggested
1 55
I. 25-1. SO
.oSi .50
under .08 .30-. so
56
.70-. 90
.60
3 so
Locomotive Castings, Ligiti
Average
Suggested
1.72s 07S
1.50-2.00 under .08
.53
.40-60
ss
.60-.80
.50
3SO
Locomotive Cylinders
Average
1.457
i.oo-iso
.084 .58 .60
.08-10 .TO- TO 80-1 0
.60
3 SO
Mixing Iron by Analysis
283
Locks and Hinges (see Hardware, Light)
Machinery Castings, Heavy
Mixture
Average . . .
Suggested .
Silicon
Per cent
1. 335
I. 00-1.50
Sulphur
Per cent
.084
under .10
Phosphorus
Per cent
■ 43
.30-50
Manganese
Per cent
.58
.80-1.0
Combined
carbon
Per cent
.33
Total
carbon
Per cent
3.21
low
Machinery Castings, Medium
Average
Suggested
1.932
1.50-2.00
.078
under .09
.61
.40-. 60
.53
.60-. 80
.47
3-33
Machinery Castings, Light
Average
Suggested ....
2.57
2.00-2.50
.069
under .08
.74
.SO-. 70
.52
.50-. 70
• 27
3.49
Machine Tool Castings (see Machinery Castings)
Motor Frames, Bases and Spiders (see Dynamo)
Molding Machines (see Machinery Castings)
Mowers (see Agricultural Castings)
Niter Pots (see Acid-resisting Castings and Heat-resisting
Castings)
Ornamental Work
Average
Suggested . . .
2.9s
2.25-2.75
.09s
under .08
.54
.50-. 70
Permanent Moulds
Average
Suggested. . .
2.085
2.00-2.25
.078
under .07
I 075
.20-. 40
.35
.60-1.0
.485
Permanent Mould Castings
2.5
1.50-3.00
3.50
under .06
under .40
Piano Plates
Average . .
Suggested.
2.00
2.00-2.25
low
under .07
.40
.40-. 60
.60
.60-.80
284
Mixing Iron
Pillow Blocks
Mixture
Silicon
Sulphur
Phosphoru-s
., 1 Combined
Manganese ^^^j^„
Tot*l
carbon
Average
SuRKcsted
Per cent
1.60
I SO-I.7S
Per cent
.04
under .08
Per cent
.55
.4»-.SO
Per cent
SS
.60-.80
Per cent
.30
Percent
3. so
Pipe
3.00
1.50-2.00
under .10
.60
.50-80
.60
.60-80
Suggested. . . .
Pipe Fittings
Average
2.36
I.7S-2.SO
.084
under .08
51
.50-80
.74
.60-80
.70
368
Pipe Fittings for Superlieated Steam Lines
Average
1. 57
1.50-1.75
.078
under .08
• 49
.20-. 40
.56
.70-90
.17
2.90
low
Piston Rings
Average
1.61
1.50-2.00
.073
under .08
• 72
.30-. 50
.45
.40-. 60
.53
low
Plow Points, Chilled
Average
I. IS
.75-1.25
.086
under .08
..30
.20-. 30
.68
.80-1.0
2.10
3.30
Printing Presses (see Machinery Casting)
Propeller Wheels
Average
Suggested....
1. 28
I. 00-1.75
low
under .10
■26 .455
.20-. 40 .60-1.0
.60
low
Pulleys, Heavy
Average
2.07
1.75-2.25
.05
under .09
.575
.50-70
575
.60-. 80
.30
3.66
Mixing Iron by Analysis
Pulleys, Light
28s
Mixture
Silicon
Sulphur
Phosphorus
Manganese
Combined
carbon
Total
carbon
Average
Suggested
Per cent
2.55
2.25-2.75
Per cent
.069
under .08
Per cent
.695
.60-. 80
Per cent
.62
•SO-. 70
Per cent
• 35
Per cent
3.48
Pumps, Hand
Average
2.52
2.00-2.25
under .08
under .08
.80
.60-. 80
.40
.50.-70
Suggested
Radiators
Average
Suggested. . . .
2.30
2.00-2.25
low
under .08
.62
.60-. 80
• 42s
.50-. 70
.425
.50- 60
3.45
Railroad Castings
Average
Suggested —
2.03
1.50-2.25
.065
under .08
.69
.40-. 60
.64
.60-. 80
.525
3.50
Retorts (see Heat-resisting Castings)
Rolls, Chilled
Average
.73
.60-. 80
.055
.06-. 08
• 534
.20-. 40
.74
I. 0-1.2
1.75
3.12
3.00-3.23
Rolls, Unchilled {Sand Cast)
Average
.75
.03
.25
.66
1.20
4.10
Scales
1.83
2.00-2.30
I. OS
.60-1.0
1.43
under .08
Slag Car Castings
Average
Suggested ....
1.88
1.75-2.0
.058
under .07
.67
under .30
• 79
.70-. 90
.56
3.6!J
286
Mixing Iron
Smoke Stacks, Locomotive (sec Locomotive Castings)
Soil Pipe and Fittings
Mixture
Silicon
Sulphur
Phosphorus
Per cent
1.00
.50-. 80
Manganese
Combined
carbon
Total
carbon
Average
Suggested —
Per cent
3.0O
I. 75-2 -25
Per cent
.060
under .09
Percent
.60
.60-80
Per cent
Percent
Steam Cylinders, Heavy
Average
Suggested
1.20
I.0O-I.2S
.091
under . 10
.36
.20-. 40
.50
.80-1.0
.81
3.3s
low
Steam Cylinders, Medium
Average
Suggested —
1.658
I. 25-1. 75
.082
under .09
.30-. so
61 .62 3.43
■^■^ 1
Steam Chests (see Locomotive Castings
Stove Plate
and Machiner>' Castings)
Average
Suggested
2.77
2.25-2.75
.076
under oS
.82
.60-. 90
• 59
.60-80
.28
3.33
Valves, Large
Average
Suggested
1.34
.095
.43
.20-40
.64
.80-1.0
Valves, Sfnall
Average
Suggested
1.96
1.75-2.25
.067
under .08
.585
.30-. 50
.70s
.60-.80
1. 16
4.18
low
Valve Bushings (see Loconioti\-e Casting
Water Heaters
5 and Machineo' Castings)
Average
Suggested
2. IS
2.00-2.25
.050
under .08
.40
.30-50
.50
.60-80
Mixing Iron by Analysis
287
Weaving Machinery (see Machinery Castings)
Wheels, Large
Mixture
Silicon
Sulphur
Phosphorus
Manganese
Combined
carbon
Total
carbon
Average
Suggested
Per cent
2.10
1.50-2.00
Per cent
.04
under .09
Per cent
.40
.30-. 40
Per cent
.70
.60-.80
Per cent
Per cent
Wheels, Small
I. 8s .0665
1.75-2.00 under .08
.50
.40-. 50
• 45
.50-. 70
Suggested
Wheel Centers (see Locomotive Castings)
White Iron Castings
Average.
2.90
Wood Working Machinery (see Machinery Castings)
Brake Shoes
Average
Suggested. . .
1.94
I . 40-1 . 90
.125
.08-. 10
.67s
.556
.50-. 70
3.16
low
Knowing the desired analysis for any class of casting to be made, the
simplest way to arrive at the amounts of the different irons to be used
is by percentage. For example, let the requirements be for an iron to
produce machinery castings of which the analysis shall be :
Silicon
Sulphur
Phosphorus
Manganese
2.00
.084
.350
.625
As previously stated, the loss in silicon in remelting will be from 10
to 20 per cent, the same for manganese, and a gain of .03 in sulphur,
phosphorus remaining constant. The mixture then must contain:
Silicon
Sulphur
Phosphorus
Manganese
2.22
.054
• 350
.687
s88 Mixing Iron
The irons then availaliie arc:
No. 2 Southern
No. 3 Northern
Silver gray
Scrap
Silicon
4.20
1.90
Sulphur
02s
.080
Phosphorus
280
3SO
.830
.284
Manganete
735
940
820
S40
After two or three trials it is found that the desired mi.xture may be
obtamed from
Silicon
Sulphur
Phosphorus
Manganese
ao per cent No. 2 Southern, giving
20 per cent No. 2 Northern, giving
10 per cent silver gray, giving . . .
• 45°
.420
420
.950
2.240
.008
004
.0025
.0400
■ 054S
.056
.070
.082
142
.350
147
188
082
.687
Example 2. — Required an iron for pulleys and light castings of
following analysis: Silicon, 2.40; sulphur, .09; phosphorus, .700;
manganese, .52, and to carr>' 50 per cent scrap.
Avaflable irons:
No. 2 Southern
No. 2 Northern
Silver gray
Scrap
Silicon
2.72
2.40
s-oo
2.20
Sulphur
.070
.020
.024
.080
Phosphorus
Manganese
.750
.48
.600
56
.960
S3
.660
62
Correcting for losses of silicon and manganese and gain of sulphur the
mixtiffe must contain silicon, 2.66, sulphur, .06, phosphorus, .70, man-
ganese, .577.
For reasons of economy no more than 10 per cent of the silver gray
iron should be used. This with the 50 per cent scrap supplies:
10 per cent silver gray
50 per cent scrap
To be supplied by remaining pig
iron
Silicon
■ SO
1. 10
iTfo
1.066
Sulphiu"
.0024
.040
.0424
.0176
Phosphorus
.096
■ 330
.426
Manganese
.053
■ 310
.363
Mixing Iron by Analysis
289
By txial it is found that the remaining amounts of the different elements
may be obtained by using:
Silicon
Sulphur
Phosphorus
Manganese
25 per cent No. 2 Southern
IS per cent No. 2 Northern
Giving
.68
1.04
.0175
.0030
.0205
.1875
.0900
.2775
.13
.084
.204
The slight discrepancies of .02 silicon, .0029 sulphur, .0035 phosphorus
and .01 manganese may be neglected.
Where the scrap is very nearly of uniform quality, the analysis of the
castings from any given heat furnishes data from which a very close
approximation can be made of the scrap used in the previous heat.
Assuming such character of scrap, and knowing the mixture used in
any heat as well as the analysis of the castings, compute the analysis of
scrap used in previous heat.
Let the castings show the analysis of example 2, viz.: Si, 2.40, S, .09,
P, .70, Mn, .52. Then the] mixture must have been as before. Si, 2.66,
S, .06, P, .70, Mn, .577.
The irons having the assumed analysis of example 2, then:
25 per cent No. 2 Southern gives.
IS per cent No. 2 Northern gives.
10 per cent silver gray gives
Which subtracted from the mix-
ture leaves
Silicon Sulphur Phosphorus Manganese
.36
■ 50
1-54
1. 12
.0175
.0030
.0024
.0229
.0371
.1875
.0900
.0960
.3735
.3265
.084
053
.257
As 50 per cent scrap was used, the analysis of scrap from previous heat
is Si, 2.24, S, .0742, P, .653, Mn, .64, giving a very close approxima-
tion.
CHAPTER XT
USE OF STEEL SCRAP IN MIXTURES OF CAST IRON
Steix scrap, when added to mixtures of cast iron in quantities varying
from lo to 40 per cent, closes the grain, increases the toughness and adds
greatly to the tensile strength of the castings made from such mixture.
The steel should be low in carbon, such as boiler i)lalc scrap, machine
steel, rail ends, etc.
Turnings from machine steel are frequently used in the ladle. In this
case the steel should be heated quite hot, placed in the ladle and the iron
tapped out on it. The mixture should be thoroughly stirred until the
steel is melted. In aU cases the iron must be very hot.
Mixing steel in the ladle does not give as satisfactory results as mixing
in the cupola.
.\s the steel is low in carbon the iron used should be high in total carbon,
otherwise the castings will be hard with over 10 per cent steel scrap.
The following table by Mr. 11. E. Diller presents the results of a scries
of tests, with mixtures made by varying in percentages of steel scrap from
I2V4 to 37!^ per cent:
No.
Sili-
con
Sul- I
phur
'hos-
hor- \
us ga
lan-
nese
Comb,
carbon
Graph-
itic
carbon
Total
carbon
Tensile
strength
Trans-
verse
strength
Per
cent
steel
I
I 43
.047
564
82
.670
3.14
3.81
23,060
25SO
0
2
I. SO
.065
532
33
.640
3 44
3
08
30.500
2840
2S
3
1.76
.062
488
53
510
3.12
3
63
22.180
2440
0
4
1.76
• 139
515
57
.430
2.94
3
37
37.090
2770 •
I2'i
S
1.77
.069
339
49
.560
2.87
3
43
32.500
3120
124
6
1.83
.100
610
55
510
2.44
2
9S
36.860
3280
25
7
1.75
.089
598
35
.740
2 12
2
86
30,160
3130
31^i
8
1.96
.104
446
44
.630
3.18
3
81
21 ,950
2230
0
9
2.12
.037
410
26
.380
326
3
64
21,890
3470
124
10
2.16
.060
31S
20
1.060
2.30
3
36
26,310
2670
124
II
I 97
.093
470
48
.S70
283
3
40
32,.S3o
3050
37I4
12
2. 35
.061
51S
56
.540
3 40
3
94
21.990
2200
0
13
2.53
.104
490
54
.600
2S6
3
16
33..390
2850
2S
14
2.36
.064
327
24
1.080
2. IS
3
23
31.560
3200
35
These tests were made with pig iron, ferrosilicon and steel scrap. No
cast iron scrap was used. Mr. Diller concludes: "The tests given seem
290
Recovering and Melting Shot Iron
2gi
to indicate that 25 per cent of steel will add 50 per cent to the strength of
the iron, and i2>^ per cent of steel, approximately 25 per cent."
The tests containing 37'/^ per cent steel were hardly as much im-
proved in strength as those with 25 per cent of steel; from which we may
infer that the limit of the amount of steel it is beneficial to melt with
iron in a cupola is between 25 and 371^ per cent.
Results of experiments made by Mr. C. B. McGahey are embodied
below.
Mr. McGahey used test bars i in. by i in. by 24 in. (distance between
supports not stated).
No.
Sili-
con
Sul-
phur
Phos-
phor-
us
Man-
ganese
Per
cent
steel
Depth
of
chill
Trans-
verse
strength
Remarks
I
2
3
4
.82
.88
.58
■ 79
.097
.081
.097
.o8i
.23
.24
.25
.239
• 54
.67
• 44
• 64
7
20
23
21.50
In.
• 38
.40
• 48
1800
2200
2250
Entirely gray when
cast in sand.
Depth of chill ?4 in.
Steel scrap (struc-
tural shapes).
"I find that to get the strongest bars I have to keep pretty close to
these analyses and have made my strongest bar at 2350 pounds with
.55 inch deflection. The iron had a fine grain, was low in graphite, but
machined nicely.
When ferromanganese was used, about i per cent was found to be
best. The above resulting compositions (the silicons of the mixtures
being calculated to bring them about right) are intended for castings
ranging from i inch to 2H inches in section.
Should heavier work be required it is better to run the silicon in the
pig up to 2.75 and manganese up to 2.00 and use $3^^ per cent of steel
scrap."
An addition of 10 per cent steel scrap to mixtures for engine cylinders
gives excellent results affording a close-grained tough iron. Steel scrap
increases shrinkage and causes the iron to set quickly; hence the irons
used should be high in total carbon and must be melted and poured very
hot.
Steel scrap promotes chill and is largely used with coke irons in making
car wheels, obviating the use of the expensive charcoal mixtures.
The charges containing steel should be melted during the first part
of the heat, and in each charge the steel should precede the iron.
Recovering and Melting Shot Iron
The shot from gangways and cupola bottom is usually recovered by
riddling the gangway sand; picking over the dump and by grinding the
2Q2 Use of Steel Scrap in Mixtures of Cast Iron
hollnm in the i indcr mill. Tliis is also done by magnetic or hydraulic
sci)aratt>rs. The amount recovered by machines is much greater than
that obtainecl by hand.
After charging of the cujxila is completed, the shot should Ijc thrown
on toil of the last charge, using with it some of the coke picked from the
(lumj). Kach heat should take care of the shot from the previous one.
The melted iron coming from the shot can be poured into grate bars,
sash weights, or other coarse castings; or it may fjc run into pigs and
used as scrap.
Mr. \V. J. Keep describes his method of recovery as f(;llows: "After
the blast has been shut ofT and all of the melted iron has been drained
from the cupola, make a dam on the floor in front of the cupola spout
about 4 inches high, enclosing a semicircular space, having a radius of
about 4 fe«t. Let the melter lay a tapping bar across the spout and have
three or four laborers with a piece of old iVi inch shafting about 8 feet
l<jng ram in the breast. If the bottom and spout have been made right
there will be no melted iron in the cupola, but ram back and forth to
allow all to drain out.
All the liquid slag in the cupola will run into the enclosed space
underneath the spout and if there is any iron in this, it will run through
the slag and lie on the floor in the form of a slab which can be picked up
the next morning.
When the cupola has been emptied of all slag and iron drop the
bottom. I like to draw the refuse out from underneath the cupola,
turning it over and cooling it down with water. The pieces of the sand
bottom are thrown to one side and all the iron that can be seen is picked
up. All the iron taken from the cupola dump, the pig bed, or from the
gangways, which is not bad casting, is weighed up and charged as remelt
or home scrap.
All remaining small pieces of coke, iron or slag are shoveled up from
the bottom and from all [jarts of the foundry and placed in boxes on the
cupola platform. This includes skulls from the ladles which comtain
more or less iron.
WTien the last charge of iron has been placed in the cupola and the
heat is near enough to the end to show that there will be no shortage of
iron, throw into the cupola any shot iron that may be left over, and all
the refuse previously mentioned. The iron and slag will be melted at
once and the small bits of coke will hold the blast down and insure hot
iron.
All the finest shot iron is saved in this way, as well as all coke in the
form of small pieces and nothing is lost."
The disposition on the part of many foundrj'men is to neglect the
Melting Borings and Turnings 293
saving of shot iron, preferring to sell to junk dealers what can be readily
recovered. Such will not be the case, however, in a well-managed foundry,
as by close attention to its recovery the loss in melt can be reduced
from I to 2 per cent.
At one of the large western foundries, through mismanagement, shot
had been allowed to accumulate until a portion of the yard was covered
to a depth of from 12 inches to 20 inches. This was dug up, milled and
melted; 1500 pounds, at each heat, were thrown on top of the last charge,
without additional fuel; the melted iron was run into pigs.
Over 84 tons of No. 4 pig were recovered; 25 per cent of the scrap used
in charging was replaced by this iron and the usual mi.xture was in no
other respect changed.
Burnt Iron
This class of iron is of no use e.xcept for making sash weights. When
used for ordinary purposes, the loss caused is greater than the gain. It
makes iron hard, causes a great amount of slag and chokes up the cupola.
It should be carefully selected and thrown out of the scrap.
Melting Borings and Turnings
Cast iron borings and turnings which are usually disposed of to junk
dealers at a low price may be advantageously melted by packing them
in wood or iron boxes, about 100 pounds to the box.
The boxes should be charged a few at a time, by throwing them into
the center of the charge and covering them with scrap. These will
descend to near the melting zone before they are burned or melted.
Mr. W. F. Prince has patented a process for melting borings, etc.,
which consists of packing them in sheet iron pipes, with or without
bottoms. The pipes are of any convenient length, from 30 to 48 inches;
the first one is placed on the coke bed and the others on top of it, with
the charges surrounding them.
This differs little from the method of using boxes, where the latter are
piled on each other. In either case the containers prevent the fine
material from being blown out of the stack.
Many attempts have been made to render borings, etc., suitable for
melting, by briquetting. So far, these efforts seem to have been only
partially successful.
A process has recently been developed in Germany, by which the
borings are made into briquettes under hydraulic pressure. It is claimed
that the product successfully meets the purpose and preliminary tests
made in America seem to warrant the statement.
CHAI'I'KR XII
TEST BARS
This subject has been Irealcd cxhausti\ely by a Committee of the
American Foundry men's /Vssociation. Their rejxjrl was adopted by
the Association in June, 1901.
Extensive extracts from the report are given below.
The work covered the testing of 1229 bars by 1601 tests; the folhjwing
table shows the character of the heats from which the bars were taken.
Series
A*
B
C
D
E
Ft
G
H
I
J
K
L
Class of iron
Melted in
Pig iron used
Ingot mould Cupola
Dynamo frame Cupola
Light machinery. . . Air furnace
Chilled roll Air furnace
Sand roll Cupola
Sash Weight
Car wheel
Stove plate
Heavy machinery.
Cylinder
Novelty
Gun metal
Cupola
Cupola
Cupola
Cupola
Cupola
Cupola
O. H. furnace
Coke
Coke and charcoal
Coke and charcoal
Cold-blast charcoal
Warm-blast char-
coal
Coke and charcoal
Coke and charcoal
Coke
Coke
Coke
Coke
Coke and charcoal
Size
of
heat
tons
60 1.67
60 1.9s
40 3.04
30 .8s
30
.7a
91
97,
3 19,1
I 96
a. 49
4 19
a. 33
o9Si .032
40s 043
578 044
48a| .070
454 070
441'. 318
301 .060
160 0S4
523 081
839 084
2361.080
676 .044
* All pig iron.
t Nearly all burnt scrap, originally from charcoal and coke iron.
"Throughout the whole line of operations only regularly constituted
mixtures were used, the balance of the heats from which these test bars
were cast going directly into commercial castings of the classes designated.
The results are, therefore, entirely comparable with daily practice.
For purposes of comparison green sand and dry sand bars were made
side by side.
It was felt that comparison records were wanted just as much as
specifications for the separate lines of product. For this reason, we
recommend one standard size of test bar for comparative purposes only,
each class of iron being given its special treatment for the information
wanted in daily practice in addition.
294
Test Bars
295
"Our studies on the shape of the test bar have resulted in the selection
of the round form of cross section and this mainly on the score of great-
est uniformity in physical structure. . . . There is still a further
point of interest, in the preparation of test bars and that is, the making
of coupons from which the quality of the castings to which they are
attached is to be judged. This method is used extensively in govern-
ment work and in the making of cyl-
inder castings.
The idea of obtaining material
from the same pour in the same
mould as part of the casting itself is
good enough in theory. Unfortu-
nately, however, this direct connec-
tion introduces elements of segrega-
tion and temperature changes in the
cast iron which make this test less
valuable than is generally supposed.
At best the iron which has passed
through the different parts of a
mold before entering the space for
the coupon will not be representa-
tive of the whole body, but rather
one portion of it only. We therefore
recommend the method shown later
on in Fig. 75. The metal can be
poured from crane or hand ladle,
clean and speedily, and possesses the
temperature of the average iron in
the casting more nearly than the
coupon method now practiced.
Your committee while giving spe-
cifications for the tensile test of cast
iron is of the opinion that the trans-
verse test is the more desirable and certainly within reach of even the
smallest foundry.
In selecting the test bars for the purpose of specification, we have
followed the cardinal principle of selecting the largest cross section for
the iron consistent with a sound physical structure and within the range
and structural limits of an ordinary testing machine.
The following are the sizes of bars selected for tests as a result of
our investigations.
For all tensile tests, a bar turned to .8 inches in diameter, corre-
@
Fig. 75.
296 Tt'Sl Bars
sponding to a cross section of 14 sfjuarc inch. Results, therefore, multi-
l)lictl by two, give the tensile strength per sfjuarc inch.
I'or transverse test, of all classes of iron for general comparison; a
bar I H- inches in diameter, on supports, 12 inches ajjart; pressure applied
in the middle and deflection noted.
Similarly for ingot mould, light machinery, stove plate and novelty
iron, a I'i-inch diameter l)ar; that is to say, for irons running from 2 per
cent in silicon ui^ward, or from 1.75 per cent silicon upward where but
little scrap is in the mixture.
For dynamo frames, sash weights, cylinders, heavy machinery and
gun metal irons; similarly, a 2-inch diameter bar is recommended, that
is, for irons running from 1.5 per cent to 2 per cent in silicon or where
the silicon is lower and the proportion of scrap is rather large.
I'or roll irons, whether chilled or sand, and car wheel metals, a 2^4-
inch diameter bar is recommcnrled ; that is, for all irons below i per cent
silicon and which may, therefore, be classed as the chilling irons.
The method of moulding the test bar we would recommend is given
herewith.
At least three bars of a kind should be made for a given test.
The sand should not be any damper than to mould well and stand the
wash of the iron without cutting, blowing or scabbing. It should be
rammed evenly to avoid swells and poured by dropping the metal from
the top through gates, or from ladle direct into the open mould.
iVfter the bars are cast they should remain in their moulds undis-
turbed until cool."
Proposed Standard Specifications for Gray Iron Castings
1. Unless furnace iron, dry sand, loam moulding, or subsequent
annealing is specified, all gray iron castings are understood to be of
cupola metal; mixtures, moulds and methods of preparation to be fixed
bj- the founder to secure the results required by purchaser.
2. All castings shall be clean, free from flaws, cracks and excessive
shrinkage. They shall conform in other respects to whatever points
may be specially agreed upon.
3. When the castings themselves are to be tested to destruction, the
number selected from a given lot and the tests they shall be subjected to
are made a matter of special agreement between founder and purchaser.
4. Castings under these specifications, the iron in which is to be
tested for its quality, shall be represented by at least three test bars cast
from the same heat.
5. These test bars shall be subjected to a transverse breaking test,
the load applied at the middle with supports 12 inches apart. The
Patterns for Test Bars of Cast Iron
297
breaking load and deflection shall be agreed upon specially on placing
the contract, and two of these bars shall meet the requirements.
6. A tensile strength that may be added, in which case at least three
bars for this purpose shall be cast with the others, in the same moulds
respectively. The ultimate strength shall also be agreed upon specially
before placing the contract and two of the bars shall meet the require-
ments.
7. The dimensions of the test bars shall be as given herewith. There
is only one size for the tensile bar and three for the transverse. For the
light and medium weight castings the i^ inch D bar is to be used;
for heavy castings, the 2 inch D bar; and for chilling irons the 2],^ inch
n test bar.
8. When the chemical composition of the castings is a matter of
specification, in addition to the physical tests, borings shall be taken
from all the test bars made; they shall be well mixed and any required
determination (combined and graphitic carbon alone excepted), made
therefrom.
9. Reasonable facilities shall be given the inspectors to satisfy them-
selves that castings are being made in accordance with specifications,
and if possible tests shall be made at the place of production prior to
shipment."
Patterns for Test Bars of Cast Iron
SSC31
f-ltp::
For Transverse Test
U-2"-n
w t-
/3
©'IC:::^'^
H- 2|^^^.- /of-
For "y?> Tensile Test
Fig. 76.
h2i"H
l--±
z>
K- //4 - -'<
Steel Socket for Tensile Test of Cast Iron. — Two required
Tp^--yf' r --- '^'-"-w- j-w
k J3" >l
Standard Test Bar for Cast-iron Tensile Test. — Cross section equals
3^ sq. in. ; test piece should fit loosely in socket
Fig. 77.
2y8 I'tsl Uars
Modulus of Ruplurc in I'ouuds Per Square huh
Tlie rtport of the committee is accompanie<J by a table giving the
mcxluli of rupture jier wjuare inch for bars under the various con-
ditions (jf the tests and from '« s<|uare inch to i6 square inches. It was
found that, with few exceptions, the values decrease as the areas
increase.
In the table on pages 299 and 300, which is extracted from their
reiwrt, the moduli are given for bars ha\ing areas of i square inch,
2.25, 4. and 9 square inches.
"The results show that rough bars arc stronger than machined and
that there is practically no diflerence between bars made in green or dry
sand.
An examination of the table shows that the transverse strength is
greater in the rough than machined bars, except in two instances, \iz.:
D bar, series J, in drj' sand the rough bar broke with 178 pounds less
load than the machined bar. O bar, series L, in dry sand, the rough
bar broke with 115 pounds less load than did the machined bar. The
average loss in transverse strength of the green sand bar by machining
was 12 per cent; that of the dry sand bar 10 per cent.
The following articles are introduced as showing how little reliance
can be placed on the results from test bars. It is shown that bars
identical in chemical composition, but made from diflerent brands, differ
widely in physical properties; indicating the importance of using in
mixtures, irons from different localities, as well as from different furnaces.
The micrographs show clearly the variation in structure corresponding
to the widely varv'ing results, but it remains for the metallurgist to point
out the causes for these differences."
Erratic Results — Test Bars
Mr. F. A. Nagle submitted to the American Society of Mechanical
Engineers the following report of his investigation of test bars for castings
used in the Baltimore Sewage pumps.
"In machinery castings as well as in cast i)ij)es, separate bars are cast
and subjected to tensile or transverse stress to the breaking point, these
results being used as evidence of compliance with the contract speci-
fications. The writer has examined a large number of such test bars for
castings used in the Baltimore Sewage pumps and here reports the results
of this examination and study.
Perhaps the most important conclusion is that the test bar is not to
be regarded with loo much confidence as indicative of the exact strength
of the casting. All transverse bars were nominally 2 indies by i inch by
Modulus of Rupture in Pounds Per Square Inch 299
Rough
Machined
Area in
square
Square
Round
Square
Round
inches
Green
sand
Dry
sand
Green
sand
Dry
sand
Green
sand
Dry
sand
Green
sand
Dry
sand
- Ingol Mould Iron.
Series A. Silicon 1.67
1. 00
37 140
27,530
44,210
33.660
43,200
38,610
26,100
27,840
2.2s
32,880
31.320
34.570
33.870
29.340
30,790
39.810
38,120
4.00
29.540
25,550
34.900
31,610
31.150
26,500
34.320
32,290
9.00
26,200
21,180
27,280
26,540
26,980
21,690
26,030
28,660
Dynamo Frame Iron. Series B. Silicon 1.95
1.00
39.220
38,380
44.300
49,160
37.440
30.240
40,020
39.150
2.2s
39.540
34.900
41.270
44.840
36,670
36.180
44.790
37.800
4.00
33.960
34.460
41,680
39.230
34.7SO
33.250
38.750
37.270
9.00
29,680
30,050
35.600
35.620
32,740
30,880
35.400
32.810
Light Machinery Iron. Series C. Silicon 2.04
37.000
32,880
36,170
30,980
39.190
38,780
34.S50
29.230
48,050
38,890
42,560
38,080
50,380
43,950
40,150
37,780
40,230
36,990
33,290
38.880
35.420
32,710
55.680
47.340
42,920
36,520
47.850
51,350
37.550
36,290
Chilled Roll (Furnace). Series D. Silicon 0.85
44,120
47,760
46,710
52,700
44,010
67,680
43.260
54.910
49.440
49.850
69,130
59,010
65,940
75.000
65,850
51.660
Sand Roll Iron (Furnace). Series E. Silicon 0.72
51.560
41.740
34.700
33.040
44.180
46,290
33.720
35,760
51,620
41 ,420
55. no
53,540
48.740
41,960
61,770
55,440
Sash Weight Iron. Series F. Silicon 0.91
52,920
59,170
61,870
42,710
42,540
51,130
Si,8io
39,160
58,430
39,840
50,130
42.370
50,050
53.010
47,090
4S.730
300
Test Burs
Rough
Machined
Area in
SqUATC
Square
Round
Sfjuaro
Round
inches
Green
sand
Dry
sand
Green
sand
Dry
sand
Green
sand
Dry
sand
Green
sand
Dry
sand
Car Wlieel Iron. Series G. Silicon 0.97
1. 00
47.110
44.810
52.600
61.720
43.200
46.080
64J80
52.200
2.2s
32.120
28,200
45.880
39.740
44.640
40.680
43.aoo
46,170
4.00
35.460
32.190
45.970
39.330
27.520
32.760
41.590
37JSO
9.00
32.0SO
32.140
37.610
3S.ISO
28.730
28,960
33.930
28,040
Stove Plate Iron. Series H. Silicon ^.ig
1.00
27.980
29.360
42.570
36.920
48.960
43.200
78JOO
68,600
2.25
24.960
30.710
42,160
41.420
22,500
24,480
33.250
3I.5SO
4.00
27.980
28,930
40.540
36.940
23.400
28.810
32.290
21,910
9.00
25,620
25,020
33.350
33.550
23.710
24.100
2S.S40
23,000
Heavy Machinery Iron
Series I. Silicon 1.
96
1.00
36,000
44.060
S3.2IO
54,180
43.200
46.080
52,200
S5.680
2.25
35.290
35.040
43.860
47.100
33.120
39.060
44.900
43.200
4.00
36.120
33.580
42.290
41,330
30,400
32.970
41,670
42,420
9.00
23.850
20,880
33.040
34.970
37.040
30,410
36/930
38/»»
Cylinder Iron. Series J. Silicon 2. ^g
1. 00
2.25
4.00
9.00
43.350
30.880
32.600
27,830
34.270
31.950
30.420
25.630
51.690
33,400
43.180
40,900
55. 500
41.900
41.320
40,170
39.790
39.960
26.400
26,400
39.790
38.520
26,610
24,890
52,200
51,040
38,110
34,470
46,980
53.160
38,240
34,310
Novelty Iron. Sei
'ies K. Silicon 4.19
1. 00
2.25
4.00
9.00
25.430
25.640
27.120
22,220
36.490
26.200
26,860
24.130
39.040
37.760
3.^,550
30,890
42,530
37.670
34.560
32.520
Gil
n Iron (Furnace).
Series L. Silicon 2.32
1.00
2.2s
4.00
9.00
52.230
49.290
50.400
41,980
44.030
46,760
49.990
43.050
71,570
67,060
66,980
S9.0I0
67.350
66.140
66.730
59.460
53.270
47.520
46.670
41.990
50,400
39.600
39.680
47.830
80,040
59.040
61,470
56.140
71.340
71.160
53.310
59.480
Erratic Results — Test Bars
301
24 inch centers. They were cast from two patterns in one mould and
made in the same kind of sand as the main casting. The flask was
inchned about 30 degrees. There was but one gate for the two bars with
suitable risers. The iron for the bars was poured from a small ladle of
iron taken as nearly as possible from the middle of the pour of the main
casting.
The breaking loads were, corrected for varying dimensions of the bars
by the formula W =
Wbd^
, where b and d are the actual dimensions,
W the actual breaking load and W the corrected load of weight. These
results are used throughout this paper. The deflections were not
corrected.
The tensile bars, 1% inches by 6 inches, were cast upright in the same
mould as the main castings, within 3 or 4 inches thereof, and connected
by an upper and lower gate. The tensile bars were turned to i i-i inches
in diameter and threaded, and the middle portion reduced to 1.129 inches
in diameter which is equal to i square inch area. Table I gives the
results of the chemical analysis of the several bars tested.
Table I
13
0
1
■d
<u
m
is
S--
a
1
.y
II
1
1,
3
P.
a
8
■4J ^
S3 o-
> M
a
.0
t
u
0
0 "
1
3
w
m
1^
Nov. 21,
1907....
3580
2.830
.75
• 79
.48s
.081
1. 59
24.900
2440
49
Nov. 26,
1907....
3.396
2.736
.66
.38
■ 459
.124
1.91
22.000
2075
.40
From Aug. 5, 1907 to April 4, 1908 there were made 67 single tensile
bars, and the same number of pairs of transverse bars; and the average
of the latter was used in this record. From April 4 to Dec. 19, 1908, there
were made 91 pairs of tensile bars and an equal number of transverse
bars and each piece of the pair is recorded instead of the average.
Of these 249 tensile bars and their corresponding transverse bars, 32
sets — 26 flat and 6 round — ^were rejected for defects due to blow-holes
and four tensile bars were too hard to bear threading, but the companion
pieces were used in this record.
Of the 217 specimens here recorded, 42 were designated as abnormal;
that is, the ratio between the tensile and the transverse bars was either
considerably greater or smaller than the average.
302
Tesl Hars
By referring to Table II it will be seen that of the 175 specimens of
cast iron runninj^ from 20,000 l<j jo.ooo pounds Icnsilc strength, the
ratio of tensile to breaking loads is practically 10 to i and the deflection
0.45."
Table 11
Number of
specimens
Transverse
Tensile
Deflection
Ratio of tensile to
transverse
Inch
29
206s
31,630
.43
I0.47
36
2289
22.940
• 45
10.03
SI
2523
24.880
47
9.86
43
2756
26.500
49
9 61
16
2894
28.460
49
983
J_
175
Average 2383
23.732
45
9 96
Comparison of Test Bars
Table III gives 25 abnormal cases where this average ratio is as high as
12.56 to I with a deflection of 0.43 inch, also 17 abnormal cases where
this average ratio is as low as 7.91 to i, with a deflection of 0.44 inch;
and yet the average of both normal and abnormal bars was again very
nearly 10 to i.
Table III
Above ratio 10 to i
Number of
Transverse
Tensile
Deflection
Ratio of tensile to
specimens
transverse
In.
10
2088
27,143
■ 41
12.9s
10
2294
28.530
.43
12.44
4
2436
29.600
•49
12.15
I
2890
34.000
■ 45
11.76
25
Average 2258
28.36s
.43
13. 56
Below 10 I
0 I
I
2105
17.600
.50
8.36
4
2359
18.825
.41
7.98
7
2487
18.814
.43
7.57
3
2656
21.330
.45
8.00
3
2969
24.S00
.47
8. 35
17
2S2I
I9.9S4
■ 44
7.91
Breaking loads, presumably alike, varied in pairs of transverse bars
and also in pairs of tensile bars as follows:
Comparison of Test Bars
303
Out of 65 pairs of flat or transverse bars, 14 or 22 per cent, average
variation 18 per cent; 17 or 26 per cent, average variation 5.4 per cent;
34 or 52 per cent, average variation less than 2 per cent.
Out of 65 pairs of round or tensile bars 22 or 34 per cent, average
variation 15 per cent; 20 or 31 per cent, average variation 5.5 per cent;
23 or 35 per cent, average variation less than 2 per cent.
61 other pairs of flat bars which had only one companion tensile bar
varied in about the same ratios.
Two special flat bars and two special round bars, cast in one mould, one
gate a.id at one pour varied as follows:
Two flat bars 12 per cent; two round bars 7 per cent.
In order to get some more definite information on these variations, if
possible, I had a pair of transverse and a pair of tensile bars made and
cast in the same mould and while the average was again nearly 10 to i as
shown in Table III, the same type of bars again varied 12 and 7 per cent
respectively.
Table IV
Comparison of Cast-iron Test Bars. Special. Two Sets Cast in
Same Mould at Same Time
Number of
specimens
Transverse
Tensile
Deflection
Ratio of tensile to
transverse
I
I
2
217
2350
2100
Average 2225
All averages 2380
23,000
21,470
22,235
23.970
Inch
• SO
.45
.47
.45
9-79
10.21
10.04
10.07
I
I
I
I
I have no satisfactory explanation for the great variation of these test
bars and we can only accept the fact that mathematical uniformity in
strength of cast-iron bars is not found in the present state of the art.
To any one questioning the results, I can only say from my own
knowledge of the circumstances, that the personal equation did not enter
into them.
Careful observation of broken bars did not show that the so-called
"skin of the metal " was of any appreciable thickness and the metal was
remarkably homogeneous throughout.
The tensile bars being turned, the skin, if there was anj^, of course
disappeared.
It is my opinion that the skin adds practically nothing to the strength
in either transverse or tensile bars; other causes, though obscxire, produc-
ing far greater deviations."
304
Test Bars
Casting Defects
Although many castings were cundcnincd for physical defects not a
single case of cold-shut was observed.
In one instance of defect, he says: "To remove all doubt that the test
bars were truly representative of the iron in the main casting, two tensile
bars were cut out of a large flange which had been at the bottom of the
mould. These, from the most favored |)art of the casting, as will be seen,
stood but about 17.350 pounds; 90 per cent of that revealed by the test
bars. In this case there was a rcmarkaijlc agreement between this pair
of test bars.
It may be interesting to apply these results to the formula for the
strength of cast-iron beams subjected to similar stress.
^ PI
The formula commonly used is /? = —^ , where R is called the modulus
2 b(P
of rupture, or stress per square inch of extreme fibre,
P = load at center,
/ = length between supports in inches,
b and d = breadth and depth respectively in inches.
Make the proper substitutions and we have R = 42,840 pounds.
This is not the correct figure, however, for the extreme fibre stress. We
know this cannot exceed the tensile strength which we have found to be
23,732 pounds.
I think it is better to use D. K. Clarke's formula given on page 507 of
his " Engine Tables." S = j-jr , where 5= extreme fibre stress or
1-155 od^
tensile strength. If we use the tensile strength found in these tests as
23,732 pounds, the breaking load W would become 22S4 pounds; the
actual breaking load being 2383 pounds. As this is within 4.3 per cent
of the average found in these tests, this formula, using the tensile strength
for the extreme fibre stress, seems to me to be more intelligible and dis-
penses with the "coefiicient of rupture."
Circular Test Bars
Since the foregoing was written I have had the opportunity to ob-
serve two circular test bars, nominally iV* inch diameter by 15 inches
long, with 12-inch centers. These bars were cast from two separate
patterns in one vertical dry sand mould, and poured from a small
hand ladle, first one and then the other, with the result shown in
Table V.
Circular Test Bars 305
Table V. — Circular Test Bars in Vertical Dry Sand Moulds
Bar mark
Transverse
Tensile
Deflection
Value IF by
formula
Original
diameter
H
3344
3344
3026
2
23,070
23,754
24,670
3
• IS
.15
.12
4
2948
3036
3153
5
I 30^;
H
I 305
X
I 300
/
6
The tensile bars were taken from the bottom ends of the broken test
bars, but I do not know whether H or X was poured first.
The first tensile bar H had a small air-hole, which being allowed for,
added 7 per cent to its tensile strength, and this is also given in the table.
A second bar was then turned up from the immediate joining piece with
the result recorded in the table first. The turned bars were 0.937 inch
diameter.
Column six gives the original diameter. Column two was found by
reducing the actual breaking loads in the ratio of the cubes of the diam-
eters, and column three was reduced to the square inch area. Why the
transverse breaking loads should vary 10 per cent and the tensile bars
4 to 7 per cent the opposite way, a total variation of 14 to 17 per cent, I
leave to the reflection of the reader. If we apply Clarke's formula for
the breaking weight for circular bars, W =
0.7854 X d^ X S
I
, we find the
values given in column five.
While the blow-holes seem to be more frequent in flat transverse bars
than in round attached tensile bars, the latter seem liable to a greater
abnormal hardness, for which I have no explanation.
Some indication of the toughness of cast iron may be seen in its deflec-
tion, which is not revealed in a direct pull. I would, therefore, be
satisfied with two or three transverse test bars 2 in. by i in. by 24 in.
centers, and a deflection record poured as near as may be from the middle
of the pour of the main casting as giving a fair indication of the iron
in the main casting, but mathematical exactness cannot be looked for as
yet.
If we wish to know approximately the corresponding tensile strength
of the iron, we can multiply the breaking load of the 2 in. by i in. by 24
in. flat bar by 10.
If the test bar is iH inch diameter by 12-inch centers its breaking
load should be multiplied by 8 to obtain the approximate tensile
strength.
3o6
Test Uars
The general rule seems lu be, that where lx)lh flat bars agree in break-
ing loads, the tensile strength is lo to i uf the breaking load, but where
they differ the lo lo i ratio docs not hold. A belter practice, therefore,
might be lo cast three round transverse bars and accept the two that
agree, if each is round, as a fair siimple of the iron, disjx'nsing with the
tensile bars. This concession lo ihc manufacturer, I believe, v/ould
entail not only no loss lo the city's interests, but a positive gain.
EFFECT OF STRUCTURE OF CAST IRON UPON ITS
PHYSICAL PROPERTIES
Microscopic Evidence of the Reason why Ikons of
Similar Chemical Composition have Different
Relative Strengths
BY
F. J. Cook and G. Hailstone
" During daily foundry practice, with work made from mixtures of iron
that have the same chemical composition and where tests are frequently
taken, it is often found that widely different physical results are obtained.
Instances of this have been brought to the notice of this association
. . . but in neither case was an explanation of the phenomena given.
Attempts have been made to give a satisfactory explanation of these
differences, but on the whole the conclusions arrived at have not been
generally accepted.
In the past the instances cited have generally been isolated ones, but
a remarkable series of tests over a lengthy period has recently been met
with by one of the authors.
t\s
-i- JL
xh .2^2^i^M"-' 111- ain •, ^^=.-
Z^'ii^ T^'^^^-TUi-'in , ^v i^^ ■
V 1l ^ 1 V.
15'
-kJ -,1 ^ ^-X-4, \-J
, ^ t^u^-iA^^4"i^^Ki^t^^ ^^^ ^^t.t
^ \t V^2 li^S^' EJ_ 17, ^3tSi^^ i
3< '/T m VfSpt -J; 7c. rti jr ■■ *
Fig. 78.
Fig. 78 is a diagram of tensile test results of two series of casts, each
representing 60 consecutive days working with irons nii.\ed to give the
Effect of Structure of Cast Iron upon Its Physical Properties 307
same chemical composition, but each series made up with different
brands of pig iron.
That the chemical analysis was identical in each case was proved by
analyses taken from time to time which, in each instance, for all practical
purposes came out alike.
The diagram shows that the highest tensile result in the A series was
lower than the lowest result in the B series. A summary of the whole
of the tests is shown in Table I.
Table I. — Results of Mechanical Tests
Tensile
test, tons
per square
inch
Trans-
verse test,
cwts.
I in. sq.
bar, 12 in.
center
Trans-
verse test,
lbs. on
li in. sq.
bar, 12 in.
centers,
Keep's
test
Shrinkage
in inches
H in. sq.
bar.
Keep's
test
Hardness
Blast
pressure
in ounces
Series
A
B
A
B
A
B
A
B
A
B
A
P
Highest
12.9
8.7
10.7
60
18.3
13. 1
15.8
60
28. 5
19.0
23.1
33
32.25
25.0
29.1
30
550
390
466
58
570
375
450
59
.182
.144
.140
58
.180
.140
.155
58
68
48
57>^
60
78
561/4
64 M
56
15
10
12%
44
16
II
Average
No test taken . .
13W
39
Each tensile test bar was i inch square and transverse and hardness
bars were cast relatively of the same size, and on the casting they were
to represent; while the 54-inch transverse bars, which were also used
for the shrinkage test, were cast separately by Keep's method.
The transverse bars were cast iH inch square, machined down to
I inch square and tested on 12-inch centers.
Referring to Table I, it will be seen that the results of the transverse
tests on the i inch square bars also show a marked difference, as do the
tensile tests. It will be noted, however, that the average result of the
transverse test on the ^4-inch square bars is slightly in favor of the series
which gave the weakest tensile, and with the i-inch square bar opposite
results. This point will be referred to later.
As the method of manipulation and the chemical composition of the
two series were the same, it was thought that a microscopical analysis
would reveal a cause for the vast difference. For the first investigation
a low bar of the A series, and the highest bar of the B series were ex-
amined. The chemical analysis of the two bars was first taken as
shown in Table II.
30« Tcsl liars
Table II, — Comi'arative Cukuical Analysis of the Two Series
Schc.
.,
B
9.1 tons per
Tensile test ] square inch,
I)er cent
18.3 tons per
square inch,
per cent
3.250
2.397
3092
3 2K0
•8S3 90J
1.328 I 314
.095 1 lOI
.923
■290
94 "4
.909
.335
94 149
Chemical Analyses
These analyses will be seen to he practically identical, even to the
amount of the combined and graphitic carbon.
To insure the results being absolutely comparative, a number of
micrographs were each taken from the same position at the center of
the bars. Fig. 79 shows the polished, but unetched section of the low
bar from the .1 series. Fig. 80 the high bar from the B series. These
show the size of the graphite in each case, the one having it in the form
of long flakes, the other in very small flakes.
Fig. 79.
Fig. 80.
Figs. Si and 82 show the same surfaces etched with iodine and magni-
fied 1 20 diameters. In the one case the large flakes of graphite are plainly
seen in a matrix of cementite, phosphorus eutectic, peariitc and ferrite;
while in the other, the graphitic carbon is scarcely visible and a closer
structure is observed. Otherwise, there is nothing very remarkable to
account for such widely different physical results.
Chemical Analyses
309
The same surfaces were then treated on the lines laid down by Mr.
Stead at the 1909 convention, to bring into prominence the phosphorus
eutectic. Fig. 83 shows the 9.1 ton bar, and Fig. 84 the 18.3 ton bar.
In both cases not only is the phosphorus shown but the cementite as
. well.
In Fig. 83 the phosphorus and cementite are evenly distributed, and
have not taken up any definite form of structure, the graphite being also
shown intermixed with them, but in Fig. 84 a very remarkable arrange-
ment of a net-like formation of phosphorus and cementite is shown. As
Fig. 81. — A Series; tensile strength
18,200 pounds per sq. inch; mag-
nification 120 diameters.
Fig. 83. — A Series; tensile strength
18,200 pounds per sq. inch; mag-
nification 30 diameters.
Fig. 82. — B Series; tensile strength
36,600 pounds per sq. inch; mag-
nification 120 diameters.
Fig. 84. — B Series; tensile strength
36,600 pounds per sq. inch; mag-
nification 30 diameters.
it had been noticed with bars previously examined that those giving
high test had also been associated with this particular net-like structure,
we were lead to the conclusion that probably strength was associated
with this structure independently of what the chemical composition
might be; we, therefore, examined a series of bars made by one of the
authors a few years ago to show the effect on strength of different rates
of cooling. For this experiment four bars had been made in one box,
cast from the same ladle of metal, which was ordinary No. 3 foundry
pig iron.
Taken from " castings," Aug. 1909.
3IO
Tc-si Hars
The rale of cooling was re^ulalt-d \)y means of cast iron chills of
(lidercnt thicknesses placed in the moulds for three of the bars, the other
having no iron chill. The bar without the chill gave a tensile test result
of 8.1 tons per stjuarc inch, while the bar at the other end of the series
broke at 15.2 tons per s(|uare inch. These two bars were selected, the
chemical analyses of which are given in Tabic III.
Table III. — Analysis of MEOiini Bar
Tensile- strength
13.9 per cent
3 J7a
2.740
532
1.307
III
.948
.330
94 032
Graphitic carbon
Silicon
Phosphorus
Iron by difference
Chilled and Unchilled Bars
These results are identical, and as there is practically no combined
(arbon present, there must be an absence of cementite. The bars are
also totally diCfcrent in chemical composition from those previously
examined.
Figs. 85 and 86 show unetched sections from the two bars, with the
difference in the formation of the graphite as previously pointed out in
Fig. 85.
Fig. 86.
connection with the other bars; that is, elongated flakes of graphite in
the unchilled bar, and finely divided graphite in that of the chilled
one.
Figs. 87 and 88 show the formation of the phosphorus eutectic in the
case of the weak bar to be broken up and ha^^ng no distinct pattern,
while in the case of the strong bar there is dearly shown that net-Uke
Chilled aixl Unchilled Bars
311
formation which was the distinguishing feature of the strong bar from
the B series, but with this difference, tliat the structure was rather
smaller.
As there is no cementite present in this specimen, it is proof that the
particular formation is not dependent upon cementite.
Fig. 87.
There was next examined another bar from B series. This had a
tensile strength about half way between the two bars previously selected,
and had given a tensile test result of 13.9 tons per square inch. The
analysis of this bar is shown in Table III. This showed that while the
total carbon and other elements were practically the same as the two
bars previously taken, the graphitic carbon was higher by 0.35 per cent,
and the combined carbon lower by 0.35 per cent. This was probably
due to the fact that this bar had been cast on a much larger casting than
the previous two.
The size of the graphite in this bar is illustrated by an unetched
section in Fig. 89 which shows that although it is smaller than that shown
in Fig. 79 of the 9.1 ton bar, it is larger and more elongated than that
contained in the 18.3 bar, Fig. 80.
Fig. 89.
Fig. go.
The phosphorus eutectic which is shown in Fig. 90 is the same net-like
formation as associated with the previous strong bars, though rather less
dearly defined and appears to be getting into the transition stage between
the two.
312 Test Bars
The foregoing results, we think, have been sufficient to show that in
each case, physical properties ha\e been associated with this net-Uke
formation of the phosphorus, also that the graphite, when in the elongated
form, appears to split up phosphorus eutectic and prevent this formation,
as clearly shown in F'ig. 83. The question of the tendency of the graphite
to take either an elongated or finely divided form, we think, is more a
question of the way in which the pig iron has been made than of its
subsequent treatment in the foundry. The statement of Mr. Pilkington
in this respect is very interesting: "Furnace men have always been
conversant with the fact that the temperature at which pig iron leaves
the tapping hole of the furnace has a powerful effect on its physical
characteristics. The temperature of a large modern blast furnace is
very much higher and the metal, therefore, takes very much longer to
cool than that which leaves the tapping hole of the smaller furnaces.
Pig iron from the extreme types could be made practically in a
different manner altogether, and would show very different grades, grains
and degrees of hardness.
On referring again to the sunmiary of tests taken with the A and B
series it will be seen that the results of the ,' 2-inch transverse bars of the
A series, which gave weak tensile results, are slightly higher than those
of the B series, and from this, together with the evidence of the chilled
and unchilled bars made from low grade iron, we are of the opinion that
no matter what their chemical compositions may be, there is a rate of
cooling which will give high physical properties; the structure of the
iron then being associated with the net-like formation of the phosphorus
eutectic and the cementite when present.
Tests reported to the International Association for Testing Materials
show:
Circular bars showed greater bending and tensile strength than those
of rectangular section.
Test pieces taken from castings showed lower strength figures than bars
separately cast.
Extracts from Prof. Porter's Report
Prof. Porter's report contains so much information of value to the
foundryman, that extensive extracts are made from those parts relating
to the properties and mixtures of cast iron, notwithstanding they may
comprise much which has already been considered.
In treating of the different forms of iron as occurring at differ-
ent temperatures, they are designated as the "alpha," "beta" and
"gamma."
The "alpha" form in the ordinary iron as known in unhardened steel
Chilled and Unchilled Bars
313
at ordinary temperatures, is one of the constituents of slowly cooled
gray pig iron, and is formed below 1140° F.
The "beta" form is that between 1440° F. and 1680° F.; it is harder
than the "gamma." Prof. Howe suggests its identity with martensite,
the chief constituent of hardened tool steels. It is non-magnetic and
diflfers from "alpha" iron in specific heat and density.
The "gamma" form is the stable one above 1680° F., is very hard,
non-magnetic, and differs in specific heat and density from both the
"alpha" and "beta."
It is held that the "gamma" and "beta" forms may be preserved at
ordinary temperatures by verj^ rapid cooling, especially in the presence
of carbon which is supposed to retard the change from one form into
another.
Table I. — Forms of Combination of Iron anb Carbon
Name
Synonyms
Physical characteristics
Graphite
Very soft dark flakes of variable
size. No strength.
Kish
Graphite in very large flakes.
Graphite in form of very fine
powder.
Temper carbon . . .
Free carbon
Ferrite
Iron
Soft, very ductile, low strength.
Very hard and brittle, high static
Cementite
Combined carbon. Iron car-
bide. FeC.
strength, no ductility.
Austenite
Solution carbon in "gamma"
Slightly softer than martensite.
iron.
Also weaker and more brittle.
Martensite
Solution carbon in "beta"
Hard, but less brittle than ce-
iron. Transition product
mentite. Chief constituent of
austenite to pearlite.
hardened tool steels.
Troostite
Transition product marten-
Softer than martensite, less
site to sorbite.
brittle and more ductile.
Sorbite
Transition product. Troost-
ite to pearlite.
Softer than troostite and more
ductile. Strongest form.
Pearlite
An intimate mechanical mix-
Very strong. Harder than fer-
ture of cementite and fer-
rite.
rite.
Prof. Porter classifies the more important physical properties of cast
iron as follows:
Static strength, including: Tensile strength; compressive strength;
transverse strength; torsional strength; shearing strength.
Dynamic strength, embracing: Resistance to repeated stress; resist-
ance to alternating stresses; resistance to shock.
Elastic properties, embracing: Elastic Hmit; resilience or elasticity;
rigidity; toughness; malleability.
314 Test Bars
Hardness, embracing: Hardness *>{ mass; ability to chill; hardness
of chill.
Grain slruclurc, including: I-ractiirc or grain size; f>orosity; specific
gravity.
5Artnitagc, embracing: Shrinkage of the liquid mass; shrinkage of the
solid mass; stretch.
Fluid properties, embracing: Fusibility; fluidity.
Resistance to Ileal, embracing: Resistance to continued heat; resist-
ance to alternate healing and cooling; resistance to very low temjjcratures.
FJectrical properties, including: Electrical conductivity; magnetJc
permeability; hysteresis.
Miscellaneous properties, including: Resistance to various corrosive
agencies; resistance to wear; coetTicient of friction.
Properties of the mass: Soundness, or freedom from blow-holes and
shrinkage cavities; cleanness, or freedom from inclusions of dross, etc.;
freedom from pin-holes and porous places; homogeneity, or lack of
segregation; crystallization; freedom from shrinkage strains; tendency
to peel off sand and scale.
CHAPTER XIII
CHEMICAL ANALYSES
Strength
As regards chemical composition there are nine factors which influence
strength of cast iron: (i) Per cent graphite; (2) size of individual graphite
flakes; (3) per cent combined carbon; (4) size of primary crystals of
solid solution Fe-C-Si; (5) amount of dissolved oxide; (6) per cent
phosphorus; (7) per cent sulphur; (8) per cent silicon; (9) per cent
manganese.
1. "Per cent graphite. — The weakening effect of graphite is due to
its own extreme softness and weakness, and to the fact that it occurs
in small flakes or plates and hence affords a multitude of cleavage planes
through the metal. The size of the graphite particles is evidently
important as well as the amount but this factor will be discussed under
another head.
Theoretically, the simplest method of decreasing graphite is to lower
the silicon, each decrease on i per cent in silicon lessening the graphite
by 0.45 per cent, provided the total carbon remains the same. Practi-
cally, however, the fact that all the carbon not graphite becomes combined
is an important objection, for when we lower the silicon too much the
resulting increase in combined carbon increases the hardness and, beyond
a certain point, decreases the strength. The minimum permissible
silicon will depend chiefly on the hardness allowable.
The same objection applies to decreasing the graphite by increas-
ing the sulphur and manganese, and in the case of sulphur there is
also the objection that its direct effects are injurious. The rate of
cooling is, of course, beyond the control of the foundryman in the
majority of cases, while even if it were not, the graphite could not
be reduced by rapid cooling without a corresponding increase in com-
bined carbon.
Coming finally to the total carbon, we find here a means of reducing
graphite without in any way affecting carbon, and hence, hardness.
The only limitation to this is that as total carbon and graphite are
reduced, shrinkage is increased and the metal becomes more liable to
oxidation, blow-holes and other defects.
31S
3i6 Chemical Analyses
There are three ways of reducing total carbon in castings; first, by
ihc use of low carbon pig iron; second, by melting in the air furnace;
tliird, by the use of steel scrap in the cupola mixture.
In air furnace melting it is easy to reduce total carbon to almost any
U^UTC within reason. 2.75 per cent is commonly obtained in melting for
malleable castings. Of course the silicon is also burnt out during this
l)rocess, but were it desired, this could be readily replaced by suitable
additions of ferrosilicon. From the standpoint of quality the air
furnace is certainly the ideal method of melting, and hence, we find that
many lines of castings which must be of particularly high quality are
invariably made from air furnace metal.
The addition of steel scrap to the cupola has now become common
practice, the product obtained being known as semi-steel and differing
chemically from ordinary cast iron only in being somewhat lower in
total carbon and graphite. Physically the metal so made is characterized
by greater strength and total shrinkage, hardness remaining about the
same. ..."
The chief points to be watched in melting steel scrap in the cupola
mixture are as follows:
" Trouble with hlow-hohs. — This is due to the fact that semi-steel being
lower in carbon oxidizes more readily than cast iron. The trouble may
usually be overcome by correct cupola practice and the use of ferro-
manganese or other deoxidizers in the ladle. Owing to the higher
melting point of semi-steel mixtures, ferromanganese is much more
efficient as a deo.xidizer here than in the case of cast iron. . . .
Tligh shrinkage. — This is due to the decrease in graphite and is
hence inevitable. On work where this is an important factor a proper
balance must be struck between shrinkage and strength. . . .
Imperfect mixture of steel and iron resulting in irregular quality of
casting, hard spots, etc. — This results from the higher melting point of
steel and consequent difficulty of getting perfect solution in the cast
iron. It ma)' be largely overcome by careful attention to the charging
of the cupola, placing the steel scrap on the coke and the iron on top of
the steel (so that the steel will reach the melting zone first and the molten
pig wall run down over the heated steel instead of away from it as would
happen if the order were re\'ersed). \ large recei^^ng ladle should, of
course, be used also. Another point to be obser\'ed is in regard to the
size of the steel scrap. Too large scrap is difticult to melt, but, on the
other hand, very small scrap is also objectionable as being an abundant
source of hard sjiots in the castings. .Apparently very small pieces of
steel are liable to be washed down through the coke bed and out of the
cupola spout without being completely melted.
Strength 317
Regarding the amount of steel scrap to use, it has been found by trial
that the best results are obtainable with about 25 per cent. Increase to
33 '4 per cent caused a slight falling off in strength. Probably these
figures would not hold for every condition of practice, but, in general,
20 to 30 per cent steel is a sufficient amount to give the maximum
results.
2. Size of graphite flakes. — The size of the graphite flakes is prob-
ably the most important factor of all those which influence strength, and
is the one which most frequently upsets our calculations as to the rela-
tion between chemical composition and strength. . . . Recently, how-
ever, Messrs. F. J. Cook and G. Hailstone have brought out in a striking
manner the great difference in irons in this respect. They give data
showing that of two mixtures practically identical in composition the
one was invariably much lower in strength (usually about one-half)
than the other, this being the case for a great many heats extending over
a long period of time."
Analyses and tests are given as typical of the series.
"Messrs. Cook and Hailstone have investigated and compared the
micro-structure of the strong and weak bars and record two interesting
facts: First, that the graphite flakes are invariably much larger in the
weak bars; second, that when the polished specimens are treated so as
to bring out the phosphide eutectic this eutectic is seen to be arranged
in the customary heterogeneous manner in the weak bars but in a dis-
tinct meshwork structure in the strong iron.
These authors draw the conclusion that it is this meshwork structure
which gives great strength to cast iron, but with this conclusion the
writer cannot entirel}^ agree. It seems more probable that the increase
in strength is caused by the fine state of division of the graphite and that
the same influences which have caused this have also caused the meshwork
structure.
We may get some idea of the quantitative relationship between
strength and size of graphite by considering the relative strength of
malleable cast iron and a very open gray cast iron representing the
smallest and largest graphite respectively. Malleable cast iron has a
tensile strength of 40,000 poimds and upwards per square inch; open
gray iron about 20,000 pounds per square inch. Apparentl}', then, the
increase in the size of the graphite has caused a loss of at least 20,000
pounds in tensile strength.
It is one thing to find that to get strong iron we must have the
graphite in finely divided state and another and much more diflicult
matter to formulate rules whereby we may secure this desired
condition. . . .
3i8 Chemical Analyses
The factors which inlluciuc the size of the graphite flakes in cast
iron are as follows:
A. Factors which certainly exert an influence.
a. Rate of cooling.
b. Pouring tempgrature.
B. Factors which may possibly exert an influence.
c. Time which iron has remained in the molten state.
d. Presence of dissolved oxide.
e. Presence of steel scrap in the mixture.
/. Mixture of difl'ercnt brands.
g. Nature of ore from which iron is made and treatment in the
blast furnace.
h. Per cent metalloids.
a. The influence of rate of cooling is undoubted, and an example
showing its effect on strength and structure is given by Cook and Hail-
stone. We have to distinguish here, however, between the rates of
cooling through different ranges of temperature. Evidently the graphite
which is separated within the semi-Uquid iron will have a much better
chance to grow large cr>'stals owing to the greater mobihty of the medium
in which it is formed, while that graphite formed within the solid metal
will necessarily be in small particles. Hence, we see that it is the rate
of cooling through the soHdification range 2200° to 2000° F., which is
of prime importance, and if we can check the formation of graphite
through this range and then allow it to form in the solid metal at lower
temperatures we will have all the conditions for both the soft and strong
iron. This is the principle of Custer's process of casting in permanent
moulds and the making of malleable castings is based on the same theory."
b. The pouring temperature also undoubtedly exerts an influence
on the size of the graphite flakes, and hence, on the strength. ..."
Longmuir finds that iron poured at a medium temperature is stronger
than when poured either very hot or very cold. Longmuir's e.xperi-
ments, b}' the way, are the only ones in which a pyrometer was used and
the temperatures of pouring measured in degrees. . . . For this
reason we may place the greatest faith in Longmuir's results.
It is probable that the pouring temperature affects the size of the
graphite flakes indircctlj' through changing the rate of cooling through
the solidification range. On this assumption the best results should be
obtained from metal poured at as low a temperature as will suflSce to
give sound castings.
c. Time uhicli iron has remained in the vwUoi stale. This might
tunceivably have an effect in the case of cast iron high in total carbon,
Strength 319
since graphite separating in the liquid metal would remain in the metal
if poured at once, and this graphite is in the form of large flakes known
as kish.
d. Presence of dissolved . oxide. — There is no direct proof that this
affects the size of the graphite flakes. However, it is well known that
addition of deoxidizing agents almost invariably improves the strength
and it is barely possible that a portion of this may be due to change in
the size of the graphite.
e. Presence of steel scrap in the mixture. — Although no exact data
are at hand it is the common impression that the addition of steel scrap
'closes the grain,' which is equivalent to saying that it reduces the size
of the graphite. . . .
/. Mixture of irons. — It is firmly believed by many foundrymen
of the old school that a mixture of brands gives better results than a
single brand of the same chemical composition as the average of the
mixture. . . .
g. Cook and Hailstone believe that the difference in strength of the
two mixtiures quoted by them is due to some inherent quality of the pig
iron derived from the ores used or their manner of treatment in the blast
furnace. This inherent quality may have some connection with the
presence of oxygen or nitrogen in the metal. ..."
h. Per cent metalloids. — This, we know, has a certain effect. For
example, high silicon is likely to, cause larger graphite as well as more
of it. Phosphorus should, theoretically, cause larger graphite since it
prolongs the solidification period in which large flakes are free to separate.
. . . Sulphiur and manganese . . . close the grain, and probably
diminish the size of the graphite, as well as its amount.
3. Per cent combined carbon. — According to Professor Howe the
properties of cast iron are the properties of the metallic matrix modified
by the presence of the graphite, but since this metallic matrix may be
considered as a steel of carbon content equal to the combined carbon of
the cast iron, we can predict accurately the effects of combined carbon
by the use of the data on steel.
In the case of steel it is found that the strength increases regularly
with the carbon up to about 0.9 per cent, then remains nearly stationary
up to about 1.2 per cent, above which it falls off slowly.
In the case of cast iron the strength is dependent upon so many
factors besides combined carbon that it is almost impossible to determine
by direct experiment the percentage of combined carbon giving the
maximum strength. All indications, however, are that the highest
strength is obtained with somewhere between o. 7 per cent and i per cent
combined carbon which is in sufficiently close accord with the corre-
320 Chemical Analyses
sjxjnding value for stccl. \Vc may, therefore, stale tentatively that the
maximum strength is obtained with 0.9 per cent carbon, all other factors
remaining constant.
Tliis applies only to tensile strength (and approximately to transverse).
I or lompressivc strength a somewhat higher value, probably alxjut 1.5
l>cr cent combined carljon, would be found to give Ijellcr results.
4. Size of primary crystals 0/ solid solution Fe-C-Si. — There is
absolutely no data as to the cflcct of this factor on the strength of cast
iron and it is only from analog)- with steel that we give it a place in the
list of actors influencing strength. ..."
5. Ejfect oj dissolved oxide. — ... It is j)robabIy a much more
important factor than is generally supposed, but there is absolutely no
data on which to base a quantitative estimate of its effect."
To reduce o.xide in cast iron to the minimum, the following points
may be obscr\ed :
First, get the best brands of pig iron. It i.s probable that pig made
with charcoal fuel contains less o.vygen than that made with coke fuel.
Cold blast pig is better than hot blast. Pig iron made from easily
reducible browTi or carbonate ores is lower in oxygen than the pig made
from red hematite or magnetic ores, whih iron made from mill cinder
should never be used in foundries 'uliere strength is a prime consideration.
Moreover, a pig iron high in manganese is apt to be comparatively free
from oxide because of the deoxidizing power of manganese at the high
temperature of the blast furnace. It is noteworthy as confirming these
obserx'ations that most brands of iron which have achieved a reputation
for strength are high in manganese and many of them are charcoal irons.
The Muirkirk and Salisbury brands wloich have been knowTi for years
as among the strongest irons made in this country answer to every
one of these conditions. They are made from readily reducible ores
using cold blast and charcoal fuel and contain from i to 2 per cent
manganese."
Second, avoid oxidizing conditions in the cupola, particularly high-
blast pressures and wrong methods of charging. Dr. Moldenke's
system of using small charges is to be higldy recommended in this
connection."
Third, deoxidizing agents may be used, added either to the cupola
or to the metal in the ladle. Of the commercially available deoxidizers,
ferrotitanium, ferrosilicon and ferromanganese are, perhaps, the most
successful, all things considered. Titanium thermite is also extremely
valuable in this connection. ..."
6. Per cent phosphorus. — Phosphorus lessens both the djTiamic and
static strength, but the former more than the latter. It weakens be-
Strength 321
cause it forms with iron a hard and brittle compound which has but
little resistance to shock. The weakness produced is in nearly direct
proportion to the amount of this compound present. The efifects of
•phosphorus on strength do not become marked until upward of i per
cent is present, but for great strength and particularly strength to shock
it should be much lower. Ordinary strong irons may have up to 0.75
per cent, while iron which is to withstand shock should not exceed 0.50
per cent and is better even lower. ..."
7. Per cent sulphur. — The action of sulphur in decreasing the strength
of iron is explained in Chap. IX, page 261, and it is also explained
there why it is so much less harmful in the presence of manganese.
Many tests have been made showing that sulphur has no marked effect
on strength and many foundrymen will use sulphur to harden iron and
close the grain. It is true that an indirect strengthening effect can be
obtained through the use of sulphur in some cases, i.e., if too soft an
iron is being used the strength will be increased by the addition of any
element which will lessen the graphite, but the hardening is usually better
obtained through decrease in silicon than through increase in sulphur.
While increased sulphur may not always show in decreased strength of
test bars, yet it is a frequent source of blow-holes, dirty iron and various
defects caused by high shrinkage, hence, it often causes an indirect
weakness in the iron.
8-9. Per cent silicon and manganese. — These elements act chiefly in
an indirect manner and because of their effects on the condition of the
carbon; their direct influence in the strength of the metallic matrix is
unimportant. From analogy with steel it is probable that sihcon in
amounts of over i per cent causes weakness and brittleness in the metal.
Similarly, manganese has probably a weakening effect due to its direct
action when present in amounts of more than 1.5 per cent.
The preceding discussion is summarized in the following practical
rules for making strong castings:
Use strong brands of iron. . . . Charcoal irons if cost will permit;
irons made from easily reducible ores; irons high in manganese.
Avoid oxidation in melting. Look carefully after the details of
cupola practice; avoid oxidized scrap; use deoxidizing agents in
ladle if practicable. . . .
Keep the silicon down as low as possible and still have the necessary
softness. About 1.50 per cent will be right for the ordinary run
of medium castings; higher for small castings and lower for
heavy ones. With low total carbon high sihcon has less effect.
Keep the phosphorus low, especially when sulphur is high. 0.50
per cent or under is best.
322 Chemical Analyses
Keep ihc sulphur low, especially if phosphorus is high. Unrler
o.io per tenl is all right for most castings."
Keep manganese high, i per cent for large castings, 0.7 per cent
for medium, 0.5 per cent for small castings.
Use from 10 to ^5 jkt lent steel ^crap in the mixture.
Mk. Ki:t;p recommends using 10 per cent cast iron Iwrings charged
in wooden Ixjxes. He states that this is very effective in closing
the grain and strengthening the castings.
For iron which is required to have the greatest possible resistance
to shock, the points to be especially observed are as follows:
Keep the phosphorus as low as practicable, still having the necessary
fluidity. It should best be below 0.30 per cent.
Keep the sulphur as low as possible.
If practicable add vanadium or titanium to the ladle either in the
form of ferroalloy or as thermite. . . .
Elastic Properties
Of the elastic properties of metals, only toughness and its opposite,
brittlcness, and elasticity and its opposite, rigidity, are ordinarily con-
sidered in cast iron.
Toughness is defined as resistance to breaking after the elastic limit
is passed.
Elasticity is the amount of yield under any stress up to the elastic hmit.
It is unusual for these properties to be determined separately in cast
iron, but their sum is given by the deflection which is determined in
transverse testing. It is probably true that they nearly always vary
together, and, hence, that deflection is a fairly good measure of either
one as well as both.
Toughness is practically always a desirable quality in cast iron, but
the same is not true of elasticity since in many machines great rigidity
is a i)rime requisite.
The factors influencing toughness and elasticity are about the same
as those influencing strength, i.e., the chemical composition, presence of
oxide and size of graphite. ... In general, to get a tough elastic
iron we should keep sulphur, phosphorus and combined carbon low;
manganese, no higher than is necessar>' to take care of the sulphur;
graphite and silicon, the less the better, providing that the combined
carljon is not increased; and finally, use metal of good quality, melted
carefully so as to be free from oxide.
In ordinar>' gray iron castings it is not practicable to attempt to
control the graphite, since the combined carbon needs first attention and
Elastic Properties
323
the graphite will necessarily be the difference between total carbon and
combined carbon. The silicon also must be adjusted with a view to
regulating the combined carbon. Practical rules for getting the maxi-
mum toughness and elasticity will then be about as follows:
SiHcon, 1.5 to 2.0 per cent for castings of average thickness, more or
less for very light and very heavy castings respectively.
Sulphur as low as practicable, best under 0.08 per cent.
Phosphorus as low as practicable considering the necessity for
fluidity. Best under 0.50 per cent.
Manganese from three to five times the sulphur.
Use good irons and good cupola practice to insure freedom from
dissolved oxide. . . .
"In case steel scrap can be used, i.e., semi-steel made, the toughness
may be considerably increased through decrease in the amount of graphite
and in the size of the grain. The other elements may remain about as
before except that it may be necessary to run the manganese a httle
higher to counteract the greater tendency of the semi-steel to become
oxidized.
As previously noted, rigidity is desirable in some cases. This is the
converse of elasticity and may be obtained by the direct opposite of the
rules given for obtaining elasticity. However, to get rigidity with the
least sacrifice of strength and toughness it is desirable to use manganese
and combined carbon rather than to increase phosphorus and sulphur.
That is, we would lower silicon as much as necessity for softness will
allow and raise manganese to about i per cent (or less in very light work).
It should be noted that manganese is particularly efficient in increasing
rigidity since it accomplishes this end with comparatively little sacrifice
of strength and toughness.
A few examples of very tough and elastic iron are as follows:
No.
Silicon
Sulphur
Phos-
phorus
Manga-
nese
Com-
bined
carbon
Graphite
carbon
Total
carbon
I
2.50-2.75
.80
2.45
1. 18
2.36
.050
.092
.084
.064
30
■ 43
■ 30
.24
'"'87"
I 08
2.34
2.15
3.21
3
4
S
063
27
33
3.23
No. I represents iron which in thin sections can be punched and bent.
No. 2 is an analysis of a gray cast iron which is exceedingly malleable.
Nos. 3, 4 and 5 are gray irons showing deflections for the transverse test
bars rather higher than usual.
324 Chemical Analyses
Hardness
. . . It is generally stated that hardness in cast iron is due chiefly
to the presence of combined carlxm and is only indirectly or to a less
extent caused by other elements. The writer believes that this is not
altogether true and that there is another factor causing hardness which
has not heretofore been generally considered in the case of cast iron."
It is well known that when steel is hardened by quenching from a
temperature above its critical point its carbon is not in the combined
state l)ut rather in a form known as hardening or solution carbon, while
the iron is retained in the 'gamma' allotropic form. It is the bcUef of
the present wTiter that the same is true of cast iron and that many cases
of hardness are to be explained in this way. For example, Keep de-
scribes a sample of cast iron which was too hard to drill and yet containetl
only 0.60 per cent combined carbon, and many analyses are on record
of irons which have been quenched from comparatively low temperatures
and are almost glass hard in spite of the fact that the combined carbons
are under i per cent. I think it probable that the hardness of high
manganese irons is due chiefly to this same cause since manganese is
known to favor the retention of 'gamma' iron.
Granting for the present the truth of this theory, the presence of the
'gamma' or hard form of iron is controlled by the rate of cooUng and the
percentages of metalloids present; so that for all practical purposes we
can say that there are six factors which influence hardness, i.e.. the rate
and manner of cooling, the combined carbon, silicon, sulphur, man-
ganese and phosphorus. The first two of these are of the greatest
importance and we will then take up in reverse order, leaWng the most
important till the last.
Phosphorus has a slight hardening eCfect in large quantities but in
amounts less than i per cent its eCfects are nearly unperceptible, and it
does not become important until the amount exceeds commercial Umits,
or, say, 1.5 per cent. We may, therefore, usually neglect the efJects of
phosphorus in considering hardness.
Manganese, although usuallj- regarded as a hardening agent may
sometimes soften iron. This anomalous result is cxplaincil l)y the action
of manganese on sulphur. If the iron is high in sulphiu- and low in
manganese the first additions of manganese will unite with the sulphur
forming the comparatively inert manganese sulphide and thus softening
the iron. If, however, the manganese be increased beyond the amount
necessary to care for the sulphur, increased hardness will result.
... A pig iron containing 3 per cent manganese may ha\e a
beautiful open gray fracture and yet be so hard as to be drilled only
Hardness 325
vnth great difficulty. In addition, the presence of manganese sometimes
produces a peculiar kind of gritty hardness, the iron acting as if contain-
ing small hard grains. With regard to the amount of manganese re-
. quired to produce hardness it will be evident that this depends largely
on the per cent of sulphur present and also on the rate of cooling. In
general, heavy castings will stand up to i per cent of manganese without
noticeable increase of hardness, medium castings about 0.75 per cent
and Hght castings 0.50 per cent.
Sulphur is an exceedingly energetic hardening agent acting, however,
chiefly through the carbon. That is, sulphur has a strong tendency to
keep the carbon in combined form and in that way to harden
Each o.oi per cent sulphur will increase the combined carbon by about
0.045 P^r cent, other things being equal. It must be remembered, how-
ever, that this applies only to sulphur in the form of iron sulphide, and
that in the form of manganese sulphide, i.e., in the presence of about
three times its weight of manganese, it acts much less energetically.
Sulphur also has a direct action in hardening, iron sulphide and
manganese sulphide being quite hard substances. Usually this action
is imperceptible, but occasionally one meets with hard spots which are
due to the segregation of these sulphides.
Silicon is generally known as a softening agent and, within reasonable
Umits, has this effect due to its action in decreasing the combined carbon.
The direct effect of silicon, however, is to harden since it forms with iron
a compound which is harder than the iron itself.
When silicon is added to cast iron its first effect, as before stated, is
to decrease the combined carbon. This, it does, at the rate of about
0.45 per cent for each per cent of silicon added. Actually the rate of
decrease is more rapid than this, and, in consequence, by the time we
have from 2 to 3 per cent silicon present (depending on the rate of cooling)
we have practically all the combined carbon precipitated out as graphite
and, hence, there is no further possibility of softening in this way. Now,
any increase in silicon only increases the amount of the hard iron-silicon
alloy, there is no more combined carbon to be decreased, and, hence, the
hardness will now be increased again. In other words, it is possible to
have too much of a good thing, the good thing in this case being silicon.
The actual percentage of silicon which is necessary to secure any
given degree of softness will depend upon the size of the casting, the
nature of the mold and the amount of sulphur and manganese present.
It is, therefore, impossible to give definite silicon standards unless each
of these factors is known. . . .
Combined carbon (or solution carbon) is the chief hardening agent
of cast iron, and, under ordinary conditions, the hardness of the metal
326 Chemical Analyses
will be cl<3scly profMjrlional to the i)erccntai,'c present. Of such relative
unimportance are the efTects of the other elements that it has been found
practicable to use the amount of combined carlx)n as a measure of the
hardness of castings and as a means of predicting their liehavior in the
machine shop. . . .
"To machine easily, cast iron should not contain over 0.75 \ycT cent
combined carbon, i.oo per cent combined carbon gives a pretty hard
casting and 1.50 jjcr cent is about the upper limit for iron to be machined.
The rate and manner of cooling of the casting are usually supposed
to influence its hardness only as it affects the percentage of combined
carbon. That it does affect the amount of combined carbon is a well-
established fact. . . . However, we sometimes get hardness in the
absence of any considerable amount of combined carbon. Hence, there
must be some other factor at work, wiiich, in the writer's opinion, is a
solution of carbon in 'gamma' iron, the hard constituent of tool steel.
According to this theory, combined carbon disappears in the tem-
perature range 2200° F. to 1500° F., while 'gamma' or hard iron is not
transformed into the 'alpha' or soft variety until the casting has cooled
to about 1300° F. Evidently, then, ordinary rapid cooling of castings
from the melted state results in both high combined carbon and high
'gamma' iron, and hence we have hardness due to both of these causes.
The more rapid the cooling, the higher the combined carbon and the
higher also the 'gamma' iron, therefore, since both var>' together, the
percentage of combined carbon is a satisfactor\' measure of the hardness
produced by both factors.
"If, now, the conditions of cooling are changed, this need no longer
be the case. For example, suppose we cool the casting slowly from the
molten state down to 1600° and then quench it in water. In this case
we would get nearly all combined carbon changed to graphite during the
slow cooling through the upper range, while the rapid cooling through
1300° preserves the 'gamma' iron solution and hence gives hardness due
to this cause.
Some of the peculiar things noted in connection with Custer's process
of casting in permanent moulds are to be explained on this basis. Also,
the much greater softness of castings which have been allowed to cool
in sand and thereby anneal themselves over those shaken out soon after
being poured.
"Chilled iron is simply while iron, that is, iron in which graphite is
absent and the carbon all in the combined or solution state. The same
iron may be both gray and white, depending on rate of cooling and hence
the exterior of the casting, if rapidly cooled, may be white while the
interior which cools more slowly remains gray. Usually there is an
Hardness
327
intermediate zone having a mottled structure formed through the inter-
lacing and the gradual merging of the gray and white. A chilling iron,
then, is one which when rapidly cooled contains all of its carbon in the
•combined state. The factors which influence the depth and quaUty
of chill are the temperature at which the iron is poured, and the amounts
of siUcon, sulphur and phosphorus, manganese and total carbon, besides
some of the elements which are not normally present in cast iron, but
which are occasionally added.
The higher the temperature at which iron is poured the deeper the
chill, other things being equal, and it is usually considered advisable to
pour chilled castings from hot iron. The quantitative effects of pouring
temperature have been studied by Adamson, and while there are some
conflicting results, it is in general indicated that in the case of the strongly
chifling irons an increase of 50° in the pouring temperature causes an
increase of from J-i to H inch in the depth of the chill.
The most important element in its effects on chill is silicon, which has
the strongest action in precipitating graphite. For chilling iron, silicon
should be low, but how low depends on the thickness of the casting, the
temperature of pouring and the depth of chill desired as well as on the
percentage of other elements in the iron. Table I gives a very approx-
imate relationship between the percentage of silicon and depth of chill,
other elements being about normal.
Table I. — Approximate Relation Between Per Cent
Silicon and Depth of Chill
Silicon,
per cent
Depth of
chill,
inch
Silicon,
per cent
Depth of
chill,
inch
%
H
I
1.50
1.25
1. 00
Ma
Ma
■ 75
.50
.40
Sulphur tends to increase the combined carbon, and, hence, the chill.
So marked is its influence in this respect that it is sometimes added
to cast iron to increase the depth of the chill. This, however, is not
usually good practice since the chill imparted by sulphur is lacking in
toughness and strength as well as in resistance to heat strains. Scott
cites the case of stamp shoes for mining machinery where sulphur was
used to increase the chill. The shoes were very hard at first, but soon
went to pieces under the repeated blows. Johnson, also, has noted the
great difference between high and low sulphur chilled iron as regards
328 Chemical Analyses
ubilily lu withstand the strains of sud<lcn cmilinj? without cracking. On
the other iiand, West states that the chill produced by sulphur is very
persistent to frictional wear, and, hence, it may be inferred that sulphur
adds t(> the life of castings which are subject to abrasion. It has been
stated that the presence of a small amount of sulphur is essential in order
to get the best results in chilled rolls. This, however, is doubtful and
it is believed that it is only rarely that sulphur is desirable in chilled
castings. The presence of a moderate amount of manganese in cast
iron greatly lessens the bad effects of sulphur in chilled as well aii in gray
iron castings.
"Phosphorus in the amounts ordinarily present in commercial cast
iron has but slight influence on the depth of the chill but does have a
more or less injurious effect on its strength. It is generally stated that
high phosphorus has the effect of causing a sharp line of demarkation
between the gray and chilled portions of the casting. . . . It is beheved
that it is best to limit the phosphorus in chilled iron to about 0.4 per cent.
Manganese, since it tends to increase the combined carbon, also tends
to increase the chill. However, it must be remembered that the first
effect of manganese is to neutralize sulphur, and, therefore, in small
amounts it may indirectly decrease the chill. Manganese very greatly
increases the hardness of the chill, and, to a less extent, its strength. It
also increases the resistance of the chill to heat strain and hence di-
minishes the danger of surface cracks in such castings as chilled rolls and
car wheels. Still another effect is the promotion of a more gradual
merging of the gray and chilled portions of the castings. Manganese
is usually considered a desirable constituent of chilled iron and the
amounts used var>^ all the way from 0.40 up to 3.0 per cent. . . .
Of late years, semi-steel mi.xtures have been used to some extent for
chilled castings, the total carbon being considerably lower than in the
ordinary mixture. The effect of low total carbon is to give a deep and
comparatively soft chill as compared with the shallow, hard chill obtained
with high total carbon.
"It has been proposed to use nickel as a means of controlUng chill,
this clement having an effect somewhat similar to silicon. Hence, by
starting with a strong chilling iron and adding nickel, the depth of the
chill would be lessened in some ratio to the amount of nickel added.
Since the same results may be oljlained by the use of less expensive
silicon it is difficult to see any advantage in adding nickel.
The quality of chilled iron may be very greatly improved by the
addition of small amounts of titanium or vanadium. The beneficial
effects of these elements are probably due chiefly to their deo.vidizing
power. . . .
Shrinkage 329
Grain Structxire
"The fracture or grain size and the porosity are closely related and
are both dependent primarily on the size of the graphite particles, and,
to a less extent, on the percentage of graphite.. . . .
Silicon should be kept just as low as possible and still have the cast-
ings soft enough to machine. The exact percentage will depend on
the thickness of the casting, the character of the mould and whether
the casting is allowed to anneal itself or is quickly shaken out after
pouring. It may range from 0.75 per cent for very heavy work up to
2.0 per cent for small valves, etc. It is believed that the majority of
founders use more silicon than is best in work of this character."
Combined carbon has a powerful action in closing the grain and giving
a dense iron and should be just as high as possible and still have the
iron machinable. . . .
Manganese had best be kept moderately high since it appears to have
some beneficial effect in closing the grain.
Sulphur is a powerful agent in closing the grain and is frequently
made purposely high for this end. It is, however, a dangerous agent
since it may cause trouble in other directions, and as a general proposi-
tion it is better to keep the sulphur low and get necessary density by a
proper regulation of silicon and manganese.
Finally, one of the best, if not the best, means of closing the grain
of cast iron and securing the maximmn density is by means of steel scrap
in the mixture. This is now common practice with makers of hydraulic
castings, and is very effective. . . .
Shrinkage
In considering the shrinkage of cast iron it is necessary to distinguish
between the contraction of the fluid mass previous to and during the act
of sohdifjang and the contraction of the solid mass. The first is that
form of shrinkage which necessitates feeding in heavy castings, and which
so often results in shrink holes or spongy places in hea\'y sections of
castings which are not fed. West calls this contraction of the fluid mass
' shrinkage. '
"The contraction of the solid mass represents more nearly what is
generally called shrinkage, this term as ordinarily used meaning the
difference in size between the casting and its pattern. This contraction
of the solid mass West calls 'contraction.'
"... It seems necessary to make some distinction between the
total amount of fluid contraction and the tendency to form shrink holes
in the heavy sections of small castings. At least there seems to be no
33° ("Inmical Analyst's
very (Icfinilc relation liclwccn clicmiial lomiMKiilion and this latter
projKJrty and it is often the case that an iron low in graphite and, there-
fore, having a high fluid contraction, will give sounder castings than
another iron high in graphite and which would, therefore, require less
fecfling in a large casting: ..."
"Cook has found that two irons (A practically identii^l chemical
composition may give very dilTcrent results as regards sjjundncss when
poured into small castings of heavy section and the writer can confirm
this fact from his own experience. A convenient test has been developed
by Cook to show the tendency of any particular brand of iron to trouble
of this sort. This test consists in making a casting in the shape of a K,
the branches having a cross section of one inch square. On breaking
off the oblique branches any tendency to sponginess or shrink holes will
at once be evident in the fracture."
"As before stated there has thus far been discovered no important
relationship between this property and chemical composition. It rather
appears to be something inherent in the brand of iron. . . . It is a
curious fact that, in some instances at least, the addition of a small
amoimt of steel scrap to the mixture will act as a partial corrective."
"The contraction of the solid mass does not take place uniformly as
the casting cools but in stages which are separated by periods of less
contraction or even of actual expansion. The total shrinkage which
perhaps includes also a portion of the shrinkage in the fluid mass is
conveniently obtained by Keep's test or by casting a test bar between
iron yokes and determining the space between the end of the bar and the
yoke after cooling."
"This, however, tells nothing as to the manner of shrinkage or the
temperature at which it takes place. To get this latter information we
must determine the shrinkage curve, or in other words, the length of the
test bar at each instant of time during cooling, starting from the instant
when the bar has solidified just enough to have some slight strength.
West, Keep and Turner have described forms of apparatus for making
these curves. Fig. 91 shows some t>T)ical shrinkage curs-cs and illus-
trates the relationship between chemical composition and the form of
these curves."
"It will be noted that there are three periods of expansion separated
by intervals during which the shrinkage takes place. The first of these
periods of expansion is due to the separation of graphite and hence is
greatest in the softest irons. Note that in the case .1 , which is a white
iron and contains no graphite, this expansion is entirely lacking. This
expansion takes place within the temperature range 2200° to 1800° F.,
or immediately after the iron has solidified."
Shrinkage
331
"The second expansion is due to the solidification of the phosphide
eutectic with a consequent secondary precipitation of graphite at that
time. Evidently, this expansion is only to be expected in high phos-
phorus irons and it will be noted that it is lacking in C, which is low in
phosphorus, and is well marked in D, which is high in phosphorus. This
expansion takes place within the temperature range 1800° to 1500° F."
"The third expansion is, in the writer's opinion, due to the change of
the iron from the 'alpha' to the 'gamma' form, since it takes place
&Z0
5)0
•4--0
20
X
£30
o
iO
-|2 50
c
■"60
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o>
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Sulphur tr. .01 .OS .03
- Phos. 0.01 .95 .04 .25-
Mang. tr .43 .55 .50
(orf^ f '•!'>' ^7? -"> ■"• i"^
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6rc
iph.Car
1
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2J3
1
2.55
1 ,
2.60
I _
50 100 150
Time- Seconds.
Fig. gi.
200
within the temperature range 1400° to 1200° F., or about where this
change would be expected to take place. Note that this expansion is
greatest in high silicon irons C and D, silicon having the effect of acceler-
ating the 'gamma' to 'alpha' change. The point at which this third
expansion occurs probably marks the lower limit below which iron cannot
be hardened by quenching."
"The study of these curves is very interesting to the experimenter
and it is believed that when we understand them better they may
become of practical value to the foundryman. At present, however,
333 Chimiral Analyses
ihc (Ictcrminalion of total shrinkage gives infcjrnialion which is of more
immidiatc value."
"The effect of composition on total shrinkage is given in concise- form
!)>• the following tabular statement:
I'cr cent
Silicon Decreases by about . oi inch per fo<ii for each . 20
Sulphur Increases by about .01 inch per foot for each .03
l'hus])horus. . . Decreases by about .015 inch per foot for each . 10
Manganese. . , . Increases by about . 01 inch per foot for each . 20
Total carbon Decreases.
"To get the minimum shrinkage an iron should be high in silicon,
from 2 to 3 per cent depending on the thickness, high in phosphorus, say.
0.75 to 1.25 per cent, as low as possible in sulphur, as high as possible in
total carbon and with only enough manganese to care for the sulphur,
or, say, 0.3 to 0.4 per cent. This will insure high graphite and hence low
shrinkage in the casting. The iron will, however, be rather weak and
it is something of a problem to get in one and the same iron considerable
strength and at the same time very low shrinkage."
" By the term ' stretch ' West describes the power of cast iron to stretch
when placed imder strain during the cooling process. This property is
undoubtedly of much importance in cast iron since there are many
castings which are called upon to exhibit it. An extreme case which
is commonly cited is that of pulleys, the arms of which are placed in
tension due to the quicker cooling of the rim and which must, therefore,
either stretch or crack. There is no data regarding the effect of various
metalloids of cast iron on its power of stretching but in general a soft iron
will stretch more than a hard one. Almost the only data on this subject
is given by West. He finds that the period of greatest stretching of
cast iron is within the temperature range i6cx>° to 1200° F.
Fusibility
Fusibility, or the melting point of cast iron, must not be confounded
with its fluidity, or ease of flow when molten. Fluidity is much the more
important of these two properties, but fusibility is of some interest,
particularly as it gives us a means of deciding intelligently in what order
to charge metals in the cupola.
The investigations of Dr. Moldenke have shown that the fusibility of
cast iron depends primarily on its combined carbon content, and, to a
less extent, on the amount of phosphorus present. . . . We find that
cast iron has a melting range wiPiTng from 2000° F. for a white iron up
to 2300° F. for gray iron containing practically no combined carbon, this
Fusibility
333
difference being due probably to the presence of silicon, sulphur, phos-
phorus and manganese.
Since the graphite in gray iron is only in mechanical mixture with the
iron we should, perhaps, expect it to have no effect on the melting point.
Moreover, it combines with the iron at temperatures below the melting
point thus increasing the combined carbon and lowering the melting
point. For this reason gray iron melts at a lower temperature than steel
having the same percentage of combined carbon.
2300
2250
2200
2150
E
£ 2100
2050
2000
x =
ffesj/
tsof
Drfli
7Mer
/ce.
s
s
V >t
%f
X
PI.6
,
\
■<Mn=
1.4
X'
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. Mn=
4
I.I
X
\
\
\
X
X
\
H
\
X
\
\
1^
2 3 4
Percent Combined Carbon.
Fig. 92.
As previously noted, phosphorus also has the effect of lowering the
melting point of cast iron but it is not nearly as powerful in its action as
combined carbon. Iron containing 6.7 per cent phosphorus would melt
at only 1740° F., but with less phosphorus than this the melting point
rises rapidly so that the i or 2 per cent present in commercial high phos-
phorus irons makes very little difference in the melting point.
Fig. 92 gives in graphic form the data of Dr. Moldenke from which
is drawn a line representing the approximate melting point of cast iron
of any per cent combined carbon.
334
Chemical Analyses
"Tiiblc I gives the melling jwints with analyses of some typical
irons and ferroalloys selected from the above data. It will be noted
that the metalloids other than carbon and phosphorus, i.e., the silicon,
sulphur and manganese, seem to have very little etlect on the melting
point."
Table I. — Melting Points of Cast Irons
Melting
Com-
point,
Graphite,
degrees F.
per cent
per cent
2030
3.98
aioo
352
.S4
2140
2.27
1.80
2170
1-93
l.f<>
2200
1.69
2.40
2210
1.48
2.30
2230
1. 12
2.66
2210
.84
307
2250
.80
3.16
2280
.13
3 43
2350
1.32
2210
6.48
(carbon)
2255
S.02
(carbon)
2190
3.38
■ 37
2040
1.82
• 47
2400
6.80
(carbon)
2280
Silicon,
per cent
.14
•47
• 4S
• 52
1. 81
1. 41
1. 13
2.58
1.29
2.40 .
.21
.14
i.6s
12.30
12.01
(chromium
62.70)
(tungsten
39^02)
Man-
Phos-
ganese,
phorus.
per cent
percent
.10
.22
.20
.20
1. 10
1.46
.16
.76
• 49
1.60
1.39
• 17
.24
.089
.47
2.12
• so
.22
■90
.oS
.49
(?)
4459
(?)
81.40
(?)
16.98
(?)
1.38
(?)
Sulphur,
per cent
037 pig iron
.036 " "
.032 " ••
.036 " "
.060 " '•
.033 " ■*
.027 " ■'
.osi '• "
.020 " "
.032
(?)
(?)
(?)
(?)
(?)
(?)
steel
ferromang.
ferromang.
silicospiegel.
ferrosilicon
ferrochrome
(?) ferrotungsten
Fluidity
"Fluidity may be defined as ease of flow. It is sjTionymoiis with
mobility and opposed to viscosity. It is a property of far-reaching
importance to the foundr>'man and especially to the manufacturer of
small and intricate castings. Unfortunately, our means of measuring
fluidity arc not very satisfactory', and this makes it dillicult to determine
quantitatively the eflect of composition upon this property. .Xbout
the most satisfactory method is to pour fluidity strips or long strips of
perhaps one square inch section (at one end) and tapering to nothing at
the other. The distance which the iron runs in a mold of this form is a
rough measure of its fluidity."
"The factors which govern fluidity are percentage of silicon, percent-
age of phosphorus, freedom from dissolved oxide and temperature above
the melting point."
"Silicon perhaps aids fluidity by causing a separation of graphite at
the moment of solidification, thus, according to Field, liberating latent
Resistance to Heat 335
heat and prolonging the Hfe of the metal. On this basis, high total
carbon would also aid fluidity by increasing the amount of graphite
separated."
"Phosphorus is probably the most important element as regards
fluidity, high phosphorus causing a marked increase in this property.
The best results are obtained with about 1.5 per cent phosphorus,
although for other reasons it is seldom desirable to use as much as that."
"Freedom from oxide is a very important point as its presence makes
the metal sluggish and causes it to set quickly. It is a frequent and often
unsuspected source of trouble. Dissolved oxide may be eliminated by
any of the methods described."
"The temperature above the freezing point is probably the most
important factor of all in connection with fluidity, and it should here be
noted that a distinction is made between freezing point and melting
point. The two may coincide in the case of white iron, but will not
usually, especially with gray iron. This is because, as we have already
seen, gray irons have a melting temperature corresponding to their per-
centage of combined carbon rather than total carbon. After they are
in the molten state, however, all the carbon is in solution (combined as
far as melting points are concerned), hence, the freezing point will corre-
spond more nearly to the melting point of a white iron having the per-
centage of combined carbon equal to the total carbon of the original gray
iron. This wiU be in general from 100° to 300° lower than its melting
point. For this reason when gray irons are melted they are always
considerably superheated above their sohdifying points, and the greater
this superheat, the more fluid the iron. Evidently, the superheat due
to this cause will be the greater the lower the combined carbon in the
iron going into the cupola."
Practical rules for getting fluid iron are as follows:
"Keep the phosphorus high, — up to i.oo to 1.25 if possible."
"If the work will permit, use a soft iron of 2 per cent or over in silicon,
and low in combined carbon."
"Avoid oxidizing conditions in melting and, if necessary, use deoxidiz-
ing agents."
"Use plenty of coke and good cupola practice."
Resistance to Heat
"Ability to withstand high temperatures is of paramount importance
in several classes of castings such as grate bars, ingot moulds, annealing
boxes, etc., and the factors which affect this ability are, the percentage
of phosphorus, sulphur and combined carbon, and the density or close-
ness of grain."
336 Chemical Analyses
"Phosphorus forms with iron an alloy which melts at only 1740° F.,or
about 400° lower than cast iron free from phosphorus, and each per cent
of phosphorus present gives rise to 15 per cent of this easily fusible con-
stituent. Now, it will be evident that the [iresence of a molten con-
stituent in a piece of iron must greatly weaken it, and hence it is that the
presence of much phosi)horus decreases the resistance of cast iron to
heat."
"Sulphur acts in a similar manner to phosphorus since it also form.s
with iron a constituent of low melting point (1780° F.). It is, therefore,
detrimental to castings which have to stand high temperatures."
"As prexnously noted, combined carbon is the element which more than
any other determines the melting point of cast iron, this melting point
becoming lower with increase in this element. It would seem then, that
combined carbon must be very detrimental in this class of castings.
However, it should be remembered that the condition of the carbon in
the solid iron changes readily at high temperatures, and, hence, after the
casting has been in use for a while its combined carbon content will not
in general be the same as when cast. This fact makes the question of
combined carbon of much less practical importance than either phos-
phorus or sulphur."
"Density or close grain is commonly stated to render cast iron con-
siderably more resistant to the effects of heat. ..."
"One feature of the effect of heat on cast iron which deserves especial
mention is the permanent expansion which it undergoes on repeated
heatings. This peculiar behavior was first discovered by Outerbridge
and has since been also investigated by Rugan and Carpenter."
"The extent to which this growth may take place is certainly sur-
prising, the increase being in some cases as high as 46 per cent by volume
and i?4 inches in the length of a 15-inch bar. The strength of the metal
is decreased proportionately to the expansion or to about one-half of the
original strength. Both the e.xpansion and the decrease in strength are
explained by microscopic examination, which shows minute cracks
throughout the interior of the metal. ..."
"Two conditions are necessary for this growth. First, repeated
heatings, and second, a proper composition of the metal."
"With regard to the heating, a minimum temperature of 1200" F. is
necessary. At 1400° to i6oo° the rate of growth is more rapid and an
increase in temperature beyond 1700° produces no additional effect.
Both heating and cooling are necessary to procure the growth, and the
time of heating makes very little difference. No greater growth was
produced by 17 hours continuous healing than by 4 hours. The num-
ber of heatings required to produce the maximum amount of growth
Resistance to Heat 337
varies with different irons, but usually lies somewhere between 50 and
100."
"Regarding the effects of composition, it appears that the growth is
favored bj- the presence of graphite and silicon, and also by a large grain
or open structure. \Yhite iron containing no graphite expands slightly
when subjected to this treatment but not sufficiently to overcome its
original shrinkage. In this case the expansion is due to the conversion
of the combined carbon into the temper form, or in other words, to the
malleableizing of the casting. Soft irons low in combined carbon and
high in silicon show the greatest increase in volume. The effects of
sulphur, manganese and phosphorus have not been investigated. Steel
and wrought iron are not subject to this growth, but on the contrary
undergo a slight permanent contraction when repeatedly heated."
"It is evident that this property of cast iron is of great importance in
many of the applications of the metal and limits its use for many pur-
poses. It is, no doubt, the reason why a close-grained iron gives better
results when exposed to high temperatures and affords an explanation
for the warping of grate bars, annealing boxes and similar castings. It
also shows why chills and permanent molds must not be allowed to be
heated to redness, such a degree of heat resulting in permanent expansion
and the loss of their original dimensions."
The following is a summary of some of the published statements
regarding the proper composition for castings exposed to high tempera-
tvires:
"Cast iron to withstand high temperatiures should be low in phos-
phorus and combined carbon."
"In car wheels manganese increases the resistance to heat strain."
"For refractory castings choose a fine grained cast iron, best contain-
ing about 2 per cent manganese to retard the separation of amorphous
carbon."
"Castings to resist heat should contain about 1.80 per cent silicon,
0.03 per cent sulphur, 0.70 per cent phosphorus, 0.60 per cent manganese
and 2.90 per cent total carbon. Low sulphur is of chief importance, low
silicon, carbon and manganese are also advisable."
"Close-grained cast iron having the greatest density will invariably
be found best to withstand chemical influences and high temperatures."
"A chill which had given excellent service had the following composi-
tion: silicon, 2.07 per cent; sulphur, 0.073 P^r cent; phosphorus, 0.03
per cent; manganese, 0.48 per cent; combined carbon, 0.23 per cent;
graphite carbon, 2.41 per cent; total carbon, 2.64 per cent.
"Two permanent mo vilds which had given excellent service analyzed
as follows:
338
Chemical Analyses
Silicon,
per cent
Sulphur,
per cent
.oS6
.070
Phosphorus,
per cent
Mancancae,
per cent
Combined
carbon,
per cent
Graphite,
per cent
carbon,
percent
a. IS
a.oa
I 26
.89
• 41
29
.13
.84
3.17
2.76
3. 30
3.60
"Ingot moulds and stools are best made from medium soft iron low in
phosphorus, or what is termed a regular Hessemcr iron. ..."
Electrical Properties
"Of the three electrical properties, conductivity, permeability and
hysteresis, the second only is of importance in connection with cast iron.
B
12.000
10,000
.,^-
^
e,ooo
*,
\%^-
'^
^
■^
--
^'
>^
K-
^''
^
6,000
•
,y
'7
y
4,000
/
Ij
/
if
/
2,000
1 /
if /
1/
EO 40 60
Fig. 93.
Little is known regarding the relation between chemical composition
and conductivity of cast iron. In the case of steel it has been found that
manganese is the element most injurious to this property with carbon
a close second. Hence, by analogy, we may infer that to make iron
castings of high conductiNTty we should keep both the manganese and
combined carbon as low as possible.
Electrical Properties
339
Permeability may be defined as magnetic conductivity and is of
importance in many castings used in the construction of electrical
machinery. Permeability data are generally given in the form of a
curve expressing the relation between the magnetizing force H and the
resulting field strength or number of lines of magnetic force per unit
area B. This is known as the permeability curve. The permeabihty
is the ratio — and it will be noted that it is different for each value of the
D
magnetizing force, H, but approaches a constant or saturation value for
high values of H. See Fig. 93.
160
024
r>'2
M
i
7
\
T
le
/'
13.
140
^^
--^
f^
^J^'
k-
/
/
10-^
L^
19
^7
■^
M
n
120
4
\
N
3. Sil. Phos. Mang.
1.79 .75 .19
-^
Z I.8J .75 .75
3 1.76 .75 1.73
♦ 1.81 .75 1.05
100
>'
& 1.76 .75 ^.46
1 I.7i .75 .35
5 ?7n 7? .-^f,
N
\
3 2.K .75 .35
0 IM .75 .36
1 3.67 .76 .36
80
\
5 1.49 .03 .75 .46
4 1.49 .16 .75 .49
\
6 im.ajs Ai
7 5.08 1.35 .75 .43
8 2.M3.I8.75 .43
60
e'
9 I.6Z .91 .47
0 1,69 l.n .49
U 1.63 1.75 .49
It 1.79 2.57 .5!
Vi 1.84 2.55 .52
24 1.76 2.61 .54
1.0
2.0 3.0
Fig. 94.
4.0
6.0
The effects of the various elements on permeability are not yet entirely
clear although there are some published data along this line. The writer
has recently done considerable work on the relation between permeabihty
and chemical composition of cast iron, and the results, as yet vmpublished,
are surmnarized in Fig. 94. It will be noted that the effects of silicon,
phosphorus and aluminum are not well marked and are probably not of
340 Chemical Analyses
any very great importance. On the other hand, manganese has a very
(Iclrinicntal ciTicl on lliis prupirly.
Sihcon has the oppobitu ellccl from manganese in that it accelerates
this change in the form of the iron, and we would, therefore, expect
it to have a more or less beneficial influence. Silicon steel has
achieved a wide rc|jutation as a high permeability material for use in
the construction of tran former cores, etc. .\ccording to tlic author's
results high silicon is particularly effective in increasing B for low values
of//.
An important clement nf)t considered in the diagram. Fig. 94, is
carbon. l"or high permeability the lower the carbon the better, and
excellent results are now being obtained through the use of semi-steel for
electrical castings. In this connection, however, it must be remembered
that manganese is undesirable and hence must be used cautiously as a
deoxidizer in this class of work.
Some practical rules for obtaining high permeability iron are given
herewith.
Keep the silicon high, best in the neighborhood of 3 per cent.
Keep the manganese low, preferably below 0.5 per cent.
If practicable keep the carbon low by the use of steel scrap or air
furnace iron.
Allow the castings to anneal themselves, i.e., cool completely in the
sand before shaking out.
Hysteresis, like conductivity, is seldom or never of importance in cast
iron. The property may be defined as the loss of energy due to molecular
friction when magnetic polarity is reversed. The effect of composition
upon hysteresis is in general about the same as in the case of permeability.
Resistance to Corrosion
Although there are a great many corrosive agencies it is not practicable,
because of lack of information, to treat of each separately, and so far as
we know the effects of composition would be relatively the same for the
various corroding agents.
The following is a summarj' of most of the published information
along this line:
Pig iron which best resists acids contains silicon, i.o per cent; phos-
phorus, 0.5 per cent; sulphur, 0.05 per cent; carbon, 3.0 per cent.
Excellent results wnth respect to resistance to corrosion by acids were
obtained through the use of a mixture of three brands of pig iron A, B
and C in the proportion, two parts of .1, one part B and one part C.
The analysis of the pig irons is thus given :
Resistance to Corrosion
341
Fracture
Silicon,
per cent
Manganese,
per cent
Phosphorus,
per cent
Total
carbon,
per cent
A Dark gray . ,
B Light Gray
C Mottled....
3. so
I so
.70
3.80
3.50
3.50
The composition of acid-resistant castings should be about as follows:
Silicon,
per cent
Sulphur,
per cent
Phosphorus,
per cent
Manganese,
per cent
Total carbon,
per cent
.8 to 2.0
.02 to .03
.40 to .60
I 0 to 2.0
30 to 3.5
and in addition, the metal should be as free as possible from oxide.
Cast iron to withstand the corrosive action of molten chemicals
should be close grained and dense. The iron having the greatest den-
sity will invariably be found to best withstand chemical influences and
high temperatures. The addition of deoxidizing agents is of great
benefit.
Gray iron is attacked by acids about three times as fast as white iron.
In cases where it is not practicable to use white iron castings it is some-
times possible to cast against chills in such a manner as to form a white
iron surface to resist corrosion and still leave the body of the casting
gray.
In a series of tests on the acid-resisting properties of some well-known
Enghsh brands of iron, the No. i iron, presumably high in silicon, and
the "hematite," low in phosphorus and probably high in silicon, gave the
best results.
Ferrosilicons with high percentages of silicon, 20 per cent and over, are
remarkably resistant to the effects of acids and are being made into
vessels for use in the chemical industries.
Sulphur has been found to be a source of corrosion in steel in some
instances, causing pitting at points where manganese sulphide has
segregated.
It has been shown that the presence of small amounts of copper in
steel and puddled iron diminish their tendency to rust.
Some practical rules for obtaining castings resistant to corrosion are
as follows:
Use white iron if practicable.
342 Chemicul Analyses
If not practicable to use white iron oistinK, chill those surfaces which
are to be in contact with the c (/rrosive substances.
If gray iron must be used get dense, close-grained castings through
the use of steel scrap or otherwise.
Avoid oxidized metal, use good cupola prai lice and good pig irons.
If possible use deoxidizing agents.
Keep the sulphur just as low as jwssiblc.
Resistance to Wear
We must first make some distinction between two cases of wear
typified by a grinding roll and a brake shoe. The first case may be
dismissed by the simple statement that the greater the hardness the
better the wear, providing at the same time that the iron is sufliciently
strong.
In the second case, however, it is necessary that the casting should not
be so hard as to unduly wear the material with which it comes in contact.
For example, the brake shoe must be softer than the tread of the car
wheel. There is no theory to guide us in the matter and the rules given
are the results of experiment chiefly with brake shoes.
Too much silicon gives an open, soft iron which does not wear well.
The best results are obtained with silicon about ils per cent in castings
of medium thickness.
Sulphur is claimed by many to be advantageous in castings for fric-
tional wear because it closes the grain and hardens somewhat. Diller
records a pecuUar occurrence of a hard spot which could not be machined,
a smooth surface being formed which wore the drill although it could be
dented with a center punch, .\nalysis showed 0.20 per cent sulphur and
0.50 per cent combined carbon.
Phosphorus is best kept moderately low. Most specifications call for
0.75 per cent or under. It is injurious probably because it weakens the
iron at the high temperature sometimes produced by friction. -
Manganese is best kept moderately high to take care of the sulphur.
Most brake shoe specifications call for under 0.70 per cent.
The addition of steel scrap to the mixture has been found to give
excellent results for this class of work, probably owing to the reduction
in the total carbon and to its action in closing the grain.
CoeflEicient of Friction
There are no data as to the relation between the composition of cast
iron and its coeflicient of friction. Since graphite is an excellent lubri-
cant it is probable that the percentage of graphite is the controlling
factor here, the friction decreasing with increase in this element. From
Casting Properties 343
theoretical considerations we should expect the best results to be obtained
\vith a very soft iron low in sulphur, manganese and combined carbon
and high in graphite.
Casting Properties
The properties which remain to be considered pertain more par-
ticularly to the casting as a whole and are chiefly influenced by the design,
moulding and pouring of the casting, and to a very much less extent, by
the composition of the metal.
Unsoundness due to the presence of blow-holes and shrinkage cavities,
while usually resulting from bad practice in moulding may also be caused
by poor quality of metal. Blowholes may be caused by oxidized metal
or by excessive sulphur. . . . When caused by sulphur the remedy is
to decrease this element. Raising the manganese is often effective in
preventing blowholes since it acts both as a deoxidizer and desulphiurizer.
Scott states that manganese below 0.25 per cent often results in blow-
holes. High phosphorus sometimes acts as a corrective of blowholes due
to its prolonging the fluidity, thus giving the iron more chance to release
the dissolved gases.
Dirty castings are also caused chiefly by poor moulding, pouring or
cupola practice. Occasionally, however, it may result from wrong
composition of the metal, and the points chiefly to be watched are to keep
the sulphur low; to avoid kish or segregated graphite and to avoid
oxidized metal.
Sulphur tends to cause dirty castings because it makes the iron congeal
more quickly, and hence any dirt present has less chance to separate.
In addition, the sulphides of iron and manganese themselves form dirt
spots when segregated. Kish is usually caused by too much silicon, or
sometimes by too much total carbon. Oxidized metal is a prolific source
of dirty castings, but the oxidization is usually due to bad cupola practice,
or to the use of oxidized scrap. IModerately high manganese and phos-
phorus are conducive to clean castings, the first because it takes care of
sulphur and oxidation, and the second because it increases the fluidity of
the metal and thus gives the dirt a better chance to float out.
Porosity is usually caused by the presence of kish (see preceding
paragraph). Pinholes, another form of porosity, are usually due to
excessive sulphur in the form of iron sulphide. This compound retains
gases in solution until the metal is partially frozen and then releases
them in the form of tiny bubbles which give rise to this defect. Decrease
in sulphur or increase in manganese or both is the remedy.
Segregation proper is caused by the difference in melting point and
specific gravity of the several constituents of cast iron. The constit-
344 Chemical Analyses
ucnls of lowest melting point arc the phosphorus ami sulphur compounds,
and it is, therefore, in these cases that we find the greatest tendency
towards segregation. It is not unusual to find hard s[xjts in heavy
castings high in phos|)h<)rus which are caused Ijy the phosphide lx:ing
squeezed out into blow-hulcs formed during solidification. Frequently
the phosphide does not completely fill the cavity, or fills it as a loose
globule. The sulphides, owing to their low specific gravity, usually
segregate in the top of the casting and it is not infrequent to find sev-
eral times the normal amount of sulphur in the upper part of heavy
castings. Manganese sulphide segregates more readily than iron sul-
phide.
Besides segregation proper we sometimes find cases of non-homo-
gencily due to other causes. Occasionally spots of white iron are found
in the interior of castings. It has always been diflicult to account for
these but the clew is given by the fact that they are invariably found in
castings poured from the first metal tapped.
Undoubtedly they are caused by the iron boiling on the sand bed and
are connected in some way with the partial Bessemerizing of the metal.
Again, hard spots in castings are sometimes due to small pieces of metal
(for example, small steel scrap and shot iron) being incompletely melted
in their passage through the cupola. Ferromanganese and other ferro-
alloys may give rise to this same trouble through incomplete solution
when stirred into the ladle.
Shrinkage strains are caused primarily by ^vTongly designed castings,
but the trouble may be aggravated by the composition of the metal.
High sulphur is a particularly prolific source of internal stresses, and,
in general, the greater the total shrinkage, the greater the strains due to
this cause.
As all foundr>'men know, the fineness of finish and smoothness of skin
of a casting depend chiefly on the sands and facings used and the skill
of the moulder. High phosphorus in the iron, however, is a consider-
able aid in getting the fine skin desired in ornamental work, .\nother
element affecting the skin is manganese which has the rather peculiar
action of causing the sand to peel from the castings with extreme readi-
ness. With I per cent manganese this tendency is CNident and with
2 per cent it is verj' marked.
Bars, plates and hollow castings were treated, which were permitted
to cool in the moulds. The plates cooled more slowly than the bar
samples and the material proved somcv.'hat softer, givnng smaller values
for the bending, tensile and compressive strength, but was better as
regards flexiu-e and strength to resist impact.
Tests reported to the Iron and Steel Institute showed:
Notes on the Micro-structure of Cast Iron 345
The best tensile and transverse tests are obtained from bars which
have been machined.
Transverse test bars cast on edge and tested with the "fin" in com-
pression give the best results.
The transverse test is not so reliable or helpful as that of the moment
of resistance.
Cast iron gives the best results when poured as hot as possible.
As in some measure explanatory of the conflicting results obtained in
testing bars of precisely the same chemical combination, and as showing
the importance of microscopical examinations of the structure of cast
iron in pointing out the causes of difference in its physical properties, the
paper of Mr. Percy Longmuir published in the Journal of the American
Foundrymen's Association, June, 1903 is given in full.
Notes on the Micro-structure of Cast Iron
By Percy Longmtjir, Sheffield, England
Journal of the American Foundrymen's Association, Vol. XII, June, IQ03.
Instances are occasionally found where metal of the right chemical
composition goes wrong in practice. It is in cases of this kind that the
real value of microscopical examination is most evident, for very often
such an examination will locate the trouble and at the same time suggest
a remedy. Naturally an examination of diseased samples can only be
undertaken after a thorough study of healthy ones, hence a foundation
for the study of abnormal samples must necessarily be based on the,
knowledge gained from a wide series of normal ones, that is, samples of
knowTi chemical composition and known physical conditions.
The structure of cast iron is very complex — far more so than that of
steel — a fact readily shown by the high content of elements present
other than iron. By polishing and etching a sample of cast iron, several
of the compounds of the elements with iron are, under suitable magni-
fication, rendered visible. The structural features, such as the arrange-
ment and distribution of the various compounds and their relationship
to each other, can then be readily noted and the effect of this combination
on the mass then becomes an estimable quantity.
If the metal under examination contain no impurities it is evident that
its mass will be built up of pure crystals. A section cut from such a pvure
metal will, after polishing and etching, show only the crystal junctions.
Crystal junctions of this type are shown in Fig. 95 , which represents the
structure of almost pure iron. Even here, although the metal is so pure,
the very minute trace of carbon present can be readily detected in the
dark knots of which about a dozen are to be seen. As foreign elements
346
Chemical Analyses
arc added to pure iron the structure becomes more complex and a point
is reached when all the pure crystals are rejilaced by more complex ones.
It is to be remembered that all Kt^ay irons contain appreciable amounts
of two varieties of carbon, silicon, manKancse, sulphur and phosphonis.
Fig. gs. — Magnified 360 diameters.
Carbon 0.03 Sulphur o.oi
Silicon 0.02 Phosphorus o.oi
Manganese 0.07 Iron 99.86
Of these elements graphite is present m its elementary form, that is, as
free carbon. The remaining constituents are present in compound form
associated either with iron or with other elements. Thus sulphur may
occur as sulphide of manganese or as iron sulphide. Carbon occurring
Fig. g6. — Magnified 60 diameters.
Combined Carbon 0.54 Manganese 0.63
Graphite 3. 11 Sulphur 0.04
Silicon 1.77 Phosphorus 1.34
in the combined form is present as a definite carbide of iron; or under
certain conditions as a double carbide of iron and manganese. Phos-
phorus is associated with iron as a definite phosphide. These compounds
are all distinguisliable under suitable magnification, but the association
of silicon and iron is, so far as present knowledge goes, unrecognizable.
Notes on the Micro-structure of Cast Iron
347
Microscopically these constituents have received other names — for
instance pmre iron is known as "ferrite," hence a structure similar to
that of Fig. 96 consists almost entirely of ferrite. Combined carbon
.receives the term "cementite" and a mixture of cementite and ferrite
Fig. 97. — Magnified 460 diameters. Fig. 98. — Magnified 360 diameters.
is known as "pearlite." Pearlite often consists of alternate striae of
cementite and ferrite and in such a form gives a magnificent play of
colors resembling those of mother-of-pearl , consequently this constituent
was named by its discoverer, Dr. Sorby, the "pearly constituent," a term
now contracted to "pearlite."
Fig. 99. — Magnified 50 diameters.
Combined Carbon 3.25 Sulphur 0.41
Silicon 0.78 Phosphorus 0.06
Manganese o . 09
The classical researches of Professor Arnold have conclusively shown
that iron containing 0.89 per cent carbon consists entirely of pearlite.
As the content of carbon increases above 0.89 per cent, structurally free
cementite appears increasing in quantity with each increment of carbon.
It therefore follows that a white cast iron will consist essentially of
34^ Chemical Analyst's
rcmunlitc and pcarlilc. in llie miijorily of gray irons used in the found-
ries the a)ml)incd carbon is well below 0.89 per cent — cementite is,
therefore, only present as a constituent of pcarlitc.
Suli^hide kIoIjuIcs when in the form of manganese sulphide show a light
gray color, while iron sulphide shows a hght brown tint.
In high sulphur irons the sulphide lends to envelop the crystals; a
section cut fmm sucii an iron would show a network of sulphide following
the crystal junctions and destroying their continuity. These sulphides
have been thoroughl>' in\x'stigatcd by Professor Arnold whose researches
have thrown much light on the behaviour of both iron and manganese
sulphide.
The relations ol iron and phosphorus have been very thoroughly
studied by Mr. J. E. Stead. In September, 1900, Mr. Stead presented
Fig. ICX5. — Magnified 50 diameters.
Combined Carbon 0.82 Manganese 0.09
Graphite 2.07 Sulphur 0.37
Silicon 0.75 Phosphorus 0.07
before the Iron and Steel Institute a most exhaustive research on this
subject. With ordinarj' pig irons the phosphide of iron appears to be
rejected to a eutectic of uncertain composition. Eutectic may for our
purpose be defined as that portion last to soUdify. This phosphide
eutectic may be readily distinguished in all gray irons by an ordinary
etching medium, but in while irons containing structurally free cementite,
Mr. Stead's "heat tinting" process becomes necessary to distinguish the
eutectic from the cementite.
Fig. 96 reproduces a photo-microscope of an unetched section of gray
iron at a magnification of 60 diameters.
This magnification gives, as it were, a general view only — to get at the
ultimate structure higher powers must be used. Fig. 97 represents the
structure of an ordinary gray iron magnified 460 diameters. The larger
Notes on the Micro-structure of Cast Iron
349
portion of this field consists of pearlite embedded in which are irregular
areas of the phosphide eutectic and several notable black plates of
graphite. The, phosphide eutectic is recognizable by its irregular shape
and broken up structure; an area in the center of the photograph enclos-
ing an area of pearlite is worthy of notice.
Fig. 98 reproduces an area of phosphide eutectic from the same section
as Fig. 96.
A tj^ical .white cast iron consisting essentially of pearlite and cementite
is shown in Fig. 99. This is a type of iron used as a base for the production
of malleable cast iron.
The influences of annealing are shown in Fig. 100, which represents the
same iron as Fig. 99, after going through the ordinary malleable iron
Fig.
Magnified 60 diameters.
annealing in ore. This section consists essentially of pearlite and
graphite — the analyses appended to each figure showing the change in
carbon condition. For the loan of the negatives illustrating Figs. 99
and 100, the writer is indebted to the courtesy of Mr. T. Baker, B. Sc.
Quite apart from the clear light thrown on what has been aptly termed
the internal architecture of a metal, microscopical examination reveals
many other features of profitable interest, one notable feature being the
examination of minute flaws. Space will not permit of many illustra-
tions under this head, but Fig. loi, reproduced from a photo-micrograph
of a pin-hole in the same section as Fig. 96, will show the range of possi-
bility in this direction. Obviously, a study of flaws of this character
offers much to the founder producing castings which have to meet a
hydraulic or high steam pressure test.
(11 AI'IKk XIV
Standard Specifications for Cast Iron Car Wheels
Chemical Properties
Tin: wheels furnished under this specification must liC mudc from the
best materials and in accordance with the best foundry methods. The
following pattern analysis is given for information, as representing
the chemical properties of a good cast iron wheel. Successful wheels,
var\-ing in some of the constituents quite considerably from the figures
given, may be made:
Analysis
Per cent
Analysis
Per cent
3. SO
2.90
.60
.70
Manganese
Phosphorus
Sulphur
Graphitic carbon
oS
1. Wheels will be inspected and tested at the place of manufacture.
2. All wheels must conform in general design and in measurements
to drawings which will be furnished, and any departure from the stand-
ard drawing must be by special permission in writing. Manufacturers
wishing to deviate from the standard dimensions must submit duplicate
drawings showing the proposed changes, which must be approved.
Drop Tests
3. The following table gives data as to weight and tests of various
kinds of wheels for different kinds of cars and service:
Wheel
33-inch diameter freight and pas-
senger cars
36-inch diameter
Kind of service... j
60.000 lbs.
capacity
and less
I
600
70,000 lbs.
capacity
2
650
100,000 lbs.
capacity
3
700
Passenger
cars
A
700 lbs.
Locomotive
tenders
s
f Desired . . .
Weight ]
[ Variation .
7Solbs.
Two per cent either way
Height of drop. feet.
Number of blows ..
9 12 12
10 10 12
12
12
la
14
35°
Material and Chill 351
Marking
4. Each wheel must have plainly cast on the outside plate the name
of the maker and place of manufacture. Each wheel must also have
cast on the inside double plate the date of casting and a serial foimdry
nimiber. The manufacturer must also provide for the guarantee mark,
if so required by the contract. No wheel bearing a duplicate number, or
a number which has once been passed upon, will be considered. Num-
bers of wheels once rejected will remain uniilled. No wheel bearing an
indistinct number or date, or any evidence of an altered or defaced
number will be considered.
Measures
5. All wheels offered for inspection must have been measured with a
standard tape measure and must have the shrinkage number stenciled
in plain figures on the inside of the wheel. The standard tape measure
must correspond in form and construction to the "Wheel Circumference
Measure" established by the Master Car Builders' Association in 1900.
The nomenclature of that measure need not, however, be followed, it
being sufficient if the graduating marks indicating tape sizes are one-
eighth of an inch apart. Any convenient method of showing the shrink-
age or stencil number may be employed. Experience shows that
standard tape measures elongate a little with use, and it is essential to
have them frequently compared and rectified. When ready for inspec-
tion, the wheels must be arranged in rows according to shrinkage numbers,
all wheels of the same date being grouped together. Wheels bearing
dates more than thirty days prior to the date of inspection will not be
accepted for test, except by permission. For any single inspection and
test, only wheels having three consecutive shrinkage or stencil numbers
will be considered. The manufacturer will, of course, decide what three
shrinkage or stencil numbers he will submit in any given lot of 103 wheels
offered, and the same three shrinkage or stencil numbers need not be
offered each time.
Finish
6. The body of the wheels must be smooth and free from slag and
blowholes, and the hubs must be solid. Wheels will not be rejected
because of drawing around the center core. The tread and throat of the
wheels must be smooth, free from deep and irregular wrinkles, slag, sand
wash, chill cracks or swollen rims, and be free from any evidence of hollow
rims, and the throat and tread must be practically free from sweat.
Material and Chill
7. Wheels tested must show soft, clean, gray iron, free from defects,
such as holes containing slag or dirt more than one-quarter of an inch in
352 Slundard Specifications for Cast Iron Car \\ beds
di;imclcr, or clusters of such holes, honeycombing of iron in the hub,
while iron in the |)lales or hub, or clear white iron around the anchors of
chaplcls at a greater distance than one-half of an inch in any direction.
The dc|)th of the clear white iron must not exceed seven-eighths of an
indi at the throat an<l one inch at the middle of the tread, nor must it be
less than three-eighths of an inch at the throat or any part of the tread.
The blending of the white iron with the gray iron behind must be without
any distinct line of demarcation, and the iron mu.st not have a mottled
appMiarancc in any part of the wheel at a greater distance than one and
five-cighlhs inches from tlic tread or throat. The depth of chill will Ijc
determined by inspection of the three test wheels described below, all
test wheels being broken for this purpose, if necessary. If one only of
the three test wheels fails in limits of chill, all the lot under test of the
same shrinkage or stencil number will be rejected and the test will be
regarded as finished so far as this lot of 103 wheeb is concerned. The
manufacturer may, however, offer the wheels of the other two shrinkage
or stencil numbers, provided they are acceptable in other respects as
constituents of another 103 wheels for a subsequent test. If two of the
three test wheels fail in limits of chill, the wheels in the lot of 103 of the
same shrinkage or stencil number as these two wheels will be rejected,
and, as before, the test will be regarded as finished as far as this lot of
103 wheels is concerned. The manufacturer may, however, offer the
wheels of the third shrinkage or stencil number, provided they are
acceptable in other respects, as constituents of another 103 wheels for
a subsequent test. If all three test wheels fail in limits of chill, of course
the whole hundred will be rejected.
Inspection and Shipping
8. The manufacturer must notify when he is ready to ship not less
than 100 wheels; must await the arrival of the inspector; must have a
car, or cars, ready to be loaded with wheels, and must furnish facilities
and labor to enable the Inspector to inspect, test, load and ship the
wheels promptly. \\'heels offered for inspection must not be covered
with any substance which will hide defects.
9. One hundred or more wheels being ready for test, the inspector will
make a list of the wheel numbers, at the same time examining each wheel
for defects. .\ny wheels which fail to conform to specifications by
reason of defects must be laid aside, and such wheels will not be accepted
for shipment. As individual wheels are rejected, others of the proper
shrinkage or stencil number may be offered to keep the number
good.
Thermal Test 353
Retaping
10. The inspector will retape not less than 10 per cent of the wheels
offered for test, and if he finds any showing wrong tape-marking, he will
tape the whole lot and require them to be restenciled, at the same time
having the old stencil marks obliterated. He will weigh and make check
measurements of at least 10 per cent of the wheels offered for test, and
if any of these wheels fail to conform to the specification, he will weigh
and measure the whole lot, refusing to accept for shipment any wheels
which fail in these respects.
Drop Tests
11. Experience indicates that wheels with higher shrinkage or lower
stencil numbers are more apt to fail on thermal test; more apt to fail
on drop test and more apt to exceed the maximum allowable chill than
those with higher stencil or lower shrinkage numbers; while, on the
other hand, wheels with higher stencil or lower shrinkage numbers are
more apt to be deficient in chill. For each 103 wheels apparently
acceptable, the inspector will select three wheels for test — one from
each of the three shrinkage or stencil numbers offered. One of these
wheels chosen for this purpose by the inspector must be tested by drop
test as follows: The wheel must be placed flange downward in an anvil
block weighing not less than 1700 pounds, set on rubble masonry two
feet deep and having three supports not more than five inches wide for
the flange of the wheel to rest on. It must be struck centrally upon the
hub by a weight of 200 pounds, falUng from a height as shown in the
table on page 350. The end of the faUing weight must be flat, so as to
strike fairly on the hub, and when by wear the bottom of the weight
assumes a round or conical form, it must be replaced. The machine for
making this test is shown on drawings which wiU be furnished. Should
the wheel stand, without breaking in two or more pieces, the number of
blows shown in the above table, the one hundred wheels represented by
it will be considered satisfactory as to this test. Should it fail, the whole
hundred will be rejected.
Thermal Test
12. The other two test wheels must be tested as follows: The wheels
must be laid flange down in the sand, and a channel way one and one-half
inches in width at the center of the tread and four inches deep must be
molded with green sand around the wheel. The clean tread of the wheel
must form one side of this channel way, and the clean flange must form
as much of the bottom as its width will cover. The channel way must
354 Standard Specifications for Cast Iron Car Wheels
ihcii l>c fillud l<) the toj) from <»nc ladle with molten cast iron, which must
he jKiuretl direi tly into the channel way without previous cooling or
stirring, and this iron must be so hot, when |)ourcd, that the ring which
is formed when the metal is cold shall be solid or free from wrinkles or
layers. Iron at this temperature will usually cut a hole at the jjoint of
impact with the flange. In order to avoid spitting during the pouring,
the tread and inside of the flange during the thermal test should be
covered with a coat of shellac; wheels which are wet or which have been
exposed to snow or frost maybe warmed sufficiently to dry them or
remove the frost before testing, but under no circumstances must the
thermal test be applied to a wheel that in any part feels warm tn th<-'
liand. The time when pouring ceases must be noted, and two minutes
later an examination of the wheel under test must be made. If the wheel
is found broken in pieces, or if any crack in the plates extends through
or into the tread, the test wheel will be regarded as having failed. If
both wheels stand, the whole hundred will be accepted as to this test.
If both fail, the whole hundred will be rejected. If one only of the ther-
mal lest wheels fails, all of the lot under test of the same shrinkage or
stencil number will be rejected, and the test will be regarded as finished,
so far as this lot of wheels is concerned. The manufacturer may, however,
offer the wheels of the other two shrinkage or stencil numbers, provided
I hey are acceptable in other respects, as constituents of another 103
wheels for a subsequent test.
Storing and Shipping
13. All wheels which pass inspection and test will be regarded as
accepted, and may be either shipped or stored for future shipment, as
arranged. It is desired that shipments should be, as far as possible, in
lots of 100 wheels. In all cases the inspector must witness the shipment,
and he must give, in his report, the. numbers of all wheels inspected and
I he disposition made of them.
Rejections
14. Individual wheels will be considered to have failed and will not
!)c accepted or further considered, which.
First. Do not conform to standard design and measurement.
Second. Are under or over weight.
Third. Have the physical defects described in Section 6.
15. Each 103 wheels submitted for test will be considered to have
failed and will not be accepted or considered further, if,
First. The test wheels do not conform to Section 7, especially as to
limits of white iron in the throat and tread and around chaplets.
Standard Specifications for Locomotive Cylinders 355
Second. One of the test wheels does not stand the drop test as de
scribed in Section 11.
Third. Both of the two test wheels do not stand the thermal test as
described in Section 12.
Standard Specifications for Locomotive Cylinders
Process of Manufacture
Locomotive cylinders shall be made from a good quahty of close-grained
gray iron cast in a dry sand mould.
Chemical Properties
Drillings taken from test pieces cast as hereafter mentioned shall
conform to the following limits in chemical composition:
Silicon from 1.25 to i . 75 per cent
Phosphorus not over o . 90 per cent
Sulphur not over o. 10 per cent
Physical Properties
The minimum physical qualities for cylinder iron shall be as follows:
The "Arbitration Test Bar," i!4 inches in diameter, with supports
12 inches apart, shall have a transverse strength not less than 3000
pounds, centrally applied, and a deflection not less than o.io of an inch.
Test Pieces and Method of Testing
The standard test-bar shall be iV* inches in diameter, about 14 inches
long, cast on end in dry sand. The drillings for analysis shall be taken
from this test piece, but in case of rejection the manufacturer shall have
the option of analyzing drilhngs from the bore of the cylinder, upon
which analysis the acceptance or rejection of the cylinder shall be based.
One test piece for each cylinder shall be required.
Character of Castings
Castings shall be smooth, well cleaned, free from blow-holes, shrinkage
cracks or other defects, and must finish to blue-print size.
Each cylinder shall have cast on each side of saddle, the manufacturer's
mark, serial number, date made and mark showing order number.
Inspector
The inspector representing the purchaser shall have all reasonable
facihties afforded to him bj^ the manufacturer to satisfy himself that the
finished material is furnished in accordance with these specifications.
All tests and inspections shall be made at the place of the manufacturer.
3s6 Stanthird SiK'cificaliuns for Cast Iron \'\\>c
Standard Specifications for Cast-Iron Pipe and
Special Castings
Drs(rif>li(in of Pipes
The pipes shall be made with hub and spigot joints, and shall accurately
conform to the dimensions given in tablas Xos. I and II. They shall be
straight and shall be true circles in section, with their inner and outer
surfaces concentric, and shall be of the specified dimensions in outside
diameter. They shall be at least 12 feet in length, exclusive of socket.
For pipes of each size from 4-inch to 24-inch, inclusive, there shall be two
standards of outside diameter, and for pipes from 30-inch to 60-inch,
inclusive, there shall be four standards of outside diameter, as shown by
table No. II.
All pipes having the same outside diameter shall have the same inside
diameter at both ends. The inside diameter of the lighter pipes of each
standard outside diameter shall be gradually increased for a distance of
about 6 inches from each end of the pipe so as to obtain the required
standard thickness and weight for each size and class of pipe.
Pipes whose standard thickness and weight are intermediate between
the classes in table No. II shall be made of the same outside diameter as
the next heavier class. Pipes whose standard thickness and weight are
less than shown by table No. II shall be made of the same outside diam-
eter as the class A pipes, and pipes whose thickness and weight are more
than shown by table No. II shall be made of the same outside diameter
as the class D pipes.
For 4-inch to 12-inch pipes, inclusive, one class of special castings
shall be furnished, made from class D pattern. Those having spigot
ends shall have outside diameters of spigot ends midwaj- between the
two standards of outside diameters as shown by table No. II, and shall be
tapered back for a distance of 6 inches. For 14-inch to 24-inch pipes,
inclusive, two classes of special castings shall be furnished, class B spe-
cial castings with classes A and B pipes, and class D special castings
with classes C and D pipes, the former to be stamped "AB" and the
latter to be stamped "CD." For 30-inch to 60-inch pipes, inclusive,
four classes of special castings shall be furnished, one for each class of
pipe, and shall be stamped with the letter of the class to which they
belong.
Allowable Variation in Diameter of Pipes and Sockets
Especial care shall be taken to have the sockets of the required size.
The sockets and spigots will be tested by circular gauges, and no pipe will
be received which is defective in joint room from any cause. The diam-
eters of the sockets and the outside diameters of the bead ends of the
Special Castings 357
pipes shall not vary from the standard dimensions by more than 0.06
of an inch for pipes 16 inches or less in diameter; 0.08 of an inch for
18-inch, 20-inch and 24-inch pipes; o.io of an inch for 30-inch, 36-inch
and 42-inch pipes; 0.12 of an inch for 48-inch, and 0.15 of an inch for
54-inch and 60-inch pipes.
Allowable Variation in Thickness
For pipes whose standard thickness is less than i inch, the thickness of
metal in the body of the pipe shall not be more than 0.08 of an inch less
than the standard thickness, and for pipes whose standard thickness is
I inch or more, the variation shall not exceed o.io of an inch, except that
for spaces not exceeding 8 inches in length in any direction, variations
from the standard thickness of 0.02 of an inch in excess of the allowance
above given shall be permitted.
For special castings of standard patterns a variation of 50 per cent
greater than allowed for straight pipe shall be permitted.
Defective Spigots may be Cut
Defective spigot ends on pipes 12 inches or more in diameter may be
cut off in a lathe and a half-round wrought-iron band shrunk into a
groove cut in the end of the pipe. Not more than 1 2 per cent of the total
number of accepted pipes of each size shall be cut and banded, and no
pipe shall be banded which is less than 1 1 feet in length, exclusive of the
socket.
In case the length of a pipe differs from 12 feet, the standard weight
of the pipe given in table No. II shall be modified in accordance therewith.
Special Castings
All special castings shall be made in accordance with the cuts and the
dimensions given in the table forming a part of these specifications.
The diameters of the sockets and the external diameters of the bead
ends of the special castings shall not vary from the standard dimensions
by more than 0.12 of an inch for castings 16 inches or less in diameter;
0.15 of an inch for 18-inch, 20-inch and 24-inch castings; 0.20 of an inch
for 30-inch, 36-inch and 42-inch castings; and 0.24 of an inch for 48-
inch, S4-inch and 60-inch castings. These variations apply only to
special castings made from standard patterns.
The flanges on all manhole castings and manhole covers shall be faced
true and smooth, and drilled to receive bolts of the sizes given in the
tables. The manufacturer shall furnish and deliver all bolts for bolting
on the manhole covers, the bolts to be of the sizes shown on plans and
made of the best quality of mild steel, with hexagonal heads and nuts
and sound, well-fitting threads.
35^
Suindurd SjKJcifications for Cast Iron I'iix;
Table No. I. — Gkneral Dimensions ok I'ipes
Classes
A-B
C-D
A-B
C-D
c-b
A-B
C-D
A-B
C-D
A-B
C-D
A-B
C-
A-B
C-D
A-B
C-D
A-B
C-D
A
B
C
D
A
B
C
D
A
B
C
D
A
B
C
D
A
B
C
D
A
B
C
D
Actual
outside
diam.,
inches
4.80
S 00
6.90
7.10
9 05
9.30
II. 10
11.40
13.20
13. so
15 30
15.65
17.40
17.80
19-50
19.92
21.60
22.06
25.80
26.32
31.74
32.00
32.40
32.74
37.96
38.30
38.70
39-16
44.20
44.50
45. 10
45.58
50.50
50.80
51 .10
SI. 08
56.66
57.10
57.80
58.40
62.80
63.40
64.20
64.82
Diameter of
sockets
Pipe,
inches
5. 60
5.80
7.70
7.90
9.8s
10.10
11.90
12.20
14.00
14.30
16.10
16.4s
18.40
18.80
20.50
20.92
22.60
23.06
26.80
27.32
32.74
33.00
33-4J
33-74
38.96
39.30
39.70
40.16
45.20
45.50
46.10
46.58
51.50
51.80
52.. JO
52.98
57.66
58.10
58.80
59 40
63.80
64.40
65.20
65 82
Special
castings,
inches
5.70
5.70
7.80
7.80
10.00
10.00
12.10
12.10
14.20
14.20
16.10
16.4s
18.40
18.80
20.50
20.92
22.60
23.06
26.80
27.32
32.74
33.00
33.40
33.74
38.96
39 30
39.70
40.16
45 20
45.50
46.10
46.58
51.50
51 80
52.40
52.98
57.66
S8.10
58.80
59 40
63.80
64.40
65 20
65 82
Depth of
sockets
Pipe,
inches
3. so
3 50
3.50
3 SO
4.00
4.00
4.00
4. CO
4.00
4.00
4.00
4 00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4 SO
4.50
4.50
4.50
4.50
4.50
4.50
4.50
5.00
5.00
5.00
5. 00
5 00
5.00
5.00
5 00
5. SO
5 50
5 .so
5 50
S 50
5 50
S SO
S 50
Special
castings
inches
4.00
4.00
4 00
4 00
4.00
4.00
4.00
4 00
4.00
4.00
4.00
4 00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.00
4.50
4.50
4.50
4.50
4 so
4.50
4.50
4.50
5 00
5.00
5.00
5 00
5. 00
5.00
5.00
5 00
S.so
SSo
5 50
5. SO
5. 50
5. 50
5.50
5.50
A
B
15
1 30
1.5
1.30
IS
1.40
IS
1.40
IS
I-So
IS
I. SO
I-S
I SO
1.5
1.60
I-S
1.60
I.S
1.70
IS
1.70
IS
1.80
1.7s
1.80
I-7S
1-90
1. 75
I 90
I.7S
3.10
I.7S
2.00
1. 75
2.30
2 00
3 10
3.00
3. SO
2.00
2-SO
2.00
2.30
3.00
2.60
2.00
3 00
2.00
3. SO
2.00
3. 80
2.00
3.10
2.00
3 40
2 00
3.80
2.00
3.00
3.00
3.40
2.00
380
2.00
3.00
2.00
3 30
2.00
3.80
2.00
4.20
2.25
3 20
2.25
3.60
2 23
4 00
2 25
4 40
2.25
3 40
2 25
3 70
2.25
4 20
2-25
4-70
Standard Specifications for Cast Iron Pipe
359
Table No. II. — Standard Thicknesses and Weights of
Cast Iron Pipe
Class A
Class B
'Nominal
100 ft. head. 43 lbs.
pressure
200 ft. head. 86 lbs. pressure
inside
diameter,
. inches
Thickness,
inches
Weight per
Thickness,
inches
Weight per
Foot
Length
Foot
Length
4
.42
20.0
240
.45
21.7
260
6
.44
30.8
370
.48
33.3
400
8
.46
42.9
515
51
47-5
570
lO
.50
57.1
685
.57
63-8
765
12
.54
72.5
870
.62
82.1
98s
14
.57
89.6
1.075
.66
102. s
1.230
i6
.60
108.3
1,300
.70
125.0
1.500
i8
.64
129.2
1.550
-75
150.0
1,800
20
.67
150.0
1,800
.80
175.0
2,100
24
.76
204.2
2,450
89
233.3
2,800
30
.88
291.7
3.500
1.03
333.3
4,000
36
■99
391-7
4.700
I -15
454.2
5.450
42
1. 10
512.5
6,150
1.28
591 7
7,100
48
1.26
666.7
8,000
1.42
750.0
9,000
54
1 . 35
800.0
9,600
1. 55
933.3
11,200
60
1-39
916.7
11,000
1.67
1,104.2
13.250
Class C
Class D
Nominal
inside
300 ft. head. 130 lbs
pressure
400 ft. he
ad. 173 lbs. pressure
diameter,
inches
Thickness,
inches
Weig
it per
Thickness,
inches
Weight per
Foot
Length
Foot
Length
4
.48
23.3
280
.52
25. 0
300
6
51
35.8
430
.55
38.3
460
8
56
52.1
625
.60
55.8
670
10
62
70.8
850
.68
76.7
920
12
68
91-7
1,100
.75
100.0
1,200
14
74
116.7
1,400
.82
129.2
I.5SO
16
80
143.8
1.72s
.89
158.3
1,900
18
87
175.0
2,100
.96
191 -7
2,300
20
92
20S.3
2,500
1.03
229.2
2.7SO
24
04
279.2
3„3So
1. 16
306.7
3.680
30
20
400.0
4,800
1.37
4SO.O
5.400
36
36
545.8
6,550
1. 58
625.0
7.S0O
42
54
716.7
8,600
1.78
825.0
9.9CO
48
71
908 3
10,900
1.96
1050.0
12,600
54
90
1,141.7
13.700
2.23
1341.7
16,100
60
2
00
1.341-7
16,100
2.38
1583.3
19,000
The above weights are for 12-feet laying lengths and standard sockets; propor-
tionate allowance to be made for any variation therefrom.
360 Stundurd Specificutions for Cast Iron I'ipc
Marking
Evcrj' pipe and special casting shall have distinctly cast upon it the
initials of the maker's name. When cast especially to order, each pipe
and special casting larger than 4-inch may als<j have cast U|X)n it figures
showing the year in which it was cast and a numljcr signifying the order
in point of time in which it was cast, the figures denoting the year being
above and the number below, thus:
1901 1901 1901
I 2 3
etc., also any initials, not exceeding four, which may be required by the
purchaser. The letters and figures shall be cast on the outside and shall
be not less than 2 inches in length and J6 of an inch in relief for pipes
8 inches in diameter and larger. For smaller sizes of pipes the letters
may be i inch in length. The weight and the class letter shall be con-
spicuously painted in white on the inside of each pipe and special casting
after the coating has become hard.
Allowable Percentage of Variation in Weight
No pipe shall be accepted the weight of which shall be less than the
standard weight by more than 5 per cent for pipes 16 inches or less in
diameter, and 4 per cent for pipes more than 16 inches in diameter, and
no excess above the standard weight of more than the given percentages
for the several sizes shall be paid for. The total weight to be paid for
shall not exceed, for each size and class of pipe received, the sum of the
standard weights of the same number of pieces of the given size and class
by more than 2 per cent.
No special casting shall be accepted the weight of which shall be less
than the standard weight by more than 10 per cent for pipes 12 inches
or less in diameter, and 8 per cent for larger sizes, except that curves,
Y pieces and breeches pipe may be 12 per cent below the standard weight,
and no excess above the standard weight of more than the above per-
centages for the several sizes will be paid for. These variations apply
only to castings made from the standard patterns.
Quality of Iron
All pipes and special castings shall be made of cast iron of good quality
and of such character as shall make the metal of the castings strong,
tough and of even grain, and soft enough to satisfactorily admit of
drilling and cutting. The metal shall be made without any admixture
of cinder iron or other inferior metal, and shall be remelted in a cupola
or air furnace.
Coating 361
Tests of Material
Specimen bars of the metal used, each being 26 inches long by 2 inches
wide and i inch tliick, shall be made without charge as often as the
engineer may direct, and, in default of definite instructions, the con-
tractor shall make and test at least one bar from each heat or run of
metal. The bars, when placed flatwise upon supports 24 inches apart
and loaded in the center, shall for pipes 12 inches or less in diameter
support a load of 1900 pounds and show a deflection of not less than 0.30
of an inch before breaking, and for pipes of sizes larger than 12 inches
shall support a load of 2000 pounds and show a deflection of not less than
0.32 of an inch. The contractor shall have the right to make and break
three bars from each heat or run of metal, and the test shall be based upon
the average results of the three bars. Should the dimensions of the bars
differ from those above given, a proper allowance therefor shall be made
in the results of the tests.
Casting of Pipes
The straight pipes shall be cast in dry sand moulds in a vertical position.
Pipes 16 inches or less in diameter shall be cast with the hub end up or
down, as specified in the proposal. Pipes 18 inches or more in diameter
shall be cast with the hub end down.
The pipes shall not be stripped or taken from the pit while showing
color of heat, but shall be left in the flasks for a sufliicient length of time
to prevent unequal contraction by subsequent exposure.
Quality of Castings
The pipes and special castings shall be smooth, free from scales, lumps,
blisters, sand holes and defects of every nature which unfit them for the
use for which they are intended. No plugging or fiUing will be allowed.
Cleaning and Inspection
All pipes and special castings shall be thoroughly cleaned and sub-
jected to a careful hammer inspection. No casting shall be coated unless
entirely clean and free from rust, and approved in these respects by the
engineer immediately before being dipped.
Coating
Every pipe and special casting shall be coated inside and out with coal-
tar pitch varnish. The varnish shall be made from coal tar. To this
material sufficient oil may be added to make a smooth coating, tough and
tenacious when cold, and not brittle nor with any tendency to scale off.
Each casting shall be heated to a temperature of 300° F., immediately
before it is dipped, and shall possess not less than this temperature at the
362
Slamlard SiKcilications for C'a.st Iron I'ijx:
lime it is put in the vat. The ovens in which the pipes arc heated shall
lie so arranged tliat ail portions of the pipe shall be heated to an even
temperature. Kacli casting shall remain in the bath at least five minutes.
The varni.sh shall be heated to a temperature of 300° I*, (or less if the
engineer shall so order), and shall be maintained at this temperature
during the time the casting is immersed.
Fresh pitch and oil shall be added when necessary to keep the mixture
at the proper consistency, and the vat shall be emptied of its contents
and refilled with fresh pitch when deemed necessarj- by the engineer.
After being coated the pipes shall be carefully drained of the surplus
varnish. Any pipe or special casting that is to be recoated shall first be
thoroughly scraped and cleaned.
Hydrostatic Test
WTien Ihe coating has become hard, the straight pipes shall be sub-
jected to a proof by hydrostatic pressure, and, if required by the engineer,
they shall also be subjected to a hammer test under this pressure.
The pressures to which the different sizes and classes of pipes shall be
subjected are as follows:
Classes
Class A pipe.
Class B pipe.
Class C pipe.
Class D pipe
20-inch diam-
eter and larger,
pounds per
square inch
150
200
250
300
Less than
20-inch diam-
eter, pounds
per square inch
300
300
300
•WO
Weighing
The pipes and special castings shall be weighed for payment under the
supervision of the engineer after the application of the coal-tar pitch
varnish. If desired by the engineer, the pipes and special castings shall
be w^eighed after their deliver)' and the weights so ascertained shall be
used in the final settlement, provided such weighing is done by a legalized
weighmaster. Bids shall be submitted and a final settlement made upon
the basis of a ton of 2000 pounds.
Contractor to Furnish Men and Materials
The contractor shall provide all tools, testing machines, materials and
men necessary for the required testing, inspection and weighing at the
foundry, of the pipes and special castings; and, should the purchaser have
Engineer or Inspector 363
no inspector at the works, the contractor shall, if required by the engineer,
furnish a sworn statement that all of the tests have been made as specified,
this statement to contain the results of the tests upon the test bars.
Power of Engineer to Inspect
The engineer shall be at hberty at all times to inspect the material at
the foimdry, and the moulding, casting and coating of the pipes and special
castings. The forms, sizes, uniformity and conditions of all pipes and
other castings herein referred to shall be subject to his inspection and
approval, and he may reject, without proving, any pipes or other casting
which is not in conformity with the specifications or drawings.
Inspector to Report
The inspector at the foimdry shall report daily to the foimdry office all
pipes and special castings rejected, with the causes for rejection.
Castings to be Delivered Sound and Perfect
All the pipes and other castings must be delivered in all respects sound
and conformable to these specifications. The inspection shall not relieve
the contractor of any of his obligations in this respect, and any defective
pipe or other castings which may have passed the engineer at the works
or elsewhere shall be at all times liable to rejection when discovered until
the final completion and adjustment of the contract, provided, however,
that the contractor shall not be held liable for pipes or special castings
found to be cracked after they have been accepted at the agreed point of
deUvery. Care shall be taken in handling the pipes not to injure the
coating, and no pipes or other material of any kind shall be placed in the
pipes during transportation or at any time after they receive the coating.
Definition of the Word "Engineer"
Wherever the word "engineer" is used herein it shall be understood
to refer to the engineer or inspector acting for the purchaser and to his
properly authorized agents, limited by the particular duties intrusted
to them.
.^64 Suinuard S|>ccificalions /or Cast Iron I'i|>c
Volume and Wiiioux ok Piled, Bell and Simcot Cast Iron Pipe
Size of
pipe,
inches
Head
in
feet
Thiclc-
ness of
metal,
inches
Weight
of one
pipe in
pounds
No. of
pipes in
one ton
of 2240
pounds
Cubic
feet in
one ton
of 2240
pounds
pipes in
40 cubic
feet
o( pipe
in 40
cubic feci
. ublc
feet In
one
pipe
3
loo
.38
167
1341
21.414
; 104. 121
1.604
3
200
.42
I8S
12. II
19 79<i
-. ■,■ ,
4J23.3»
I 63s
3
300
45
200
11.20
18.961
23.626
4724.224
I 693
3
400
• 45
200
11.20
18.961
23.626
4724.224
I 693
4
100
.40
230
9 74
23.646
16.479
3787.720
2.438
4
200
.42
243
9.26
22.953
16.135
3920. o.M
2.479
4
300
• 45
260
8.61
22.873
15 754
4004.480
2.539
4
400
.47
265
8.45
21.823
15.491
4104.372
2.582
S
100
.42
295
7.59
26 .537
11.433
3376.136
3. 495
5
200
.45
31S
7. II
25 356
11.222
3534. 332
3.565
5
300
• 48
338
6.63
24.13s
10.983
3712.000
3-643
S
400
• SI
355
6.31
23.503
10.738
3811.172
3 725
6
100
.43
364
6.15
28.825
8.359
3008.000
4684
6
200
• 47
393
5.70
27.285
8.356
3283.240
4 787
6
300
• SI
426
5.2s
25.764
8.177
3477.224
4.900
6
400
• 54
445
5. 03
25.114
8.017
3567.092
4 990
8
100
• 47
SI3
4.36
33.42s
S.224
2680.164
7^656
8
200
• 51
567
3.95
30.833
5118
2906.196
7804
8
300
• 56
624
359
28.666
5.009
3129.392
7985
8
400
• 61
665
3 37
27.456
4.906
3262.730
8.153
10
100
.50
68s
327
37 400
3.454
2366.256
11.579
lo
200
• S6
765
2^93
34^676
3.388
2587.484
11.826
lo
300
.62
852
2.63
31800
3.317
3826.248
12.058
lo
400
.68
920
2.43
30.266
3.216
2959-172
"•435
12
100
• S3
870
2.S7
41.230
2.497
2172.492
16.018
13
200
.60
985
2.27
37.218
2.444
2407.236
16.367
12
300
.68
11 10
2.02
33.858
2384
3646.288
16.778
12
400
• 75
1210
1.98
34 839
2.159
2612.892
17 549
14
100
• S6
1074
2.08
44.310
1.882
2021.388
31.252
14
200
• 65
1229
1.82
39 798
1.831
2250.592
21.843
14
300
• 73
1399
1.60
35.699
1794
2509.568
33.398
14
400
• 82
IS40
145
33.242
1757
2969.184
22.847
i6
100
.60
1293
1.73
47.32s
1.464
1893.864
27.308
i6
200
.69
1496
I 50
41.829
1.434
2145 788
27.886
i6
300
•79
1723
1.30
37.095
1. 401
241s . 256
28.535
I6
400
.89
1900
1.18
36.020
1.316
2490.308
30.578
I8
100
.63
i.';32
1.46
48.274
1. 211
1855 876
33019
I8
200
74
17»8
1.28
44 456
1.157
2068.864
34 569
I8
300
.85
206s
l.o8
38.572
1.124
2321 . 284
35 S83
i8
400
• 96
2300
.974
35441
1. 100
2532.076
36.338
Volume and Weight of Piled, Bell and Spigot Cast Iron Pipe 365
Volume and Weight of Piled, Bell and Spigot Cast
Iron Pipe {Continued)
Size of
pipe,
inches
Head
in
feet
Thick-
ness of
metal,
inches
Weight
of one
pipe in
pounds
No. of
pipes in
one ton
of 2240
pounds
Cubic
feet in
one ton
of 2240
pounds
No. of
pipes in
40 cubic
feet
Pounds
of pipe
in 40
cubic feet
Cubic
feet in
one
pipe
20
100
.66
1.788
1,28
53.874
.945
1778.040
41.893
20
200
.78
2,104
1.06
45.596
.938
1963,836
42.854
20
300
.91
2,444
.916
39900
.918
2240.272
43. 559
20
400
.03
2,740
.814
36.508
.891
2443 188
44.850
24
100
.75
2,407
.931
55.122
.679
1626.132
59-207
24
200
.87
2,803
.799
49 463
.646
1811.112
61.906
24
300
1.02
3,299
.679
43.122
.630
2080.876
63-415
24
400
1. 16
3,680
.600
38.783
.619
■2277.256
64.639
30
100
.87
3.482
.649
59-733
.434
IS13.268
92.039
30
200
1. 01
4,027
.556
52.760
.421
1697.492
94.892
30
300
1. 19
4.783
.468
45.550
.411
1965.660
97.337
30
400
1.37
5.420
.413
41.047
.402
2181.364
99 387
36
100
.98
4,699
.476
63.567
.299
1407.388
133-544
36
200
1. 14
5,460
.410
55.586
.295
1610.884
135.577
36
300
1.36
6.543
.342
47.019
.291
1903.636
137.484
36
400
1.58
7.490
.300
42.566
.282
2111.516
141.888
40
100
1.09
5.807
.386
63.591
.242
1409.936
164.74s
40
200
1-23
6.52s
.343
56.997
.240
1570.636
166.174
40
300
1.48
7.858
.285
48.909
.233
1831.588
171. 610
40
400
1.72
9.050
.247
43.413
.227
2059.372
175.763
42
100
1. 10
6.147
.364
66.117
.225
1353.628
181.640
42
200
1.28
7.100
.315
58.179
.216
1537.664
184.69s
42
300
1-54
8,563
.258
48.802
.211
1810.768
189.157
42
400
1.79
9.890
.248
48.002
.206
2043.812
193.559
48
100
1 .25
7,982
.281
65.246
.171
1370.164
233.023
48
200
1. 41
8,946
.250
59.800
.167
1496.000
239.200
48
300
1. 71
10,857
.206
50.862
.166
1758.940
246.903
48
400
1.99
12,550
.179
44.767
.163
2007 . 856
250.097
60
100
1.40
II,OCO
.203
74.817
.108
1193.836
368.559
60
200
1.68
13.260
.169
63.188
.107
1418.568
373-897
60
300
2.0s
16,040
•139
52.903
.105
1685.760
380.599
60
400
2.41
18,970
.118
46.253
.102
1938.820
391.978
Fig. 103. — Pile of 100 Pipe.
360
SuiuJard S|K-ciliculions for Casl In in i'i|K'
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Pattern Size and Weight of Cast Iron Pipe
367
to
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368
SUindard Specifications for Cubl Iron I'ijx;
%%
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Pattern Size and Weight of Cast Iron Pipe
369
Pattern Size and Weight of Cast Iron Pipe, % to ii?^2
Inches Thick
40-inch
Pipe
42-inch
Pipe
48-inch
Pipe
60-inch
Pipe
Thickness, inches
Pattern
Weight,
Pattern
Weight,
Pattern
Weight,
Pattern
Weight,
size, inches.
pounds
size, inches.
pounds
size, inches.
pounds
size, inches,
pounds
42
3910
25^3
42M6
4075
4240
44!-i
4440
2^62
42^6
4405
44? 16
4615
42>4
4737
44H
4790
2?i2
42M6
4903
44^6
496s
i^ie
A2%
4903
44?8
SI40
5969
40-inch
Pipe
42-inch
Pipe
48-inch
Pipe
60-inch
Pipe
Thickness, inches
Pattern
Weight,
Pattern
Weight,
Pattern
Weight,
Pattern
Weight,
size, inches.
pounds
size, inches.
pounds
size, inches.
pounds
size, inches,
pounds
31.^2
42^6
S070
44i^1 6
5316
501/2
6068
42^2
5237
44H
5492
So9i6
6267
1 1/62
42?^6
S404
44?i6
5668
So'Js
6467
5572
445&
5844
6667
62j;8
8282
l9^2
42' Hf
5740
44' '/'h
6021
50%
6867
621^1 e
8532
ij-i
42^4
5908
44^4
6198
5o'?i6
7067
63
I?^2
42i?'i6
6077
44' ^i 6
6375
5o?i
7268
63H6
9032
40-inch
Pipe
42-inch
Pipe
48-inch
Pipe
60-inch
Pipe
Thickness, inches
Pattern size, inches
Weight, pounds
Pattern size, inches
Weight, pounds
Pattern size, inches
Weight, pounds
Pattern size, inches
Weight, pounds
I?i6
I?^2
tH
I%2
1^6
ll!-^2
A2%
42lfi6
43
43M6
43'/^
43?'! 6
6246
6415
6585
6755
692s
7096
^A'A
44*^6
45
45 He
45^6
4S?i6
6552
6730
6908
7086
7264
7443
50' fie
51
51 Vis
SiH
5I?'18
5lH
7469
7670
7871
8073
8275
8477
63'/6
63^16
63I/4
63M6
63?S
63^6
9282
9S32
9782
10,032
10,283
10,534
m
43M
7267
45 H
762
SiMe
8679
63;-^
10,785
40-inch
Pipe
42-Lnch
Pipe
48-inch
Pipe
60-inch
Pipe
Thickness, inches
Pattern size, inches .
Weight, pounds
Pattern size, inches.
Weight, pounds
Pattern size, inches.
Weight, pounds
Pattern size, inches.
Weight, pounds
I>?^2
43?i6
7438
45916
7801
^1%
8882
63?i6
11,086
43?i
7610
45?^
7980
51M6
9083
639i
11.337
ll^fc
43^6
7782
45^/16
8160
9288
63IH6
I I, 588
ii/i
43}^
7954
45 K2
8340
Si^ie
9491
63?i
n.839
1^2
439'i6
8127
45?-! 6
8520
51?^
969s
63'?'! 6
12,091
iyi%
8300
45?€
8700
511 He
9899
633;^
12,343
i^%2
43IH6
8473
451 He
8881
5i?4
10,103
6315,^6
12,545
370
SUndard SiMJcilicalions for Cast Iron ri|)C
Pattern" Size and Weight of Cast Iron Pipe, ih tj 2Wi
Inches Thick
40-inch
Pipe
4J-inch
Pipe
48-inch
Pipe
60-inch
Pipe
Thickness, inches
Pattern size, inches i.vli
Weight, pounds I 8647
Pattern size, inches. .
Weight, pounds
Pattern size, inches..
Weight, pounds
Pattern size, inches. .
Weight, pounds
1 iH
inia
I'M.
AM
43' 5i.
iJ4
l.vli
43'?. 0
44
8647
8831
899s
9170
934S
4S>i
4S'?i»
4SJi
4S'^i«
46
9062
9243
9424
9606
9788
Si'^io
Si^i
Si'Mo
52
S2H0
10.307
IO,SI2
10,717
10,922
II. 127
64
64M6
64^6
64? i 8
64M
12,847
13.099
I3JS7
13.603
13.856
i*»4j
44H*
9S»
46H«
9970
52W
"033
64Ma
40-inch
Pipe
42-inch
Pipe
48-inch
Pipe
60-inch
Pipe
Thickness, inches
Pattern
Weight,
Pattern
Weight,
Pattern
Weight,
Pattern
Weight,
size, inches.
pounds
size, inches. .
pounds
size, inches..
pounds
size, inches.,
pounds
I'^-iu
i2;62
44H
i»%t
i«M«
44 '/6
44'?io
9688
9862
10,048
46!-6
46?! 6
46M
46518
46H
10,152
10,335
10,518
10,700
10.885
S2?i6
52! 4
525iB
52H
S2'/(»
1 1. 539
11,745
I I. 951
12,158
12.365
6498
64^16
64 Mo
64? i 8
64''8
14.362
14.615
14.868
15.121
15.374
I»^J
52^
12.573
64' H«
15.638
40-inch
Pipe
42-inch
Pipe
48-inch
Pipe
60-inch
Pipe
Thickness, inches
Pattern size, inches.
Weight, pounds
Pattern size, inches.
Weight, pounds
Pattern size, inches.
Weight, pounds
Pattern size, inches.
Weight, pounds
5291 8
12,779
64?4
15.882
52H
12.987
64'?<6
16.136
2M8
S3'H«
13.19s
6aH
16,390
2942
5294
13443
641518
16.644
2H
52' 91 8
13.611
65
16.898
40-inch
Pipe
42-inch
Pipe
,»o<-inch
Pipe
60-inch
Pipe
Thickness, inches
Pattern
Weight,
Pattern
Weight,
Pattern
Weight,
Pattern
Weight,
size, inches.
pounds
size, inches.
pounds
size, inches.
pounds
size, inches,
pounds
29^2
65H8
17.152
29^8
65Vi
17.407
6s9i«
17.662
2M
6sM
17.917
39^2
659I8
18.172
CHAPTER XV
MECHANICAL ANALYSIS
While chemical analysis is absolutely necessary for the determination
of the constituents of iron and the fuels, and is of greatest importance to
the foundryman as a guide in their purchase, chemists cannot, however,
as yet predict with certainty the physical properties which will result
from the mixture of irons possessing identical composition.
Test bars have shown, that of two irons, precisely the same in their
chemical constituents, one may exceed the other in tensile strength by
as much as 50 per cent. No satisfactory explanation of the discrepancy
has been made. Various suggestions, attributing the cause to the ores,
changes of temperatvure in the furnace, to difference in cooling, etc., are
offered, but the problem is still unsolved.
Whatever may be the cause of these differences, the foundryman needs
some means of quickly detecting and correcting them. He should
have prompt information as to shrinkage, softness and strength of his
castings.
During 1885, Mr. Keep made the important discovery that the shrink-
age of test bars varied inversely as the silicon content, and that by
measurement of shrinkage the silicon is practically determined.
His investigations resulted in pointing out the intimate relations which
exist between shrinkage and the other properties of cast iron, both
chemical and physical. Mr. Keep's conclusions as to the importance of
mechanical analysis are summarized as follows:
The physical properties of the casting are not wholly dependent upon
its chemical composition.
Mechanical analysis measures the physical properties of the iron,
which are, shrinkage, strength, deflection, set and depth of chill. The
measure of these properties shows the combined influen^ce of each element
in the chemical composition, and in addition thereto, it shows the in-
fluence of fuel and every varying condition attending melting.
These influences, particularly that of sulphur, are counteracted by the
use of silicon.
The measurement of shrinkage tells whether more or less silicon is
needed to bring the quality of the casting to an accepted standard of
excellence.
371
372 Mechanical Analysis
Instead of calculating the chemical c<)mpf>silion and predictinR the
pliysi(al properties, mechanical analysis ascertains the physical jiropcr-
ties first, and determines from the shrinkage whether more or less silicon
is reciuired to protluce castings of a given standard. Measurement of
shrinkage is made quickly at a nominal cost and alone gives all necessary
information.
It tells the founder exactly what physical properties his castings have
and exactly what to do to bring each of those properties to standard.
By this method a founder can determine whether a low-priced iron is
suitable for his use.
Having fixed upon a standard, he can ascertain during the heat
whether the mixture is of the desired quality, and if necessar>' can increase
or decrease the silicon, according as the shrinkage should be reduced or
increased.
Mechanical analysis answers all the requirements of the ordinary
founder. Its simplicity renders the emplojTnent of an expert unneces-
sary.
Pig iron and coke, having been purchased upon guaranteed analysis,
an occasional analysis of the castings is only required.
In a report to The American Society oi Mechanical Engineers, Mr.
Keep presents a Shrinkage Chart and Strength Table, which are given
below with his directions for using them.
Shrinkage Chart
W. J. Ki:i:i'
While the tensile tests show an increase of strength with an increase
of phosphorus, yet the transverse tests seem to show that phosphorus
reduces strength. This is also general shop experience.
Sulphur. — There is not in these tests enough uniformity between
the percentage of sulphur and the strength to show any decided influence,
but the indication is that sulphur dccrciises strength. In .some cases
sulphur might add to strength by causing the grain to be closer.
Manganese. — The percentage is too nearly the same in these series
to show any influence on strength.
By comparing strengths and chemical composition of the irons nearest
alike, with all chemical elements nearly alike, and no scrap, but with
quite different strengths, it is very evident that strength is dependent
upon something outside of the ordinary- chemical composition.
Slow cooUng decreases strength by making the grain of a casting
coarse and more open. The larger the casting the weaker it become*"
per square inch of section. The weakness is not caused by a decrease
in combined carbon because a complete analysis of each size of test bar
Shrinkage Chart
373
(Transactions, American Society of Mechanical Engineers, Vol. XVI,
p. hoc) shows the same combined carbon in all sizes of many series,
but in all cases the strength per unit of section decreased as the size
increased.
Strength of any size of test bar cannot be calculated by any mathe-
matical formula from the measured strength of another size, because the
grain changes by slow cooling.
1.00 l.'ZS 1.50 1.75 2.00 E.25 ?.50 2.75 3.00 3.25 3.50
425
400
375
350
325
300
275
250
225
200
175
5400
3200
3000
2800
2600
2400
2200
'■
^
^
%^
^
^
y
y
y
/
^
■
2'k
/"
2000
1
^i', ..
1800
- —
2
■ ■
... 2
4"
■
-^
1600
3
'~!.^___
~ '
1400
1 ^
4
r^.
Hi;^
.
[i;;;;^
:^
— ■
IX
0 I.?
5 I.E
0 1.7
5 2
00 2.'
5 Ih
0 2.-
5 3.
DO 3.
E5 3.5
Percent Silicon.
Fig. 104.
Tensile Strength Chart. — Fig. 105 shows this chart. The dotted line
estimated.
"Table for Obtaining the Strength of any Size of Test Bar from the
Measured Strength of the Standard Test Bar. — Table on p. 375 is cal-
culated for a standard i-inch square test bar. Measure the shrinkage
per foot of the standard test bar, then on the shrinkage chart, Fig. 105,
find this shrinkage on the left-hand margin and follow horizontally
imtil you intersect the line of the measured test bar. Follow the
vertical line at the intersection to the top of the chart, and you find
the percentage of silicon that is expected to produce the shrinkage.
Find this same percentage at the top of Table i , and follow down to the
size of test bar that you wish the strengths of. If you wish the actual
374
Mechanical Analysis
strength use the lower figures as mullij)lier of the measured strength of
the standard i-inch bar. If you wish the strength of a section i inch
square by 12 inches long of the rc<juire<l test bar use the upper number
to multiply by."
"If you have the strength of any size of test bar other than a i-inch
bar and know the silicon percentage, divide such strength by the lower
.190
.180
.170
.160
.150
.140
.130
.120
.110
.100
.090
.080
.070
.060
.050
.040
..030
N
\
V
\
\
X
i.
>-
X
N
V
\
s
^
N,
N,
'x
X
-^
5
^ 1
'n
^
"N
K
— -
^
\
s
X
s
^
%
X
N,
s
\
\
N,
"*\
h
s.
X
•v
\
N
X
<
^
N,
<.
-<5
^s
X
\
[^
k^
N
<
\
N,
s
^
S
sl
\
N,
N
X
<:
N,
\
X
\:
\
\
X
X
^
I. m 1.50 t75 2.00 Z.ZS ?.50 a75 3100 5.25 350
Percent.
Fig. 105.
number for the bar, or if you have the strength of a section of the re-
quired test bar i inch square by 12 inches long, divide by the upper
number, and the result in either case is the strength of the standard
I-inch bar."
" To find the Strength of any Casting. — Divide the cubic contents of
the casting by the square inches of cooling surface, and the quotient is
the cooling ratio. If the casting has a large flat surface the edges may
be neglected; for example, a casting i inch thick and 24 inches square.
Keep's Strength Table
375
O O
in o
00 o>
Tj- 00
lo o
00 00
t- O
Si N
.S. S~^ J:8 ?38
■=* ■^ M 00
;s
376
Mechanical Analysis
A strip one inch wide and 24 inches lonj; would have 24 cubic inches
contents and 48 sfjuarc inches of cooling surface. 24 -^ 48 = 0.5 ratio.
Find this ratio at the top of the chart, Fig. 105, and follow down to the
•*!''
Iron fol low-board with yokes and brass
pastums for test bars ^i in. square X
12 in. long.
Fig. 106.
Iron Flask.
Taper steel scale which measures
shrinkage.
Fig. 107.
diagonal and we find that a 2-inch square test bar represents the strength
of the casting."
"With the shrinkage of a standard i-inch test bar, cast at the same
time as the casting, find on the shrinkage chart the percentage of silicon
in the casting. Then in the Table
find the upper multipUer for a 2-inch
test bar. This multiplied by the
measured strength of the standard
test bar gives the strength of a sec-
tion of the casting i inch square
and 12 inches long."
Mechanical analysis covers tests
for shrinkage, strength and hard-
ness.
Figs. 1 06 and 107 show a de\nce
designed by Mr. Keep for determin-
ing shrinkage.
Determinations for strength are
generally made by taking the trans-
verse strength and deflection.
The Riehle Machine as shown in
Fig. 108 is in common use for this
purpose.
This illustration represents faith-
fully the general appearance of this
machine. The specimen is shown in position. The weighing-beams
and levers are all carefully sealed to the standard of the United States,
Government, and guaranteed to be accurate and reliable.
Fig. 108.
Constituents of Cast Iron 377
Operation
The weighing-beam must be balanced before the specimen is arranged
for testing. The wheel shown must be moved from left to right, and,
as the beam rises, the poise must be moved out to restore the equipoise.
If more strain is required to break the specimen than can be weighed by
the poise, move the poise back to zero and place the loose weight on the
weight dish shown at the extreme left (small end) of weighing-beam, and
move the poise out as before, until the test is completed. The calcula-
tions are made so that the beam registers the center load.
Dimensions
Extreme length 3 ft. 2 in.
Extreme height 3 ft. i in.
Extreme width i ft. 4 in.
Weight 200 lbs.
Shipping weight 230 lbs.
Adaptation
Transverse specimens 1 2 in. long
Hardness
This property may be measured by embedding steel balls in the casting
to be tested, by Turner's Scleroscope (see cut, page 114, Turner's Lec-
tures on " Founding "); or by Keep's Machine (see cut, page 187, " Cast
Iron "). The latter method is the more simple and gives accurate results.
A small high speed drill may be used for this purpose, but it must be so
arranged that the load on the spindle will be constant.
Standard Methods for Determining the Constituents
of Cast Iron
As reported by the Committee of the American Foundrymen's Association, Phila-
delphia Convention, May 21-24, ^907.
Determination of Silicon
Weigh one gram of sample, add 30 c.c. nitric acid (1.13 sp. gr.);
then 5 c.c. sulphuric acid (cone). Evaporate on hot plate xintil all
fumes are driven off. Take up in water and boil until all ferrous sul-
phate is dissolved. Filter on an ashless filter, with or without suction
pump, using a cone. Wash once with hot water, once with hydrochloric
acid, and three or four times with hot water. Ignite, weigh and evapo-
378 Chemical Analysis
rale with a few drops of sulphuric acid and 4 or s c.c. of hydrofluoric acid.
Ignite slowly and weigh. Mullii)ly the difference in weight by 0.4702,
which equals the per cent of silicon.
Determination of Sulphur
Dissolve slowly a three-gram sample of drillings in concentrated nitric
acid in a platinum dish covered with an inverted watch glass. After
the iron is completely dissolved, add two grams of potassium nitrate,
evapx)rate to dryness and ignite over an alcohol lamp at red heat. Add
50 c.c. of a one per cent solution of sodium carbonate, boil for a few
minutes, filter, using a little paper pulp in the filter if desired, and wash
with a hot one per cent sodium carbonate solution. Acidify the filtrate
with hydrochloric acid, evaporate to drj-ness, take up with 50 c.c. of
water and 2 c.c. of concentrated hydrochloric acid, filter, wash and after
diluting the filtrate to about 100 c.c. cool and precipitate with barium
chloride. Filter, wash well with hot water, ignite and weigh as barium
sulphate, which contains 13.733 per cent of sulphur.
Determination of Pliosplioriis
Dissolve 2 grams sample in 50 c.c. nitric acid (sp. gr., 1.13), add 10 c.c.
hydrochloric acid and evaporate to dryness. In case the sample contains
a fairly high percentage of phosphorus it is better to use half the above
quantities. Bake until free from acid, redissolving in 25 to 30 c.c. of
concentrated hydrochloric acid; dilute to about 60 c.c, filter and wash.
Evaporate to about 25 c.c, add 20 c.c. concentrated nitric acid, evapo-
rate until a film begins to form, add 30 c.c. of nitric acid (sp. gr., 1.20)
and again evaporate until a film begins to form. Dilute to about 150 c.c.
with hot water and allow it to cool. WTien the solution is between 70
degrees and 80 degrees C. add 50 c.c. of molybdate solution, .\gitate
the solution a few minutes, then filter on a tarred Gooch crucible having
a paper disc at the bottom. Wash three times with a 3 per cent nitric
acid solution and twice with alcohol. Dr>' at 100 degrees to 105 degrees
C. to constant weight. The weight multiplied b}- 0.0163 equals thef>er
cent of phosphorus in a i-gram sample.
To make the molj'bdate solution add loo grams molybdic acid to
250 c.c. water, and to this add 150 c.c. ammonia, then stir until all is
dissolved and add 65 c.c. nitric acid (1.42 sp. gr.). Make another solu-
tion by adding 400 c.c. concentrated nitric acid to 1100 c.c. water, and
when the solutions are cool, pour the first slowly into the second
wnth constant stirring and add a couple of drops of ammonium
phosphate.
Determination of Total Carbon 379
Determination of Manganese
Dissolve one and one- tenth grams of drillings in 25 c.c. nitric acid
(1.13 sp. gr.), filter into an Erlenmeyer flask and wash with 30 c.c. of the
same acid. Then cool and add about one-half gram of bismuthate until
a permanent pink color forms. Heat until the color has disappeared,
with or without the precipitation of manganese dioxide, and then add
either sulphtu-ous acid or a solution of ferrous sulphate until the solution
is clear. Heat until all nitrous oxide fumes have been driven off, cool
to about fifteen degrees C; add an excess of sodium bismuthate — about
one gram — and agitate for two or three minutes. Add 50 c.c. water
containing 30 c.c. nitric acid to the Htre, filter on an asbestos filter into
an Erlenmeyer flask, and wash with fifty to one hundred c.c. of the nitric
acid solution. Run in an excess of ferrous sulphate and titrate back with
potassium permanganate solution of equal strength. Each c.c. of N-io
ferrous sulphate used is equal to o.io per cent of manganese.
Determination of Total Carbon
This determination requires considerable apparatus; so in view of
putting as many obstacles out of the way of its general adoption in cases
of dispute, your committee has left optional several points which were
felt to bring no chance of error into the method.
The train shall consist of a pre-heating furnace, containing copper
oxide (Option No. i) followed by caustic potash (1.20 sp. gr.), then
calcium chloride, following which shall be the combustion furnace in
which either a porcelain or platinum tube may be used (Option No. 2).
The tube shall contain four or five inches of copper oxide between plugs
of platinum gauze, the plug to the rear of the tube to be at about the
point where the tube extends from the furnace. A roll of silver foil about
two inches long shall be placed in the tube after the last plug of platinum
gauze. The train after the combustion tube shall be anhydrous cupric
sulphate, anhydrous cuprous chloride, calcium chloride, and the absorp-
tion bulb of potassium hydrate (sp. gr., 1.27) with prolong filled with
calcium chloride. A calcium chloride tube attached to the aspirator
bottle shall be connected to the prolong.
In this method a single potash bulb shall be used. A second bulb is
sometimes used for a counterpoise being more liable to introduce error
than correct error in weight of the bulb in use, due to change of tempera-
ture or moisture in the atmosphere.
The operation shall be as follows: To i gram of well-mixed drillings
add 100 c.c. of potassium copper chloride solution and 7.5 c.c. of hydro-
chloric acid (cone). As soon as dissolved, as shown by the disappearance
3So Chemical Analysis
of all copper, filter on previously washefl and ignited asbestos. Wash
thorouglily the beaker in which the solution was made with 20 c.c. of
dilute hydrochloric acid [i to 1 ], [xjur this on the filter and wash the carbon
out of the beaker by means of a wash bottle containinjj dilute hydro-
chloric acid [i to i] and then wash with warm water out of the
filter. Dry the carbon at a temperature between 95 and 100 de-
grees C.
Before using the apparatus a blank shall be run and if the bulb does
not gain in weight more than 0.5 milligram, put the drictl filter into the
ignition tube and heat the pre-heating furnace and the part of the com-
bustion furnace containing the copper oxide, .\fter this is heated start
the aspiration of oxygen or air at the rate of three bubbles per second, to
show in the potash bulb. Continue slowly heating the combustion tube
by turning on two burners at a time, and continue the combustion for
30 minutes if air is used; 20 minutes if oxygen is used. (The Shimer
crucible is to be heated with a blast lamp for the same length of
time.)
When the ignition is finished turn off the gas supply gradually so as
to allow the combustion tube to cool off slowly and then shut off the
oxygen supply and aspirate with air for 10 minutes. Detach the potash
bulb and prolong, close the ends with rubber caps and allow it to stand
for 5 minutes, then weigh. The increase in weight multiplied by 0.27273
equals the percentage of carbon.
The potassium copper chloride shall be made by dissolving one pound
of the salt in one litre of water and filtering through an asbestos
filter.
Option No. I. — \Miile a pre-heater is greatly to be desired, as only
a small percentage of laboratories at present use them, it was decided
not to make the use of one essential to this method; subtraction of the
weight of the blank to a great extent eliminating any error which might
arise from not using a~ pre-heater.
Option No. 2. — The Shimer and similar crucibles are largely used as
combustion furnaces and for this reason it was decided to make optional
the use of either the tube furnace or one of the standard crucibles. In
case the crucible is used it shall be followed by a copper tube fi« inch
inside diameter and ten inches long, with its ends cooled by water jackets.
In the center of the tube shall be placed a disk of platinum gauze, and
for three or four inches in the side towards the crucible shall be silver foil
and for the same distance on the other side shall be copper oxide. The
ends shall be plugged with glass wool, and the tube heated wnth a fish
tail burner before the aspiration of the air is started.
Graphite 381
Graphite
Dissolve one-gram sample in 35 c.c. nitric acid [1.13 sp. gr.], filter on
asbestos, wash with hot water, then with potassium hydrate [i.i sp. gr.]
and finally with hot water. The graphite is then ignited as specified in
the determination of total carbon.
CIIAPTKR XVI
MALLEABLE CAST IRON
Thk process of rendering iron castings malleable was discovered by
Reaumur in 1722 and is essentially the same as that pursued at the
present day.
McWilliams and Longmuir divide malleable castings into two classes.
1. Black Heart
Black heart has a silvery outside and black inside, with a silky
lustre. This is made of a hard white iron, containing from 3 to 4 per
cent carbon, as hard carbide of iron.
By the process of annealing, to be described later, the carbide of iron
is decomposed into free carbon (annealing carbon) and iron; leaving a
soft malleable iron, which contains nearly all of the initial carbon but
in the free state finely divided and intermixed with the iron.
Black heart is mostly made in America. The process is conducted
much more rapidly than that of the ordinary (or Reaumur process), but
requires more skill and scientific information. The iron used must be
low in silicon and sulphur but need not necessarily be a while iron.
The analysis should appro.ximate to, silicon, i per cent to 0.5 per cent;
sulphur, .05 per cent as a maximum; phosphorus, .1 per cent maximum;
manganese, .5 per cent maximum and carbon 3 per cent.
The principle involved is that of taking white iron castings of suitable
composition, heating them to high temperature and converting them to
the malleable condition by precipitating the carbon in a fine state of
division, as annealing carbon. High temperature shortens the process,
i)ut it has been found more desirable to use a lower temperature and
longer anneal, as the desired change is more readily secured.
The method of molding is the same as for gray iron, with same allow-
ance for shrinkage. The amount of feeder required varies from 12.5
to 25 per cent of the weight of casting. Skill is required to make solid
castings with minimum amount of metal.
.Vfter cleaning in the usual manner the castings are packed in cast iron
boxes of varynng sizxs to suit their character, with iron scale or sand,
bone dust or fire clav; the boxes are covered with lids and luted, then
3S2
Black Heart
383
stacked in the annealing oven (to be described later). The temperature
of the oven is gradually raised to about 1 100° C, maintained at that point
for two days and then allowed to drop slowly until sufficiently cool to
permit removal of the boxes.
The composition of the castings after annealing is only altered in the
carbon, the total amount being somewhat less but practically all present
in the free state. The composition of castings made by one of the
largest English makers is as follows:
Si 0.5; S 0.04; P. 0.07; Mn 0.4; graphitic carbon 2.5; combined
carbon 0.05. A test piece u-inch square bent 180° — -cold; tensile
strength 40,000 pounds per square inch, elongation 6 per cent in 2 inches,
reduction of area 9 per cent.
Black heart is more reliable for light than for heavy work. To avoid
the introduction of sulphur, the pig iron is usually melted in an air
furnace.
Messrs. Charpy & Grenet's experiments on irons of the following
compositions are given herewith.
No.
Silicon
Sulphur
Phosphorus
Manganese
Carbon
I
.70
.01
trace
.03
3.60
2
.27
.02
.02
trace
3.40
3
.80
.02
.03
trace
3.2s
4
I. 25
.01
.01
.12
3- 20
5
2.10
.02
.01
.12
3.30
These irons were poured into cold water and contained no appreciable
amount of graphite, excepting the last which had 20 per cent. Samples
of these were subjected to various reheatings and to ascertain as nearly
as practicable the condition at any one temperature, the samples were
quenched at that temperature and then analyzed.
1. Heated at 1100° C. or any low temperature for long periods gave
no graphitic carbon; but at 1150° C. the separation.of graphitic carbon
was produced.
2. Heated for four hours each at 700°, 800°, 900° and 1000° C. showed
no free carbon; but it appeared in heating to 1100° C.
3. Showed traces at 800° C.
4. 5. Showed traces at 650° C.
In the case of No. 5, after heating at 650° C. for 6 hours, the content
of graphitic carbon had increased from o.io to 2.83 per cent.
The separation of graphite, once commenced, continues at tempera-
tures inferior to those at which the action begins.
Thus: A sample of No. i, heated at 1170° C. and quenched, contained
384
Malleable Cast Iron
only 0.50 graphitic carlKin and 2.t"> combined corlxin, while another
sample of the same cast iron, heate<l at the s^ime time to 1 1 70" C, cooled
slowly to 700° C. and then (iiicnditd contained 1.87 graphitic airl>on
and 0.43 comljincd larhoii.
Again a fragment of No. 3, heated to 1 170° C. and quenched, contained
1.42 graphitic carbon and 1.69 combined carbon, while another fragment
heated to 1170° C. cooled slowly to 700° C. and then quenched ct)nlaine<l
2.56 graphitic carbon and 0.38 combined carbon.
At a constant temperature the separation of the graphite is ctTectefl
progressively, at a rate that is the more gradual, the lower the tempera-
ture or the less the silicon content.
The authors show that these cast irons, with regard lo the critical
points, have the usual carbon change point, about 700° C, but that there
is another well-marked arrest in heating at 1140", 1165°, 1137° and
1165° C, for numbers i, 2, 3, 4 and 5, respectively; and similarly in
cooling at 1120°, 1130°, 1137° and 1145° C.
In an experiment made by W. H. Hatfield, with six bars, all containing:
Si i.o; S 0.04; P 0.04; Mn 0.22; graphitic carbon 2.83; combined
carbon 0.08, all white irons as cast; variously heat-treated so as to give
the same composition to analysis, but to have the free carbon in all
states of division from fine in No. i to coarse in No. 6.
Bars I inch square by 18 inches long were tested transversely on knife
edges 12 inches apart and gave
No.
Inches
deflection
Xo.
Inches
deflection
2^
4
5
6
before fracture; the gradually decreasing deflections given being due
entirely to the increasing coarseness of the free carbon.
Another set of four test bars, containing 0.45, 0.90, 1.10-1.8S per cent
silicon but otherwise similar in composition to the above; heat-treated
so that all should have the same type of free or annealing carlx)n, gave
95°i 98°, 94° and 89°, respectively, when subjected to the ordinary
bending test.
The microstructurc of these bars consisted of ferrite or silicon ferrite
speckled with annealing carbon, which if kept of suitable structure affects
the malleability Uttle more than does the slag in the case of wrought
iron.
Ordinary or Reaumur Malleable Cast Iron
38s
Pearlite, when present, after heat-treating white irons, greatly in-
creases the tenacity, one sample having a tenacity of 32.6 tons per square
inch, with an elongation of 6 per cent on 2 inches, and a bending angle
of 90°, when treated so as to leave 0.35 per cent of carbon in the com-
bined form and present as pearlite in the structure.
Another sample of the same general composition, but treated to leave
only 0.06 per cent as combined carbon had a tenacity of 21.2 tons per
square inch, elongation 11 per cent on two inches and a bending angle
of 180° unbroken.
2. Ordinary or Reaumur Malleable Cast Iron
In this class of castings the carbon is completely eliminated, leaving
a soft material similar in analysis to wrought iron.
It is stated that irons containing as much as 0.5 sulphur may be used
in this class of castings. The irons employed are mottled or white,
analyzing as follows: Si 0.5 to 0.9; S 0.25 to 0.35; P 0.05 to 0.08; Mn
0.1 to 0.2, total carbon ^li per cent
It may be melted in the crucible, in the cupola, or in the air fiumace.
The cupola is more in general use in England than the air fiirnace.
The table below shows approximately the influence of remelting by
the several processes.
Original pig
iron
Crucible
Cupola
Reverb.
Siemens
c 3.5
Si 8s
S 25
Mn 20
P OS
3.4
.82
.30
.10
OS
3.4
■ 75
.31
.10
.054
3.2
.65
.27
.10
.052
3.2
.70
,26
.10
OS
Whichever furnace is used it is necessary to have the metal fluid
enough to fill the most intricate parts of the molds to be poured in any
one batch. Molding operations are the same as for green sand, except
that provision must be made for the narrow range of fluidity and the
high contraction of wliite iron.
Allowance for shrinkage is H inch to the foot. The castings after
proper cleaning are packed in cast-iron boxes of suitable sizes, with red
hematite ore broken up finely. New ore is not used alone but one
part new is mixed thoroughly \vith four parts that have been used
before; the castings are carefully packed in this mixture so that no
two are in contact.
The oxygen from the ore oxidizes the carbon in the castings, gradually
386
MallcaMe (':lsI Iron
cliiniiuling it. Tlie ore, [)rc\ious tx) use. is red oxide of iron (FcjOi),
bill after the annealing process is found to be black oxide corresponding
to the formula FesOi.
After stacking the boxes in the annealing oven, the temperature is
gradually raised during 48 to 72 hours; maintained at the annealing
temperature from 12 to 24 hours, then allowed from 48 to 72 hours to
cool.
The length of time during which the high temperature is maintained
varies with the thickness of the castings. For thick work the high
temperature may have to be continued for a period increasing with the
thickness of the castings up to 96 hours.
Typical Teuper.\ture Curve for .Vnneallng Oven
lOOOr
Some makers anneal at as low a temperature as 850° C. (see P. Long,
" Metallurgy', Iron and Steel," page 130). Within reasonable limits,
chemical composition of the castings in this process has little bearing
on the result provided they are white iron as cast.
The sihcon may run from 0.3 to 0.9; sulphur 0.05 to 0.5; phosphorus
should be under o.i; manganese causes trouble if over 0.5.
Castings made by this process give a tensile strength of 18 to 22 tons;
an elongation of 2 '2 to 6 per cent on 2 fnches and a reduction of area of
5 to 8 per cent, with a cold bend on ' j-inch square, of 45° to 90°.
Mr. P. Longmuir obtained the following results from a commercial
casting: Tensile strength, 27 tons; elongation, 5.7 per cent on 2 inches;
reduction of area 10 per cent; it analyzed Si 0.65; S 0.3; P 0.04;
Mn 0.15.
In the process of annealing the carbon only is affected, being con-
siderably reduced in amount; what remains is partly free and partly
combined. An annealed sample containing 0.6 per cent free carbon and
0.4 combined ii considered good.
Mr. Percy Longmuir places the average silicon for good malleable
castings at 0.6, sulphur 0.3, phosphorus 0.05, and combined carbon 3
to 3.5 per cent.
Ordinary or Reaunuir Malleable Cast Iron
Analyses Before and After Annealing
387
Constituents
Total carbon
Silicon
Sulphur
Phosphorus. .
Manganese. .
After pro-
Iron as
longed an-
cast
nealing in
iron ore
3.43
.10
• 45
■ 4S
.06
.06
■ 31
.32
.53
• 53
Interesting experiments were made by Mr. W. H. Hatfield of Sheffield,
and results published in "The Foundry," Oct., 1909, by Mr. G. B.
Waterhouse.
"Three converted bars of identical composition analyzing:
Constituents
Per cent
Constituents
Per cent
Total carbon
1.64
1.64
.03
Manganese
Sulphur
Phosphorus
trace
One was packed in charcoal, another in pure quartz sand, the third
in a red hematite ore mixture, consisting of two parts old and one part
new. The pots were placed close together in the annealing oven and
slowly raised to about 800° C. This required about three days. They
were held at this temperature for 24 hours, then raised to 900° C, held
there for two days, then cooled slowly. Upon removal and breaking
the following results appeared.
No. I, from charcoal, broke short and gave a coarsely crystalline
structure showing under the microscope absolutely no free carbon.
Its carbon was 1.63 per cent, the other elements remaining unchanged.
No. 2, from sand, was fairly tough but broke without bending.
Fracture crystalline and steely. Its carbon was 0.74 per cent and again
no free carbon was found.
No. 3, from the ore mixture, bent considerably before breaking
and was fairly ductile. Its carbon was 0.15 per cent and again no
free carbon could be found, the structure being of ferrite crystals.
The experim.ents appearing to prove conclusively the possibihty cf
carbon being removed without previous formation of free or temper
carbon.
388
Malleable Cast Iron
For ihc second scries of exjxirimenls, an ordinary white iron was
taken containing:
Constituents
Per cent
Constituents
Percent
35
none
.so
Manganese
Sulphur
■ 3S
.OS
Phosphorus
The packing was the ore mixture previously referred lo.
Sami)les were heat-treated and sections were given a careful micro-
scopical examination, with the following results:
Decarburization began 54 hours after commencement of heating and
at 770° C, showing a thin skin of ferrite; the cemaining portion of the
casting retained the typical structure of white iron. 40 hours later,
during which time the temperature gradually raised to 980° C, the de-
carburized skin increased in thickness to ?i6 inch.
Fourteen hours later, at a temperature of 970° C, the interior had
broken down and free or temper carbon was apparent. During the
next interval of 60 hours, at 950° C. ver>' little change occurred. The
center showed pearlite, with a little cementite and containing temper
carbon, merging gradually into the skin of ferrite.
During the following 72 hours, the temperature was dropped to
140° C, resulting in the production of a really good sample of English
malleable cast iron of the following analysis:
Constituents
Per cent
Constituents
Percent
.65
1. 10
Sulphur 35
The author's conclusion is, that carbon is eliminated while still in
combination with the iron.
It (the elimination) begins to take place at the comparatively low
temperature of 750° C, and increases in activity with the temperature
until such a temperature is reached that free or temper carbon is pre-
cipitated.
Previous to this change the interior consists of white iron, with the
original quantity of combined carbon.
As the operation proceeds the temper carbon is gradually takiu back
into combination to replace that removed by the oxidizing influences.
American Practice 389
American Practice
The rmxtures of iron vary as the castings are thick or thin. The iron
is melted either in the cupola, the air furnace or the open hearth furnace.
The latter produces the best castings, but can only be used advanta-
geously where the output is large enough to permit of running the fur-
nace continuously.
The air furnace is most frequently used.
The castings may or may not be packed in an oxidizing material.
Sand or fire clay are frequently used.
Dr. Moldenke, who is recognized as an authority on malleable cast
iron, states: "That it is absolutely necessary to have the hard castings
free from graphite." He advises the following:
Contents: Per Cent
Carbon 3 -3.5
Silicon, heavy work, not over 0.45
SiUcon, ordinary work, not over 0.65
Silicon, agricultural work, not over 0.80-1 . 25
Sulphiu:, not over o . 05
Phosphorus, not over 0.225
Manganese, not over o . 40
"In anneaUng, the temperature of the furnace should be run up to
' heat' in the shortest safe time possible; the limit is the danger of injury
to furnace. Then the dampers should be closed and the temperature
evenly maintained for 48 hours. The furnace should then be gradually
cooled to a black heat before dumping. 36 hours are usually required
to bring the oven up to heat.
The entire process occupies about seven days. The annealing tem-
perature is 1350° F. and this must obtain at the coldest part of the fiu:-
nace, usually the lower part of the middle of the front row of pots.
A difference of 200° F. in temperature is often found at different
parts of the furnace.
Cupola iron requires an annealing temperatvure 200° F. higher than
that from an air furnace.
The fuel ratio of an air furnace runs from i to 2 to i to 4.
Loss in silicon about 35 points.
Temperatures should be carefully watched and measured with a
Le Chatelier pyrometer."
The Doctor has much to say about the danger of injury to the melted
iron in the bath, from oxidation. His practice was to have three tapping
spouts at different levels, so that for an 18-ton furnace, three taps of
6 tons each may be made at intervals, tapping at the upper hole first
and then in order from upper to bottom hole.
3<)o Malleable Cast Iron
Mr. II. i:. Dillcr, in the Journal of The American Foundrymen's
Association, Vol. XI, Dec, iyo2, says:
The hard casting should have its carbon practically all in the com-
bined state, while the annealing process should convert this to the so-
called temper, or annealing carbon.
In the manufacture of malleable castings the special make of iron
called '.Malleable Bessemer' or 'Malleable Coke Iron' is the principal
material used. The charcoal irons, while unequalled for value, arc con-
fined to the regions where they can compete with the cheaper coke
irons.
The composition required is as follows:
Per cent
Silicon o . 75 to I . so
Sulphur, below 0.04, if possible
Phosphorus, under. . . .0. 20
With the pig iron, hard sprues funannealcd scrap), steel and also malle-
able scrap are charged. The latter two materials are very good to add
to the mixture, as they raise the strength of the casting very consider-
ably.
Too much must not be added, as it would reduce the carbon to a
point where fluidity and life in the melted metal is sacrificed.
The most serious objection to cupola iron is its poor behavior under
bending test, the deflection being very slight. Test bars from this
(lass of iron seldom run above 40,000 pounds per square inch in tensile
strength, while with furnace iron, there is no dilViculty in getting a few
th:)usand pounds more.
The metal may be tapped from the furnaces into hand ladles; or it
may be caught in crane ladles, carried to the distributing point and there
emptied into the hand ladles.
When tapped into hand ladles, time is a serious item, for the begin-
ning and the end of the heat will be two diCferent things.- The latter
iron will be inferior as it was subjected to the oxidizing efTect of
the flame much longer than the first part. This difiiculty is some-
what remedied by pouring the light work first, the heavier pieces
coming later, when the silicon has been lowered too much for good light
castings.
The gating should be done to avoid the shrinkage effects as much
as may be. The little tricks that can be applied make a surprising
difference in the molding loss. Some malleable works seldom lose
more than 10 per cent, while in others 20 per cent and over is the
rule.
After the castings have been tumbled they go to the annealing room,
American Practice
391
where they are packed in mill cinder or iron ore, in cast-iron boxes.
These are carefully luted up and heated in suitably constructed ovens,
foir five or six days.
• It usually takes from 36 hours to 48 hours to get the oven up to heat,
the temperature ranging from 1600° to 1800° F. in the oven, the boxes
having a somewhat lower temperature at the coldest point.
When the fires are extinguished, the dampers are closed tight, all
air excluded, and the oven allowed to cool very gradually; often only
400" F. the first day.
After the castings come from the annealing oven, they are again
tumbled to remove the burnt scale; then chipped and ground for ship-
ment.
A well-annealed casting should not have much over o.o5 to 0.12
per cent combined carbon remaining in it. There is a material difference
between the strength of an over-annealed casting and a normal one.
Fig. iio. -
36'/0" X ff'4" ^ d'O"
-Typical American Air Furnace.
Two bars were taken from each of five heats. One from each set
was given the usual anneal and the others reannealed. The average
tensile strength of those annealed as usual, was 50,520 pounds 'per
square inch, and the average elongation 6M per cent in six inches.
The reannealed set had an average tensile strength of 43,510 pounds
per square inch; the average elongation was 6h per cent in six inches.
Over annealing had therefore cost the metal some 7000 pounds of its
strength.
'Malleable' can be made up to 60,000 pounds per square inch, though
this is not advisable as the shock resisting qualities are sacrificed.
Prof. Ledebur determined by experiment that the higher the silicon
the lower the annealing temperature required, and the higher the tem-
perature and silicon the quicker the change. He used five samples:
1 with 0.07 silicon. Could not be annealed.
2 with 0.27 silicon. Required temperature almost at melting point.
3 with 0.80 silicon. Began to anneal at 1675° F-
4 with 1.25 siHcon. Began to anneal at 1200° F.
5 with 2.10 silicon. Began to anneal at 1200° F.
393
Malleable Cast Iron
Specificalions for Malleable Castings of J. I. Case Co.
Tensile strength per s(|. in., 35.CXX) to 50,000.
Hi(jngation, 1.5 in 4 in.
Transverse test for O bar .8 inch diameter on supports 12 inches
ai)art, must show 1750 pounds to 2,400 pounds Ijreaking strength and
dcQection of not less than 0.31 inch.
Drop Test. — A bar .8 inch diameter on supports 12 inches apart must
not break under less than 1650 inch pounds, the drop being 22 pounds
and the first drop through 3 inches, second 4 inches and so on until
rupture occurs.
Torlional lest should closely approximate the tensile strength.
Bending Test. — Pieces from :>ia to 9i8 inch thick and from i to
3 inches wide, should bend over on themselves, around a circle equal
Fig. III. — .^nnealing-Ovcn equipped for Gas.
in diameter to twice the thickness of the piece and bend back again
without break.
The anneal is specified at not less than 72 hours for light and 120 hours
for heavy work.
Comparison of Tests made in iSSj wilh those made in igo8
jS8j By Prof. Ricketts
?4-inch D bar, tensile strength, 30,970 to 44,290 per square inch.
Elongation, 1.8 inches in 5 inches.
Bars I by .33, tensile strength, 32,750 to 36,990 per square inch.
Round bars, 'A inch diameter, tensile strength, 36,200 to 44,680 per
square inch.
Round bars, ?< inch diameter, tensile strength, 26,430 to 34,600 pet
square inch.
Compression, 108,900 to 160,950 pounds per square inch.
American Practice 393
igoS
Bars ,l2-inch D, tensile strength, 52,000 to 59,000 per square inch.
Larger sections, tensile strength, 42,000 to 47,000 per square inch.
Dr. Moldenke states that the tensile strength should run from 40,000
to 44,000.
The Iron Trade ReNaew gives the production of malleable castings in
1903 for the United States and Canada as 750,000 tons.
Combined output of the rest of the world 50,000 tons.
rilAP'IKK X\II
STEEL CASTINGS IN THE FOUNDRY
There is a great demand on ihe part of foundr>Tncn for an appliance
to successfully melt steel in small quantities; permitting small steel
castings, or castings for which the demand is immediate, to be made in
the gray iron foundrj'. Many eCforts have been made to realize this
desire, but so far have met with indiflerent success. There are several
appliances offered to manufacturers, some emploj'ing the Bessemer
converter, others the electric furnace in connection with the cupola.
Men cspeciall}- skilled are required to manipulate steel furnaces. The
processes of mixing and melting the metal and annealing castings differ
so radically from those of the gray iron foundry, that in the present
undeveloped state of steel founding on a small scale, steps on the part
of the foundryman in that direction should be taken with extreme
caution.
Mr. Percy Longmuir defines ordinarj'^ steel "as iron containing from
O.I to 2 per cent of carbon in the combined form, which has been sub-
mitted to complete fusion and poured into an ingot, or mould, for the
production of a malleable or forgeable metal."
" Mild steel contains about 0.2 per cent carbon; the element increasing
as the harder varieties are approached, being highest of all in the tool
steels."
"The mechanical eflect of this carbon is shown in the following table."
Material
Mild steel. .
Tool steel . . ,
Carbon
Silicon
Sulphur
Phos-
phorus
.02
.02
Tenacity
in tons
per square
inch
20.00
60.00
Extension
per cent
on two
inches
50.0
SO
Contrac-
tion
percent
of area
70.0
10. o
"Within Hmits, an increase of carbon is accompanied by an increase in
tenacity and a decrease in ductility, each increment of carbon showing
distinctly these increases."
"The following classification embraces the most familiar tempers of
Bessemer, Siemens and crucible steel."
394
Steel Castings in the Foundry
395
Class of steel
Bessemer steel ■{
Siemens or open hearth.
Crucible steel .
Content
of carbon
Purpose
.20
Ship and boiler plates, sheets, etc.
.25
Axle steel.
.03
Tire steel.
.03
Rail steel.
• SO
Spring steel.
.20
Boiler plate.
.65
Spring steel.
I 30
Tool steel.
.90
Chisel steel.
1. 10
Large files, drills and similar tool steels.
1.20
Turning tool steels.
1.40
Saw file steels.
I. SO
Razor steels.
A steel containing o.io per cent carbon is unaffected in hardness by
quenching, while one containing i per cent carbon becomes so hard under
same conditions that it will scratch glass.
Manganese is present in all commercial steels, varying from traces up
to I per cent. It promotes soundness and neutralizes the effect of
sulphur.
SiHcon tends to the production of sound metal; while it is present in
insignificant quantity in forging steel, in casting steels it may exist to the
extent of 0.3 per cent.
Phosphorus produces an exceedingly brittle, cold short metal. Pure
steels contain 0.02 to 0.03 per cent.
Usual specifications limit the phosphorus content to 0.06; at o.i the
danger limit is reached.
Steels containing appreciable amounts of sulphur are red short. In
high quality of steels the sulphur content runs about o.oi per cent.
Ordinary specifications place the limit at 0.04 per cent.
The variations in the carbon content to suit various requirements are
showTi in the following table:
Purpose for which the steel, in the form of a hardened or
steel
tempered tool, is suitable
.50
Springs.
60
Stamping dies.
65
Clock springs.
75
Hammers, shear blades, axes, mint dies.
80
Boiler punches, screw dies, cold sets.
90
Edge tools, slate saws.
95
Circular saws, pins.
00
Cold chisels, cross-cut saws.
10
Drills, large files, hand saws, mill picks.
20
Granite and marble saws, mill chisels.
30
Harder files, cutters, spindles, turning tools.
40
Saw files.
50
Turning tools for chilled rolls, razors and surgical instruments.
.V)6
Steel Castings in ihc- Foundry
Tlic follnwiii)^ tabic is taken from I'ruf. J. (J. Arnold'b "Influence
of C"arl)iin nii Iron."
MiiCHANicAL Properties " Normal Steels "
Carbon
Elastic limit,
tons per
square inch
Maximum
stress, tons
per square
inch
Elongation
Reduction
of area
08
12.19
21.39
46 6
7.«.8
.21
17.08
25 39
42.1
67.8
.38
17. 95
29.94
34. 5
S6.3
■ 59
19.82
42.82
19.9
22.7
•89
24.80
52.40
13 0
15 4
1.20
35-72
61.64
8.0
7-8
1.47
32.27
55-71
2.8
3 3
"Normal steels" represent the rolled bars heated to 1000" C. and
cooled in air.
"Comparing this table with the foregoing statements, it appears that
as pearlite replaces ferrite, the maximum stress increases, continuing
lo do so until a structure consisting of pearlite and very thin meshes of
cementite is reached. Further increase in carbon resulting in greater
dispersal of free cementite is associated with a decrease in maximum
stress."
Bessemer Process
The Bessemer process consists in l)lowing a large volume of compressed
air through a bath of molten pig iron; the oxygen of the air combining
with carbon, silicon and manganese to form oxides. That combined
with carbon passes off as gas while with silicon and manganese slags are
formed.
On removal of carbon, silicon and manganese, assuming that sulphur
and phosphorus are low, a product resembling wrought iron is obtained.
Meantime during the process of o.xidation, there is a rise in temperature
sufficient to maintain mild steel in a fluid condition. The oxidation of
silicon has the greatest effect in producing the rise in temperature. The
irons must be low in sulphur and phosphorus, as these elements are not
removed. An average content of 2.5 per cent silicon in the pig iron gives
the best results. Higher than this, the heats are liable to require scrap-
ping; while with a lower content of silicon there is danger of "cold
blows." The melted metal is taken directly from the cupola, led by
runners to the converter.
The Baby Converter
397
The Baby Converter (Robert)
This consists of a steel shell mounted on trunnions, so that it may be
properly rotated. It is flattened on the back and lined with siUca brick
or ganister. On the flattened side the tuyeres are introduced horizontally.
The surface of the metal lies approximately at the bottom of the
tuyeres so that the blast may impinge upon it. The blast is from 3 to
4 poimds per square inch and means are provided for regulating it. The
tuyeres being inchned radially, a rotary motion is imparted to the molten
metal by the blast.
In some cases the surface of the metal may be above the tuyere level,
but seldom exceeds that by more than three or four inches. The high
tuyere level permits some of the air to escape and burn on the surface
of the bath ; carbon monoxide is formed in the bath by the oxidation of
the carbon.
The combustion of carbon monoxide gives rise to considerable heat,
which is absorbed by the bath. To this reaction is due the higher tem-
perature of the side blow converter.
The Tropenas converter has a double row of tuyeres which are hori-
zontal when the converter is vertical. They are not radially inclined
as in the Robert. The surface of the metal is at the bottom edge of the
lower row of tuyeres; the blast is always on the surface of the metal.
When blowng the converter is slightly inchned, causing the direction
of the tuyeres to slope towards the surface of the metal. During the
early stage of the blow the lower tuyeres only are used; but on the
appearance of the carbon flame the upper row is opened. The carbon
monoxide, partly consumed by air from the lower tuyeres, is supplied
with sufficient oxygen for complete combustion by that from the upper
row, generating additional heat.
Recarbonization is effected in the converter or in the ladles according
to the character of the composition required.
The chemical changes taking place in a two ton Tropenas converter
are given as follows :
Constituents
Cupola
metal
Afters
minutes
blowing
After 12
minutes
blowing
After 14
minutes
blowing
After 18
minutes
blowing
End of
blow
Fin-
ished
metal
Graphite
Combined car-
bon
Silicon
Sulphur
Phosphorus
Manganese
3.180
.350
2.310
.037
.054
610
2.920
• 340
1.620
.037
.053
.600
2.900
.466
■ 03S
054
.101
2.300
.382
.036
.054
.040
.860
.084
.038
.051
.040
.100
.074
.038
.050
.042
.240
.326
037
.058
1.080
398 Steel (astinps in the Foundry
Theoretically the feeder on a steel casting should sink due to shrinkage.
If, however, instead of sinking, a rise is shown, this is clear evidence of
internal unsoundncas or sponginess. To prevent this result one of the
first essentials lies in having the steel thoroughly dead melted or " killed"
before casting. A properly "killed" steel pours quietly and settles
down gently in the mould. " Wild metal " acts in the opposite way and
in some cases is rejjrescnted by an over-o.xidized metal.
A distinction must l>c drawn between a "pipe" and a blow hole.
The former is due entirely to contraction or shrinkage in passing from
the liquid to the solid state and must be obviated by feeding.
"Blow-holes" are entirely diiTerent from "pi{>es" and are formed by
the liberation of gases absorbed during the melting process.
In considering the character of these gases, ox>gcn naturally arises
first, owing to the strong atTmity between iron and o.xygen. There is
every reason to suppose, however, that the oxygen absorbed when the
iron is molten, remains stable at low temperatures as an o.vide, and in
the absence of a deoxidizing agent this ferrous o.xide is intermingled with
the iron. O.xygenated steel is "dr>'" under the hammer and this con-
dition is not necessarily due to blow-holes, but to "red-short" metal.
Further, if free oxj-gen were present in ciuantitj' in the gas contained in
a blow-hole, its skin would show an oxide film.
The majority of blow-holes have bright surfaces; comparatively few
show colored tints, ranging from a straw to a blue, due to oxidation.
These colored blow-holes owe their o.xidized film, not to free oxygen
liberated by the iron, but to air mechanically trapped during casting.
Analyses of the gases seldom show more than traces of oxygen. Mr. E,
Munker reports sixty-seven analyses of gases evolved by molten pig
iron; the highest content of oxygen in the series is found at 0.8 per cent.
Average analyses of gases in blow-holes give results of the following
order: Percent
Hydrogen 75 '
Nitrogen 23
Carbon monoxide 2
The actual amount of these gases absorbed depends to some extent
on the temperature and composition of the bath. While fluid the gases
are retained; but with a fall in temperature after casting they are evolved.
Those set free by a fall in temperature bubble through the pasty mass, the
trapped bubbles representing blow-holes in the casting. As the tem-
perature continues to fall less movement is offered and the gases cannot
force passages through the stiffening metal. Hence more bubbles are
trapped. Finally a stage is reached at which the mass becomes rigid
and the further formation of blow-holes becomes impossible.
The Baby Converter
399
The author's conclusions from the investigations of Wahlberg are:
"i. If no internal movement is possible in the soHdifying steel, the
gas cannot disengage itself and so leads to the formation of blow-holes."
. "2. The presence of silicon and manganese lead to the retention of
the gases until sohdification is complete, hence preventing the formation
of blow-holes."
Methods of prevention include:
"i. Liquid compression.
"2. Additions to the steel of silicon, manganese or aluminum. Each
of these elements acts powerfully on the oxygen or the oxides of iron,
combining \vith the o.xygen to form slag."
" Aluminum will remove carbonic oxide. There is, however, no reason
to suppose that it will remove either hydrogen or nitrogen."
"There are grounds for the belief that silicon, manganese and alum-
inum increase the solvent power of the steel for hydrogen and nitrogen
and that these gases remain dissolved."
Brinell found that to produce an ingot of perfect density in the absence
of sihcon, 1.66 per cent of manganese is necessary. In the absence of
manganese 0.32 per cent silicon is required; and with no manganese or
sihcon 0.0184 per cent of aluminum is sufficient to produce a perfectly
sound ingot. Or e.xpressed in another way he states that aluminum is
90 times as effectiv'e as manganese and 17.3 times as much so as sihcon,
in removal of gases.
Metalhc borides are suggested by Weber for removal of oxygen; these
in conjunction with ferrotitanium tend to removal of nitrogen.
The casting temperature exercises a great influence upon the properties
of the metal. These are found to rise and fall with the temperature
above and below the casting heat, as shown by the foUowing table:
Analyses
Maximum
stress,
tons per
square
inch
Elonga-
tion,
per cent
in
2 inches
Reduc-
tion of
No.
Carbon
Si
Mn
S
P
per cent
80 A....
81 A....
82 A....
83 A....
• 29
.29
.29
.29
.07
.07
.07
.07
.16
.16
.16
.16
.07
.07
.07
.07
.06
.06
.06
.06
24.2
27,2
27.0
25.5
9-5
24.0
12.5
8.0
18.0
32.3
17. 5
12.0
These steels were poured from one large ladle at intervals of a few
minutes. They are exactly of the same analysis; the bars were annealed
together, each bar receiving exactly the same treatment, and apart from
variation of casting temperatures, the conditions were the same for all.
These results have been repeated many times. WTien the steel is poured
at an excessive temperature, similar ones are always obtained.
400
Steel Castings in the Foundry
Annealing
The following is extracted from McWilliams and Longmuir's "Gen-
eral Foundry Practice."
Steel castings are usually annealed in the rcverbcratory gas furnace.
The annealing recommended by Prof. Arnold for general work is to heat
the castings up to about 950° C. keeping them at that temperature for
about 70 hours, then luting the furnace and allowing them to cool slowly
for 100 hours.
The Clinch-Jones annealing furnace is highly spoken of, the controlling
idea being that while the castings arc heated in a mufHe, by keen flames
outside the walls of the muffle, virgin gas from the producer is allowed
to come into the muffle and combine with all the oxygen that may enter,
thus preventing it from getting to the castings to scale them by oxidizing
at their surfaces. A cut of this oven is shown on page 266 (McW. & L.).
The micrographs (McW. & L.) show the structural changes produced
by aimealing. It should be remarked that the unannealed bar. Fig. 112,
(McW. & L.) ?4-inch diameter when bent over a -^s-inch radius broke at
43°. After annealing, same bar bent double without fracture.
after annealing
Fig. 112.
Fig. 113.
Fig. 113 (McW. & L.) shows the structure of a portion of a large
open hearth casting, having originaUy the same structure as the unan-
nealed part of Fig. 112 after insuflicient annealing. When thoroughly
annealed the structure was as shown in Fig. 114.
A test bar i inch square as shown in Fig. 113 broke at 40°; while one
ft
Tropenas Process
401
as per Fig. 114 bent at 101° without fracture, showing tensile strength of
T,^ tons per square inch; elongation 30 per cent; reduction of area 41
per cent. The composition of the casting was C.C. 0.24, Si 0.15,
Mn 0.8, P 0.04, S 0.05.
Fig.
114.
Other micrographs of most interesting character are shown on pages
293 to 297 and 338 to 354 (McW. & L.).
The process of annealing must be varied to suit different compositions
and purposes for which the steel is provided.
Tropenas Process
This process was patented by Alex. Tropenas of Paris in 1891; the
first converter, 800 pounds capacity, was erected at the woriis of Edgar
Allen & Co., Ltd., Shefi&eld, Eng., and introduced into the United States
It produces hotter steel than any other process. The steel may be
carried for considerable distances in hand ladles or shanks and poured
into small castings.
The Tropenas process consists in melting a calculated mixture in the
cupola, transferring the metal to a special type of converter and its
conversion to steel therein. The reactions are identical with those of
the Bessemer and open hearth furnaces; the difference lies in the manner
of producing these reactions. The converter is designed to conserve
and increase the heat as much as possible and by preventing evolution
in the bath, to keep out any gases not necessary for or caused by the
403
Stcfl Castings in the Foundry
(Iccarburization, mechanical disturbance, gyration or ebullition of the
luith is reduced to a minimum.
The converter is in general similar to the Hcsscmcr converter, the
particular difference lacing in the location and construction of the
tuyeres.
Figs. 215 and 216, pages 307 and 308 McW. & L. give fair illustra-
tions of the device. The operation consists in melting the iron in the
cupola precisely as for gray iron castings, except that enough for the
charge must be gathered at the first lapping. The melted iron is then
transferred to the con\crter and skimmed clear of slag. The converter
is so adjusted that the \v\v\ of the metal reaches exactly to the lower edge
Fig. 1 15. Fig. 116.
of the bottom tuj'cres, so thai the blast will strike exactly upon the
surface of the metal. The longitudinal axis of the converter should
make an angle of from 5° to 8° with the vertical. This is a matter of
importance and extreme care must be taken to obtain the correct position
before applying the blast. The upper tuyeres are closed and the blast
turned on with about 3 pounds pressure.
If the composition of the iron is correct and it has been melted hot,
sparks and smoke will be emitted from the con\'erter for about four
minutes, then flame appears which gradually' increases in volume and
brilliancy. After about ten minutes, what is known as "the boil"
appears. In a few minutes this dies down considerably, and the blow
remains quiescent for a time. Then the flame increases again, attains
the maximum briihancy and finally dies down for the last time.
Chemistry of the Process 403
This is the end of the blow, the carbon, sihcon and manganese having
been reduced to the lowest limits.
The converter is now turned down, the blast shut off and a weighed
amount of ferrosilicon, ferromanganese or silicon speigel added to
recarbonize the steel to the desired point. The steel is now ready for
casting. On account of its great fluidity and thin slag it may be poured
over the lip of an ordinary ladle, instead of from one with a bottom pour.
Claims made for this process.
1. The form of the bottom of the converter gives a greater depth in
proportion to the surface area and cubic contents than any other pneu-
matic process, preventing the disturbance of the bath when blowing.
2. The sjonmetrical position of the tuyeres with respect to the center
tuyere prevents any gyrating or churning of the bath. This is directly
opposed to all other processes.
3. The special position of the bottom tuyeres during blowing, so that
they are never below the surface of the bath, reduces the power necessary
for blowing; as only enough air is introduced to make the combustion
and not to support or agitate the bath.
4. The oxidation of the metalloids takes place at the surface only, the
reaction being transmitted from molecule to molecule without any
mechanical disturbance.
5. The addition of a second row of tuyeres completely burns the CO
and H produced by the partial combustion of carbon and the decomposi-
tion of moisture introduced with the blast and this increases the tem-
perature of the bath by radiation.
6. Very pure steel is obtained, as the slag and the iron are not mixed
together.
7. There is a minimum of waste on account of the bath being kept
comparatively quiet.
8. Less final addition is required on account of the purity of the steel
and its freedom from oxides.
Chemistry of the Process
No fuel is needed in the converter. The increase in temperature after
the melted metal is introduced is occasioned by the combustion of the
metalloids during their removal.
These elements are carbon, silicon and manganese. The oxidation
of the silicon furnishes by far the greatest part of the useful heat. Prof.
Ledebur has calculated that the rise in temperature of the bath due to
the combustion of i per cent of each of the constituents is as follows:
Silicon 300° C; phosphorus 183° C; manganese 69° C; iron 44° C;
carbon 6° C.
404 SfccI Castings in ihc I'oundry
It is ncccssar)' that liie composition of the bath before blowing should
be that which has been found to give the best rc-sulLs.
Sulphur and phosphorus are as unaffected here as in any other add-
lined furnace and the content of those elements in the finished steel will
depend on how much the stock melted contained.
The cupola mixture generally consists of low phosphorus pig iron and
steel scrap, composed of runners, risers and waste from previous heats.
As much as 50 per cent scrap may be carried successfully. The mixture
must be made in such [iroportions that the analysis after melting will be:
Per cent
Silicon 1 . 90-2 . 25
Manganese o. 60-1 . 00
Carbon, about 3 00
The result of low silicon is to make the blows colder; that of high
silicon to make the blows unduly long and to increase the wear on the
lining.
Manganese should be kept within the limits specified. Low man-
ganese tends to make the slag thick. High manganese makes the blow
sloppy and corrodes the lining.
During the first period of the blow, the silicon chiefly is oxidized and
the carbon changed from graphitic to combined. The manganese is the
most active clement in the middle of the blow, being most rapidly
eliminated at the boil. The last period brings the carbon flame, and the
indications are so plain that it is feasible to stop the blow before all the
carbon is burned out, thereby reducing the amount of carburiser needed.
In addition to these elements a certain amount of iron is unavoidably
oxidized and the total loss of all elements included is about 12 per cent.
Converter Linings
The converter is generally lined with an acid or silica lining. ' Success-
ful experiments have been made with a basic lining (dolomite), but it has
not been developed commercially. Special shaped blocks to fit the
converter or the regular standard shapes may be used.
The material must be of the highest grade silica stock, burnt at the
highest possible kiln temperature. It usually contains from 95 to 97
per cent SiO.>, and is practically free from lime and magnesia.
Another method in frequent use is to run ground ganister around a
collapsible form. This probably is the cheapest method. Before making
the first blow, the converter is made white hot by a coke or oil fire.
Mr. J. S. Whitehouse of Columbus, Ohio, in a paper read before the
American Foundrymen's Association, states that the claims which were
Converter Linings 405
made for the side blow converter, when first introduced into America
were, to say the least, absurd. Many failures were made by employ-
ing inexperienced workmen, who had only limited instructions from
experts sent out with the apparatus and the results were frequently
disastrous.
A year's experience, at least, under proper instruction is required before
a man can become a competent blower. He must be able to tell the
temperature of the metal soon after the flame starts and to judge the
silicon by the first period. He must tell when the blow is iinished from
the slag as well as by the flame. He must know how to keep the lining
in the best shape to get all the heat possible from the process, and the
hundred little kinks of the trade, which, as a rule, the expert will never
impart, but are obtained only from experience.
A man with the above qualifications will blow with a loss of less than
17 per cent — about 15 per cent.
With proper blowing the main loss comes from the silicon in the charge,
usually 2 per cent, which is oxidized together with iron and manganese
to form the slag.
Mr. Whitehouse learned to blow with 2 per cent sihcon, but for the
past few years has been blowing iron, analyzing from 0.90 to 1.25 per
cent silicon from the cupola, and often has been obliged to use scrap
while blowing.
There is an advantage in the increased amount of scrap which can be
carried, as it cuts down the cupola' loss by increasing the amount of
carbon in the charge. For example : He charges 50 per cent pig carrying
about 3.75 per cent carbon and 50 per cent scrap having 0.25 per cent
carbon. Tests from such iron from the cupola give 3.25 to 3.50 per cent
carbon, showing a gain of 1.25 to 1.50 per cent carbon, taken from the
coke, instead of purchased in the pig iron. 50 per cent scrap can be
melted in the cupola, using only i2i/i per cent coke, but the blower must
have a complete knowledge of cupola practice. Most blowers use too
much volume and too high pressure of blast to get the best results. With
low silicon the volume and pressure of blast must be low. No two blows
will act ahke and require different treatment, which can be determined
by the flame, but which he is unable to describe.
It is as necessary for the blower to regulate the air valve to get proper
combustion as it is for the melter to adjust air and gas valves. With
ordinary care the steel produced in a converter is very uniform in carbon
and silicon; ihore so, he thinks, than in the open hearth. The greatest
variation seems to be in manganese. The temperature of the metal
and the condition of the slag cause more variation in the converter than
in the acid open hearth. It is possible to run several weeks without
4o6
Steel Castings in ilic I'liundry
taking an analysis and find at the end of the run very little variation in
tlif dements.
While tliis is jjossible with the open hearth, it is not |)ratticed on
account of the risk. It is, however, frequently done in converter practice.
The method of making the molds is identical with that followed in the
open-hearth practice.
Fig. 117. — .*\rrangement of the Cupola and Converter. The Metal is
Handled by a Four-ton Pneunaatic Jib Crane.
An ordinary converter shop, with one two-ton converter is capable of
producing between 100 and 150 tons of good castings per month, blowing
three times a week. He concludes with saying that the management
must be good and the salaries paid the officers as reasonable as possible,
otherwise the shop is fore-doomed to failure, regardless of the quaUty of
the product.
At the Cincinnati Meeting of the American Foundrv-men's Associa-
tion, Mr. Whitehouse, in reply to various inquiries, made the following
statements:
Converter Linings
407
When the flames show that the blow is getting very hot, scrap is
thrown in at the top of the converter until it cools down. The scrap is
as small as can be conveniently handled and is not preheated.
. The blast pressure averages from 2.25 to 2.50 pounds.
Fig. 118. — Pouring the Iron into the Converter before the Blow.
Sometimes, after the silicon is reduced and during the blow, steel scrap
is thrown into the converter.
The carbon can be varied by the final additions.
It is usual and customary to blow the heat down till the flame drops;
the carbon is then about o.io per cent. The carbon is then raised by the
addition of melted pig iron or pulverized coke. The carbon can be
raised as much as desired. If more than 0.40 or 0.50 per cent carbon is
4o8
Steel Castings in the Foundry
required, the blow is stoppcfl before completion. It is nistoraary to
blow down to .o<_t ur o.io per cent carbon, then to recarbonize with ferro-
mangancse, melted pig iron and s|)iegcleisen. I usually use coke. If
ferromanganesc is melted in a small cuix)la, as has been done in the East,
the loss is very heavy. The most economical practice is to throw the
ferromanganesc into the converter at the end of the blow. The usual
custom is to add ferromanganesc and then pig iron.
"My practice is never to reline entirely. .\t the end of the heat day,
the converter is cooled off, patched up, dried out and is then ready for
the next day. Where the converter is
ed until it is cut out, the lining re-
moved and then renewed, there is a great
loss of iron."
The practice is to blow just at the sur-
face, with the blast impinging slightly on
he metal. During the blow the tuyeres
arc submerged, and if the pressure is sud-
ilcnly stopped for any cause the iron will
run into the wind box. The converter is
so placed that the blast will strike the
surface of the metal at an angle of 175°
to 171°. He does not use a second row
of tuyeres. Upon starting to use the
converter, there was an upper row of
tuyeres, but they were subsequently dis-
carded. The lower tuyeres furnish all
the blast required.
Formerly he used bull ladles in pour-
ing small castings and experienced no
trouble. At the present time, the entire
heat, sometimes consisting of castings
weighing less than thirty pounds, is poured with a thousand-pound
ladle.
The following extract is from the Foundry, Jan., 1910, describing the
equipment of the recently erected steel foundry of the Vancouver En-
gineering Works, Ltd., Vancouver, B.C.
The cupola is the Standard Whiting t\pe, having a rated capacity of
six to seven tons per hour.
Iron is tapped from the cupola into a six-thousand-pound ladle, carried
by a pneumatic crane. Two taps are made to obtain a full charge for
the converter.
The composition of the iron is as follows: Si. 1.80 to 2.00; S. 0.04;
1
ill
ffi
J
Fig. 119. — View of One End cif
the Foundry, Showing the Con-
verter Discharging Steel into a
Ladle.
Standard Specifications for Steel Castings
409
Phos. 0.04; Mn. 0.60 to 1.50. The cupola charge is so proportioned as to
give about one per cent manganese. Steel scrap is available as desired.
The converter, of two-tons capacity,
is of the standard Whiting type (Tro-
penas) and is lined with ganister, sand
and fireclay. This lining, if cared for,
will give from 180 to 200 blows. The
air pressure of blast to converter ranges
from three to five pounds per square
inch, regulated by valve on operator's
platform.
The blowing operation requires from
15 [to 20 minutes, varying with the
percentage of metalloids in the iron.
The temperature of the bath depends
upon the rapidity of the blow.
Reduction in the weight of metal is about 18 per cent.
The steel comes from the converter at 1700° C, insiuring sufficient
fluidity to give sharp, sound castings of light section.
Fig. 120. — The Converter in
Operation.
Standard Specifications for Steel Castings Adopted
BY American Association for Testing Materials
Process of Manufacture
1. Steel for castings may be made by the open hearth, crucible or
Bessemer process. Castings to be annealed or unannealed as specified.
Chemical Properties
2. Ordinary castings, those in which no physical requirements are
specified, shall contain not over 0.40 per cent carbon, nor over 0.08 per
cent of phosphorus.
3. Castings which are subject to physical test shall contain not over
0.05 per cent of phosphorus, nor over 0.05 per cent of sulphur.
Physical Properties
4. Tested castings shall be of three classes, hard, medium and soft.
The minimum physical qualities required in each class shall be as follows:
Properties
Hard
castings
Medium
castings
Soft
castings
Tensile strength, pounds per inch
8S.000
38,250
15
20
70,000
31,500
18
25
60,000
27,000
Elongation per cent in 2 inches
22
30
4IO Steel CastiiiRS in the Foundry
5. A test to destruction may Ix; substituted for tensile test in the case
of small or unimportant castings, Ijy selecting three castings from a lot.
This test shall show the material to be ductile, free from injurious defects,
and suitable for the purjioscs intended.
A lot shall consist of all castings from the same melt, or blow annealed
in the same furnace charge.
6. Large castings are to be suspended and hammered all over. No
cracks, flaws, defects, nor weakness shall appear after such treatment.
7. A si)ccimcn one inch by one-half inch (i " X y/') shall bend cold
around a diameter of one inch (1") without fracture on outside of Ijent
portion, through an angle of 120° for the "soft," and 90° for "medium"
castings.
Test Pieces and Methods of Testing
8. The standard turned test specimen, one-half inch (W) diameter
and two inch (2") gauged length, shall be used to determine the phj-sical
properties specified in paragraph No. 4. It is shown in the following
sketch. ^
9. The number of standard hgl*' — 2 ■■-->^8'^
-XT
i I
■
Fig
?4" ;^4'>*- V--i
J
test specimens shall depend
upon the character and im- "^^
portance of the castings. A ±.
test piece shall be cut cold from j^" -^ "^41
a coupon to be molded and cast
on some portion of one or more
castings from each blow or melt, or from the sink heads (in case heads
of sufl'icient size are used). The coupon, or sink head, must receive
the same treatment as the casting, or castings, before the specimen is
cut out and before the coupon, or sink head, is removed from the
casting.
10. One specimen for bending test, one inch by one-half inch (i" X
>/i") shall be cut cold from the coupon, or sink head, of the casting, or
castings, as specified in paragraph No. 9. The bending test may be
made by pressure or by blows.
11. The yield point specified in paragraph No. 4 shall be determined
by careful observation of the drop of the beam, or halt in the gauge of
the testing machine.
12. Turnings from the tensile specimen, drillings from the bending
specimen or drillings from the small test ingot, if preferred by the in-
spector, shall be used to determine whether or not the steel is within
the limits, in phosphonxs and sulphur, specified in paragraphs Nos. 2
and 3.
Open-Hearth Methods for Steel Castings 411
Finish
13. Castings shall be true to pattern, free from blemishes, flaws or
shrinkage cracks. Bearing surfaces shall be solid, and no porosity shall
be allowed in positions where the resistance and value of the casting
for the purpose intended will be seriously affected thereby.
Inspection
14. The inspector, representing the purchaser, shall have all reasonable
faciUties afforded him by the manufacturer to satisfy himself that the
finished material is furnished in accordance with these specifications.
All tests and inspections shall be made at the place of manufacture,
prior to shipment.
The following paper, by Mr. W. M. Carr, on the manufacture of steel
castings in small quantities by the open-hearth process is given herewith
in full.
Open-Hearth Methods for Steel Castings
With Remarks on the Small Open-Hearth Furnace
By W. M. Care, New York City
It is a fact that the open-hearth process for the manufacture of steel
is gradually gaining ground, as can be proved by statistics. The reason
for its supplanting other methods is mainly one of quahty. Further, the
basic open-hearth process permits a mixture of pig iron and miscellaneous
steel scrap of a lower grade and cheaper price than raw material necessary
to other processes.
With the foregoing facts in mind the author presents this article for
the consideration of prospective investors in the manufacture of steel
castings in small, moderate and large tonnages; to be more explicit,
small tonnages are capacities of melting units in one-half, one and two
tons per heat. ISIoderate tonnages are capacities of furnaces of two to
five tons per heat, and large tonnages are capacities from ten to twenty-
five tons per heat. There are thus offered possible outputs to meet
almost any requirements.
In presenting the claims, it is with the recognition of the following
advantages :
1. The small capacity furnaces cost less to install than any other
steel making devices excepting only crucible melting furnaces.
2. The economy in operation of open-hearth furnaces in any capacity
over that of any other steel-making process.
3. The certainty of results, the greater degree of control in operation
and the reduction of the personal equation to the lowest possible expres-
412
Slccl Castings in the Foundry
It is generally known to the foundrymcn that the largest production
of steel castings comes through oj^-n-hearth fumacxs of capacities uf
five to twenty-five tons per heat. Such practice is established and
retjuires constant demand to be profital^le, and investment of consider-
al;lc capital varying with the size of the plant. It has Ijcen thought that
capacities of less than five tons per heat arc not j>ossible by open-luarlh
methods, and engineers generally have dissuaded those who wish to
engage in the manufacture of steel castings either for their own con-
sumption or the trade from using open-hearth methods, since up till
quite recently the tendency has been rather to increase the capacity of
the open hearth, supposedly for economical reasons rather than to build
small units with less capacities.
The author, however, has had the opportunity to demonstrate the
possibilities of the miniature open hearth and has found from actual
practice that it is economical, and comparing operation costs with stand-
Open-Hearth Methods for Steel Castings 413
ard capacity furnaces, bears equally well in economy. This fact is
somewhat of an innovation, but nevertheless true, and it can be said
that the operating cost of the miniature open hearth is less than that
of any tyj^e of steel-producing unit or process, making steel in equal
quantity.
To assist those who may not be familiar with an open-hearth furnace
and its operation, a study of the diagram herewith, (Fig. 122) given may
be instructive. The upper part of the furnace is represented in sectional
elevation. The structure is built of refractory bricks and bound se-
curely with structural steel beams and plates at certain points not
shown in the diagram. The lower part of the furnace, usually below
the charging floor level or carried below the shop level, consists of the
chambers, connecting flues leading to a reversing valve and thence to a
regenerator stack. Referring again to the main body of the furnace it
will be noticed that the hearth, which is practically a shallow dish Uned
with "silica" sand is fused into one solid mass at a high temperature at
the time of what is known as "making bottom." This is the laboratory
where the raw material is melted and refined to steel of any desired
composition. In outline the practice is as follows and refers to the opera-
tion of a miniature open hearth fired with fuel-oil being recommended
in preference to producer gas in capacities of less than five tons per
heat.
After the furnace has been brought up to a working temperature — •
white heat — a mi.xture of acid pig iron and low phosphorus steel scrap
usually in the projjortions, one-third pig and two-thirds scrap, is charged
into the furnace, adding the pig iron first, and when that becomes
molten, following with the scrap. The whole mass subsequently becomes
liquid by means of the oil flame passing above it. At this stage the
temperature of the furnace has been lessened through the addition of
the cold stock, but it will still be at a temperature above that required
to melt pig-iron. But in order to elevate the temperature above that
required to melt steel and have it in condition to pour, the advantage
of the principle of regeneration is available. This consists in returning
to the furnace waste heat which in other types of furnaces escapes to the
stack. Without a system of regeneration it is not possible to reach a
proper steel casting temperature; that is to say, a reverberatory furnace
without regeneration gives a temperature, (where the combustion of the
fuel is supported by cold air) , less than that required to properly liquefy
steel, but with the principle of regeneration applied to such a furnace,
high temperatures are readily reached.
To understand this principle we will follow the course of the flame of
the burning oil as indicated by the arrows in the diagram. Beginning
414 Steel CaslinRs in ihv Foundn'
111 the rinht liand end oil is delivered to the burner which is shown
surrounded witii a water tooled casing It) protect the burner fittings.
The oil is delivered cither by gravity or pump pressure, but Ixiforc
reaching the end of the burner it is atomized or vaporized by air under
pressure. This air is designated as primary air and ix;rfomi.s liltle or
no j)arl in supporting combustion of the oil vapor, and the quantity of
air delivered in excess above the amount necessary to promote combus-
tion of the oil is known as secondary air. The secondary air enters the
reversing valve shown at the stack connection, passes through the right
luind regenerator, enters the uptakes below the water c<M)le<l burner
casing, performs its function and passes along the roof of the furnace, in
part, and the remainder, mixed with the products of combustion with
the strata of flame playing above the bath, enters the downtakc at the
left hand end of the furnace and in its passage to the stack gives up
the major portion of its heat to a large quantity of brick work piled
within the chamber. WTien the waste gases have passed through the
reversing valve and entered the stack they have just about enough heat
to induce the necessarj' draft. Now, after an inter\'al of twenty to
thirty minutes the right hand burner may be shut ofT, but not withdrawn
from the furnace; the reversing valve is thrown and the oil and primary
air turned on at the left hand end of the furnace. The secondan.' air
will then be diverted by the reversing valve to flow through the left hand
regenerator or checker chamber, and passing through innumerable pas-
sages in that set of checkers absorbs a large quantity of heat radiating
from the glowing bricks which became heated in the first instance by the
outgoing gases during a previous cycle of operation. This radiated heat
regenerating the secondary air will be added to the temperature gener-
ated by the burning fuel and the products of combustion will accordingly
have an increased quantity of heat to impart to the checker work at
the outgoing or right hand end. In other words, whatever temperature
may be carried in by the secondary air will be equivalent to art incr&ise
in eCTiciency of the burning fuel. Successive reversals of the fuel, pri-
mary and secondary air produce constantly increasing increments in
flame temperatures below the melting points of the refractor)' brick
works.
We have seen what can be accomplished by storing up and restoring
to the furnace waste heat from the products of coml)ustion. producing
the effect of a higher possible temperature than in any tx^pe of melting
furnace. In addition to this effect another one is quite active and that
is reflection of heat from the walls and roof of the furnace upon the surface
of the bath of metal. This latter effect, known as radio-actixnty, is more
proDOUQced in a narrow melting chamber than in a wider one and conse-
Open-Hearth Methods for Steel Castings 415
quently the result will be two factors, one a decreasing fuel consumption
and the other the possibility of superheating steel in a miniature open-
hearth. This fact has not been recognized heretofore because most open-
hearth furnaces are fired with producer gas, and since that fuel requires
peculiar furnace construction to get the best results in burning it, it has
not been found possible to make use of such fuel in a comparatively short
furnace hearth and therefore all furnaces designed to use that fuel must
have a comparatively long hearth tending mainly in the direction of
increased capacities rather than decreased. On the other hand, the length
of the hearth is not restricted where oil can be substituted for producer
gas and therefore it has been found possible to operate an open-hearth
furnace as small as 350 pounds capacity per heat. Thus a new field is
opened to make steel by the open-hearth process.
Referring again to the operating method, we saw where the bath of
metal was molten and at a moderate temperature. This temperature
was due to the fact that the metal was highly carburized, since the
presence of carbon lowers the melting point of iron. We saw how it was
possible to gradually increase the temperature of the furnace by the
regeneration of the secondary air, and with that constant elevation of
temperature, dormant chemical actions will be set up. The first effect
will be an oxidization of the silicon occurring mostly on the surface of
the metal by the oxidizing action of the flame. The product would be
silica, which combines with whatever oxide of iron might be present in
the bath of metal. The combination would form a slag of comparatively
fight weight that would rise to the surface and cover the bath. The slag
is shown in the diagram by the heavy black line. This layer of slag
prevents the metal below from direct contact with the flame. After the
removal of the silicon the next action will be the removal of the carbon.
This action is a gas-forming one and will cause a bubbhng or boil through-
out the bath. The action can be augmented from time to time by the
addition of iron oxide in the form of iron ore. As the decarburization
progresses test plugs are taken from time to time, the operator judging
the amount of carbon in the bath by their fracture and malleability.
When the carbon has decreased to a predetermined point, the boil may
be stopped or killed by deoxidizing agents such as ferrosilicon and ferro-
manganese in properly weighed amounts. The metal can then be trans-
ferred to molds. This method as outUned refers to the acid process.
In it the elements sulphur and phosphorus are not removed. The basic
process consists of a hearth fining made of magnesite. Such a lining
permits an addition of limestone to form a slag which will absorb the two
elements and make a purer steel, chemically speaking, than the acid
process, and at the same time allow the use of cheaper and irregular
4i6 Steel Castings in the Foundry
raw materials against the acid i)roccss with strictly limited chemical
comjxjsition concerning liic t\v<i elements mentioned.
With open-hearlii furnaces desi^ne<l to use i)roducer gas and which
rarely k<) i)el(nv five tons caijacity it is not possible to adapt them to
intermittent operation. Kven in the smaller producer-gas fired furnaces
the roof span is considerable, resulting in heavy stresses on the side walls.
These stresses will vary as the furnace is heated and cooled, and if such
alternations are frccjuent there is danger of collapse of the furnace. It
becomes necessary then to maintain them continuously at a steady tem-
perature. Urdcss there should be demand for regular tonnage the fuel
consumption during idle periods would lie a constant expense.
In miniature open-hearth furnaces, owing to the comparatively narrow
hearth chamber, the roof span is of course lessened and therefore what-
ever expansion or contraction therein following heatings and coolings,
will result in comparatively slight stresses, and these results decrease in
effect with the lessened capacity furnaces, and they therefore lend
themselves to intermittent operation with greater ease and lessened
liability of repairs. The miniature open hearth is most satisfactory in
the rolling tjpe with the body cylindrical, so that the stresses even
though slight will be evenly distributed, whereas in a rectangular form
the roof will always rest and thrust upon the inside walls. In fact the
miniature open hearth is not recommended to be built in the stationary
type.
In conclusion the miniature open hearth is not costly to install, is
comparatively simple to operate, gives results equal to standard open-
hearth practice, makes hotter steel than the regular op)en hearth and
can show costs equally as low per pound of molten metal in the ladle.
Comparative Cost of Steel made by Different Processes 417
Comparative Cost of Steel made by Different
Processes
From paper presented to the American Foundrymen's Association
by Mr. Bradley Sloiighlon.
Table I. — Aero Open Hearth
Raw materials
Pig iron
Heads, gates, etc
Foreign scrap
Defective castings* (account bad metal)
Ferro-alloys
Total metal
Operating costs
Cost of steel in ladle
Per 2000 pounds of steel in ladle
Price
of raw
materials
per 2000
pounds
$14.00
14.00
14 -SO
50.00
40.60
Weight
used,
pounds
300
660
1080
20
29
20S9
Per cent
used
Cost
S2
10
4
62
7
83
SO
59
S15
64
5
5ot
?2I
14
Cost
S15.64
5t
$24.49
Cost of Steel in Castings
Cost of steel in ladle 4- 65 per centt =
Less credit for heads, etc., as_scrap = .
Net cost of steel in castings
$37.68
4.62
$27.90 S33.06
* The price given for defective castings is over and above their value as scrap
See the text following for further discussion of this charge.
t The charge of $5.50 for operating costs is the figure for a 25-ton furnace and large
tonnage; that of $8.85 is for a small furnace and small production.
X Of the steel in the ladle, 65 per cent goes into castings, 33 per cent goes into heads,
gates, etc. and 2 per cent is lost in spattering, etc.
4i8
Slecl Castings in the Foundry
TAULii II. — Basic Open Hlaktu
Raw materials
Pig iron
Heads, gates, etc. . . .
Foreign scrap
Uufective castings'. .
Ferroalloys
Total metal
Operating costs..
Cost of steel in ladle .
Per 3000 pounds of steel in ladle
Price
of raw Weight
materials I tiscd,
per 3000 pounds
pounds
Percent
used
$12-75
14.00
II. IS
50.00
40.60
660
350
40
33
2133
33
2
iW
106
Cost
*6.63
4.63
1.9s
1. 00
^
»I4.87
6. lot
•ao.97
Cost
Cost of Steel in Castings
Cost of steel in laddie -i- 65 per
cent t =
Less credit for heads, etc. as scrap = . .
Net cost of steel in castings
fo3.36
4.62
$27.64
$37 S7
4.62
$32.95
• See footnote under Hearth, Table I.
t See footnote under Table I.
X Of the steel in the ladle, 63 per cent goes into castings, 33 per cent goes into heads,
gates, etc., 2 per cent is lost in spattering in pouring.
Acid Open Hearth and Basic Open Hearth
419
Acid Open Hearth and Basic Open Hearth
[When Together in One Plant]
Raw materials
Acid open hearth per
2000 pounds of steel
in ladle
O 0) Qt3
I. fcl fe O
a-o
CJ'O
Basic open hearth per
2000 pounds of steel
in ladle
Pig iron
Heads, gates, etc.,
both furnaces
Foreign scrap
Defective castings. . .
Ferroalloys
Total metal
Operating costs.
Cost of steel in ladle.
from
$14.00
14.00
14.50
50.00
40.60
1320
420
2089
Cost of Steel in Castings
Cost of steel in ladle -r 65 per cent .
Less credit for heads, etc., as scrap.
Net cost of steel in castings —
$2.10
$12.75
II. 15
50.00
40.60
$32.28
4.62
$27.66
loio
40
33
52
15H
2
iV4
$6.63
's'63
1. 00
.67
71
$13.93
6.10
$20.03
Cost of Steel in Castings
$30.81
4.62
$26.19
•J JO
SucI C'lislings in ihc Foundry
Taulk IV. — Converter
Raw materials
Pig iron
Pig iron
Heads, gates, etc
Defective castings (account bad metal)
Ferroalloys
Total metal
Operating costs
Cost of steel in ladle
Per aooo pounds of steel in Imdle
Cost of Steel in Castings
$35.18
4.62
$30.36
$38.26
Less credit for heads, etc., as scrap . .
4.62
Net cost of steel in castings
$33.64
• See footnote under Table I.
t The percentage of defective castings in converter practice will actually be less
than this, so that the cost is a little higher than justice to average converter practice
demands. In the absence of average figures, we have charged it the same as add
open hearth, with this correction.
t Operating cost, S3.50. is for one 2-ton converter making 150 tons per week. The
$5-50 per ton is a 2-toii converter with small production.
Converter, with Large Waste
Table V. — Converter, with Large Waste
421
Raw nnaterials
Pig iron
Pig iron
Heads, gates, etc
Defective castings account bad metal.
Ferroalloys
Total metal
Operating costs
Cost of steel in ladle
Per 2000 pounds of steel in ladle
Price
of raw
materials
per 2000
pounds
S14.00
17.40
14.00
80.00
40.60
Weight
used,
pounds
Per cent
used
Cost
300
15
$2.10
1360
68
11.83
660
33
4.62
20
I
.80
38
2
.77
2378
119
$20.12
3. so
S23.62
Cost
$20.12
5.50
$25.62
Cost of Steel in Castings
Cost of steel in ladle -f- 65 per cent .
Less credit for heads, etc., as scrap.
Net cost of steel in castings
S36.34
4.62
$31.72
422 Sti'd Castings in the Foundry
Table VI. — Aciu Ui'kn IIeaktu [Making Small CastincsI
Raw materials
Per aooo pounds o( iteel in ladle
Pig iron
Heads, gates, etc
Foreign scrap
Defective castings account bad metal.
Ferroalloys
Total metal
Operating costs
Cost of steel in ladle
Price
of raw
materials
per aooo
pounds
$14.00
14.00
14. so
SO. 00
40.60
$32.92 $26.27
Cost of steel in castings
Cost of steel in ladle -i- 6s per cent*.
Less credit for heads, etc., as scrap. .
Net cost of steel in castings
• Of the steel in the ladle, 65 per cent goes into castings, 33 per cent goes into heads,
gates, etc., 2 per cent is lost in spattering during pouring. In making small castings,
the loss in pouring from a bottom-poured ladle would be much larger than this, and
the cost of steel in castings would be increased Si to $3 per ton, but data is lacking
for exact estimates.
Crucible Castings
423
Table VII. —
Basic Open Hearth [Making Small Castings]
Per
2000 pounds of steel in
ladle
Per 2000 pounds of
steel in ladle
Raw materials
Price of
raw materials
per 2000
pounds
■d
.£f a
4J
(u-d
0
u
4J
0
u
0
$12.75
14.00
II. IS
so. 00
40.60
1040
660
190
200
33
S2
33
10
$6.63
4.62
1.06
S-oo
.67
$17.98
9-55
1040
660
350
300
33
52
33
17^^
15
1 1/2
$6.63
4.62
1.95
7. so
.67
Heads, gates, etc. . . .
Foreign scrap
Defective castings. . .
Total metal
Operating costs..
2123
106
$17.98
6.10
2124
106
$19.93
6.10
$19.93
9.55
Cost of steel in ladle. .
S24.08
$27.53
$26.03
$29.48
Cost of Steel in Castings
Cost of steel in ladle -^ 65 per cent .
Less credit for heads, etc., as scrap
Net cost of steel in castings
$37.05
4.62
$32.43
$42.35
4.62
$37.73
$40.05 $45.85
4.62 4.62
$35.43 $40.73
Table VIII. — Crucible Castings
Per 2000 pounds steel in ladle
Raw materials
Price of
raw materials
per 2000
pounds
-d
ll
0
$17.34
4.62
.63
.24
$22.83
35.00
$57.83
•d"
!|
1^
$25.50
14.50
14.00
125.00
40.60
1360
660
10
12
68
33
1330
660
10
12
"myi
33
looi^
Foreign steel scrap. . . .
Heads, gates, etc
Defective castings. . . .
$9.64
4.62
.63
.24
Total metal
Operating costs . . .
Cost of steel in ladle. .
2042
102
2012
$15.13
35. 00
$50.13
Cost of Steel in Castings
Cost of steel in ladle -r- 66 per cent*.
Less credit for heads, etc., as scrap. .
Net cost of steel in castings
$87.62
4.62
$83.00
$75.95
4.63
$71.33
' Of the steel in the ladle, 66 per cent goes into castings, 33 per cent goes into heads,
gates, etc. and i per cent is lost in pouring.
424
Steel Castings in the Foundry
Table DC. — Electric Furnace
Raw materials
Steel scrap
Heads, gates, etc..
Defective castings.
Ferroalloys
Total metal...
Per aooo pounds of tteel in Li :.<
Price
of raw
materials
per 20OO
pounds
l9So
14.00
125.00
40.60
Weight
used.
pound .
Per ci-nt
1330
660
66W
33
H
looW
Cost
Cost of netting steel
In ladle
Electric power at I cent per kilowatt hour
" " 2 cents " " "
3 " " "
" " 4
5
$28.81
37 96
47.11
56.26
65.41
$39 03
52.89
66.76
80.62
94-49
CHAPTER XVIII
FOUNDRY FUELS (Cupola)
The fuels available for melting iron in the cupola are anthracite coal
and coke.
Anthracite Coal
Lehigh lump is the best coal for the purpose. It produces a hot iron
and melts it rapidly. On account of the cost as compared with coke, it
is now little used in districts removed from the anthracite region.
A mixture of anthracite and coke, particularly for the bed, gives most
excellent results, especially for prolonged heats.
Coke
When bitumin dus coal is exposed to a red heat for a prolonged period
with total or partial exclusion of air, the volatile matter is driven off and
the residuum is coke, containing more or less impurities. The coal used
is of the coking variety and to produce good foundry coke should be low
in sulphur and ash. Seventy-two hom: Bee Hive Coke is most generally
used by foundrymen. This has a hard, cellular, columnar structure,
with a gray, silvery surface. The smooth, glistening appearance foimd
in much of it is due to quenching in the furnace. (Weight about 25
pounds to cubic foot.) There will be found in each carload of coke
"black-tops" and "black-butts"; the appearance of the former is due
to deposits of carbon from the imperfect combustion of the gases at the
top of the furnace. They in no way affect the value of the fuel. Black
butts, however, come from incomplete burning and contain unconverted
coal. These should be accepted only in limited quantities.
The following are analyses from different sections:
Localities
Connellsville
Pocahontas . .
Chattanooga.
New River. .
Birmingham .
Fixed
Volatile
Ash
carbon
matter
89.58
.46
.03
9. II
92.58
.49
.20
6.05
80. SI
1. 10
.45
16.34
92.38
7.21
87.29
10. 54
Sulphur
.81
.68
1. 59
.56
1.19
425
426 Foundry l-ucls
Specific Rravily iivcruKcs 1.272. Coke will absorb from 10 to 30 per
cent of lis wcIkIu in moisture, dcpcndinj; on exfKWure. After exposure
to a hard storm the increase in weight may easily be 15 per cent.
Less pressure of air, more volume anfl larger tuyere area are required
when melting with coke than with anthracite coal.
The following specifications for coke from the J. I. Case Co. are given
by Mr. Scott.
Good clean 72-hour coke, massive and free from granulation, dust and
cinder. Per cent
Moisture not over i . 50
Volatile matter not over 3- 5°
Fi.xcd carbon not under 86.00
Sulphur not over 0.75
Ash not over 1 1 ■ 50
Coke which has over 0.85 sulphur, 0.05 phosphorus, less than 85
fixed carbon or less than 5.00 ash will be rejected.
Good foundry coke should be high in carbon, low in sulphur, have
good columnar structure, and there should not be a large percentage of
small pieces in a carload. The product should be uniform.
By-Product Coke
Certain chemical works, in the distillation of bituminous coal for
ammonia, manufacture coke as a by-product. This, when especially
prepared for foundrj' purposes, gives excellent results. It is darker,
harder and more irregular in form than beehive coke. It is high in
carbon and low in sulphur, makes a very hot fire and will melt more
iron than an equal weight of beehive. The short description of the
process of making this coke by Mr. W. J. Keep is given herewith.
"The retort oven is a closed chamber from 15 to 24 inches in ^\^dth,
5 to 8 feet in height and from 25 to 45 feet long. From 25 to 50 of these
ovens are placed in a batterj'.
"The coal is charged through three or more openings in the top and
levelled off to within a foot of the roof, after which the oven is carefully
closed and sealed, in order to exclude the air. The oven is heated by a
portion of the gas driven off in the process of coking. This is not burned
in the oven itself, but in flues constructed in their walls. The heat is
conducted through the walls of these combustion flues to the charges of
coal and distillation thereof is started immediately.
"The gas which is driven off is conducted through an apparatus in
which the tar and ammonia are recovered; after which a portion of the
gas is returned to be burned in the oven flues, and the babnce disposed
of as local conditions determine.
Effect of Atmospheric Moisture upon Coke 427
"Distillation proceeds from the side walls toward the middle of the
oven and the gas is probably driven toward the center of the oven, where
it rises, forming a cleavage plane the whole length of the oven. When
the process is completed, which takes place in from 20 to 36 hours,
depending upon the width of the oven and the temperature maintained,
the whole charge is pushed out by a steam or electric ram and is immedi-
ately quenched. The oven is at once closed and, without any loss of
heat from the oven itself, is again charged with coal.
"On account of the cleavage plane through the center of the charge,
no piece of coke can be longer than half the width of the oven."
"Owing to the complete exclusion of air, there is no combustion in the
oven; and as the temperature of the oven, when the coal is charged, is
very high, there is a considerable decomposition of volatile matter with
consequent deposition of carbon upon the coking charge. As a result
the yield of coke is a little higher than the theoretical yield, as cal-
culated from the analysis of the coal. Quenching the coke outside the
ovens mars its appearance somewhat, destroying its bright, silvery
lustre, but probably results in carrying ofif an appreciable quantity of
sulphur."
"Coke made from the same coal will have a slightly higher percentage
of fixed carbon and a slightly lower percentage of ash than if made in a
retort oven."
"The quality of retort oven coke depends upon the skill of the operator,
upon the method of preparing the coal and more than all, upon the
quality of the coal used.
He further says that after having satisfied himself that it was good
coke, "in spite of its very bad appearance," by the use of several car-
loads, "from that time to this we have never had a pound of other
coke. All through 1902 the coke was so uniform and satisfactory that
we melted 9 pounds of iron with i pound of coke."
Effect of Atmospheric Moisture upon Coke
Under normal conditions, at a temperature of 70° F., 1000 cubic feet
of air, equal in weight to about 75 pounds, contains i pound of moisture.
Each pound of moisture requires the use of o.io additional pounds of
coke. Therefore, every additional i.o per cent to the moisture of the
atmosphere requires 0.03 additional pounds of coke to melt one ton of
iron.
From 20 to 40 per cent of the sulphur in the coke is taken up by the
iron in melting. This may be largely reduced by the liberal use of
limestone.
428 Foundry Iiiels
Specifications for Foundry Cokk Suggested by
Dr. Richaru Moldenke
Coke bought under these specifications should l>c massive, in large
pieces and as free as possible from black ends and cinders.
Samplitig
Each carload or its equivalent shall be considered as a unit, and
sampled by taking from the exposed surface at least one piece for each
ton, so as to fairly represent the shipment. These samples, properly
broken down and ground to the fineness of coarse sawdust, well mixed
and dried before analysis, shall be used as a basis for the payment of the
shipment. In case of disagreement between buyer and seller an indepen-
dent chemist, mutually agreed upon, shall be employed to sample and
analyze the coke, the cost to be Ijorne by the parly at fault.
Base Analysis
The following analysis, representing an average grade of foundry coke
capable of being made in any of the districts supplying foundries, shall
be considered the base, premiums and penalties to be calculated thereon
as determined by the analysis on an agreed base price:
Volatile matter r . 00 Ash 12. 00
Fi.xed carbon 85 . 50 Sulphur i . 10
Penalties and Bonuses
Moisture. — Payment shall be made on shipments on the basis of
"dry coke." The weight received shall, therefore, be corrected by
deducting the water contained. (Note. — Coke producers should add
sufficient coke to their tonnage shipments to make up for the water
included, as shown by their own determinations.)
Volatile Matter. — For every 0.50 or fraction thereof, above the i.oo
allowed, deduct . . cents from the price. Over 2.50 rejects the shipment
at the option of the purchaser.
Fixed Carbon. — For every i.oo or fraction thereof, above 85.50 add,
and for every i.oo or fraction thereof below 85.50, deduct . . cents.
Below 78.50 rejects the shipment at the option of the purchaser.
Ash. — For every 0.50 or fraction thereof below 12.00, add, and for
every 0.50 or fraction thereof above 12.00 deduct . . cents from the price.
Above 15.00 rejects the shipment at the option of the purchaser.
Sulphur. — For every o.io or fraction thereof below i.io add, and for
ever>' o.io or fraction thereof above, deduct . . cents from the price.
Above 1.30 rejects the shipment at the option of the purchaser.
Fluxes 429
Shatter Test
On arrival of the shipment the coke shall be subjected to a shatter
.test, as described below. The percentage of fine coke thus determined,
above 5 per cent of the coke, shall be deducted from the amount of coke
to be paid for (after allowing for the water) , and paid at fine coke prices
previously agreed upon. Above 25 per cent fine coke rejects the ship-
ment at the option of the purchaser. Fine coke shall be coke that passes
through a wire screen with square holes 2 inches in the clear.
The apparatus for making the shatter test should be a box capable
of holding at least 100 pounds coke, supported with the bottom 6 feet
above a cast-iron plate. The doors on the bottom of the box shall be
so hinged and latched that they will swing freely away when opened and
will not impede the fall of the coke. Boards shall be put around the
cast iron plate so that no coke may be lost.
A sample of approximately 50 pounds is taken at random from the
car, using a iH inch tine fork, and placed in the box without attempt to
arrange it therein. The entire material shall be dropped four times upon
the cast iron plate, the small material and the dust being returned with
the large coke each time.
After the fourth drop the material is screened as above given, the
screen to be in horizontal position, shaken once only, and no attempt
made to put the small pieces through specially. The coke remaining
shall be weighed and the percentage of the fine coke determined.
If the sum of the weights indicates a loss of over i per cent the test shall
be rejected and a new one made.
Rejection by reason of failure to pass the shatter test shall not take
place until at least two check tests have been made.
Fluxes
The object of a flux is to render fusible the ash from the fuel, sand
and rust from the iron, and dirt of any sort, found in the cupola, into
slag and to put it in condition for easy removal. ■
Slag always forms to a greater or less extent where iron is melted,
but unless a flux is present, it will not be sufficient in volume to give
clean iron. Limestone and fluor spar are the most common fluxes in
use. There are many compounds furnished for the purpose, but a
limestone containing 90 per cent or more carbonate of lime, or oyster
shells, furnish as good fluxing material as can be procured.
The following is copied from a paper by Mr. N. W. Shed, presented
to the Cleveland meeting of the American Foundrymen's Association
at June, 1906.
430 Foundry Fuels
"The value of fluxes in llie cujxila is not generally appreciated by
foundrymen. Hundreds of cupolas are not slagged at all and the
cinder dumps show an immense amount of iron actually wasted. Not
only is iron lost by the large amount combined with the cinders, but the
more or less variable cinder encloses small masses and shots of iron
which cannot be se{)aralcd. It is a fact that the cinder dumps of many
foundries contain more iron than many workable deposits of iron ore,
and if these accumulations could be obtained by the German blast fur-
naces they would be quickly utilized.
Another value of flu.xcs is their cleansing action on the cujxila.
A well slagged cupola has no hanging masses of iron and cinder which
require laborious chipping out. The time and labor saved in conse-
quence is an item that is well worth considering. In the running of
heavy tonnage from a single cupola, fluxes are indispensable. It would
be well nigh impossible to run large heats in the same cupolas without
using a good flux.
The value of fluxes being generally admitted, the question arises,
what flux is best to use and how much?
There are two available fluxes for the cupola. These are limestone
and fluor spar.
Fluor spar is much advertised as a flux and the promoters claim that
it gives marvellous properties to the iron. The glowing advertisements
have evidently deceived the U. S. Geological Survey, for the reports
of the Survey speak of its great use and value in foundr>' practice."
The practical test of fluor spar, made by the writer showed it to be
an inferior flux. It did not remove sulphur and the properties of the
iron were not improved in the least by its use. There is no doubt of
the value of fluor spar in certain branches of metallurgy, but the writer
has failed to find a single supporter of its value in the foundry.
Limestone is far cheaper than fluor spar and far better as a flux.
It makes little difference what form the limestone has so long as it is
pure. It ma)' be marble, soft limestone, hard limestone, oyster shells,
or mussel shells, but it must be good. A limestone containing over
3 per cent silica is poor stuff, and one containing any considerable
amount of clay should be rejected. There should be at least 51 per cent
of lime present. The sulphur should be below i to 2 per cent. The
phosphorus is unimportant. .\ magncsian limestone would do as well
as an ordinarj' limestone for the cupola.
The amount of limestone to be used is variable, depending:
First: on the amount of silica in the coke ash.
Second: on the amount of silica or sand adhering to the pig or scrap.
Third: on the amount of silica to be carried by the slag.
Fluxes 431
The amount of limestone required to flux the coke ash can be
figured according to the ordinary method of calculating blast furnace
charges.
The amount of sand on the pig and scrap is so variable that it is
difficult to know just the additional amount of limestone to add.
The most practical and easily fusible slag has been found to be a
monosilicate, which means having equal amounts of silica and alkaline
bases. Having these variables in mind, we find it a good rule to figure
the limestone on the weight of the coke, using 25 per cent limestone.
For example, if the charge of coke on the bed is 4000 pounds, we
use looc pounds of limestone. If the next charge of coke is 1000 pounds,
we would use 250 pounds of limestone. This amount of limestone will
flux any ordinary coke ash with the average amount of sand on pig
and scrap. If we know the amoimt of sand on the pig to be excessive
we figure 30 per cent limestone on the weight of the coke.
With a low coke ash, machine pig and clean scrap, the limestone
may be reduced to 20 per cent and make a good cinder. Many foundr>'-
men are afraid to use limestone, fearing some injury to the iron. This
is a superstition for lime has no effect on the iron.
There is usually a slight reduction in the amount of sulphur, but
owing to the great amount of iron present, the iron absorbs a large
amount of sulphur from the coke.
If more than 30 per cent is required to make a good cinder and clear
the cupola it is evident that either the coke is very high in ash, or else
the limestone is high in silica. In the latter case a large amount of
lime is used in fluxing its own silica.
On account of the frequent variations in the stock, it is a good plan
to have coke, limestone and cinder analyzed occasionally.
The cinder usually tells about the condition of the furnace. A light
brown indicates a small amount of iron and the iron unoxidized. A
black cinder indicates a large amount of iron and some oxidation. A
shiny metallic lustre shows an excess of oxide of iron due to over-blow-
ing or lack of coke. Practically all the lime cinders from a cupola are
glossy in appearance, while the cinders with no lime are usually dull
and earthy. Occasionally a cinder is found full of bubbles, the color
is usually black and shots of iron are found through the frothy slag.
This is called foaming cinder, and is made when the last few charges
are at the bottom of the cupola. This cinder often rises to the charging
door and flows out over the floor. The iron cast at this time is hard
and is low in manganese, silica and carbon.
With foaming slag a dense smoke of reddish brown color pours out
of the stack.
432
Foundry lucls
Analysis of the foaming slag shows the iron to be in an oxidized
condition and in large amount. Sometimes the iron will run 30 per
cent in frothy cinder, sometimes t)nly 12 per rent. The oxidizetl cinder
and the red smoke show that iron is being rapidly burned in the cupola,
and the action going on is very much like the action in a Bessemer con-
verter when it is tilted back a little and IjJown to gain heat by burning
the iron. The cinder is oxidized and the red smoke is produced in the
same way. In both cases the iron is burnt to oxide, which is cjuickly
taken up by the slag. The oxide in the slag acts upon the carlxjn in
the iron forming a large amount of carbonic oxide, which rises through
the cinder blowing it to a frothy condition.
There are two ways of avoiding this troublesome condition. If
possible, reduce the blast. If the blast cannot be reduced, add more
coke. The presence of a good body of coke will stop the burning of the
iron, and frothing does not take place. In some cases the loss of sili-
con is very serious, and to insure good castings it is necessary to add
crushed silicon metal and ferro-manganese to the stream of iron as it
runs from the spout.
Analysis of cupola slags where no flux is used show from 14 to 28 per
cent ferrous oxide. These slags contain 2 to 4 per cent of shot iron
mingled with the cinder. This proves that some of the iron must be
lost in order to flux the coke ash and sand. If we use limestone as a
flux the amount of iron in the cinder is rarely over 3 per cent, showing
that the lime fluxes the ash and sand leaxing the iron for the ladle.
And the question is simplj' whether we will use iron as a flux at ?i8.oo
per ton or limestone at $1.50 per ton.
Another point in favor of the limestone is the clean cupola men-
tioned in the first part of this paper.
Following will be found an analysis of cupola cinder using lime."
Comparison of Analyses of Slags, Made With and Without
Lime
Constituents
Using
lime
34.60
4.10
11.02
4S.20
1.40
.20
99 52
Without
lime
CaO
6.60
21.76
ti 80
58.44 1
FeO
AKOf
SiO,
MnO ;.
1.30 '
S
.10
100 00
Total
Slags 433
The following analyses are extracted from " The Foundry," Dec.
1909.
. Analysis of Slag from a Cupola Melting Car Wheel Iron, in the South
Per cent Per cent
Silica 48 . 77 Oxide of iron 13.18
Aluminum 10.90 Metallic iron 9.23
Lime 13-79 Manganese 4 . 84
Magnesia 6.05 Sulphur 0.81
Analysis of Slag from a Cupola Melting Gray Iron, No Fluor spar
Being Used
Per cent Per cent
Silica 42 . 84 Magnesia 13 • 28
Alumina Manganese 2 . 34
Oxide of iron 21 .32 Manganese oxide. ... 3.01
Lime 21.16
Analysis of Slagfrofn a Cupola Melting Gray Iron, Fluor spar
Being Used
Per cent Per cent
Silica 39 5° Magnesia 1 1 . 05
Alumina Manganese 2 . 24
Oxide of iron 22 .82 Manganese oxide. ... 2 .89
Lime 24.50
Analysis of Slagfrofn a Cupola Melting Malleable Iron
Per cent Per cent
Silica 41 • 72 Magnesia 15 .06
Oxide of iron Manganese 3 • 20
Alumina 22.24 Metallic iron 5.82
Lime 17-84 Manganese oxide ... . 4.12
Analysis of Slag from a Cupola Melting Car Wheel Iron, in the North
Per cent Per cent
Silica 44.00 Magnesia 7.27
Oxide of iron 13- 16 Metallic iron 9.21
Alumina 9 . 76 Manganese 5 . 70
Lime 1 5 - 99 Sulphur 0.78
Cupola Slag from a Western Foundry
Per cent Per cent
Silica 37- 16 Oxide of iron 13-73
Alumina 9.16 Metallic iron 9.61
Lime 8.98 Manganese oxide. ... 2 . 77
Magnesia 8.44 Sulphur 0.36
434
Foundry I-'ucls
Sufl'icient flux must be usc'l to obUiin a fluid slag to carry off the
silica from the iron and ashes and to reduce the oxidation as much as
possible.
With low blast pressure the slag must be thin, to run off readily.
When slag wool is frcelj' produced, the indication is that the slagging
is satisfactory.
A good slag contains approximately 40 per cent of silica and from 28
to 30 per cent lime. If the slag is thin, the metallic iron will fall through
it readily and an increase of lime tends to decrease the oxide of iron.
Rusty scrap produces a dark-colored slag caused by the oxide of
iron.
A large body of slag is favorable to desulphurization, as the amount
of sulphur which can be taken up by the slag is limited. At high tem{H;r-
aturcs sulphur tends to combine with the slag and under these conditions
it has not its greatest affinity for iron.
Fire Brick and Fire Clay
A good brick has a light yellow color, a coarse and open structure,
uniform throughout. It should be burned to the limit of contractility.
The clay from which it is made should contain as little iron, lime, potash
and soda as possible.
Analyses of Fire Cl.ws Used for M.^vking Fire Brick
Clay loses its plasticity at a temperature above 100° C, and it cannot again
be restored.
Localities
a
0
.e
V a
0
E
£
7.72
.47
I. so
.13
.20
.40
.10
2.0s
• SS
.40
.37
417
.24
.24
.95
4.43
.36
• 29
.99
Stourbridge. Eng
Mt. Savage, Md
Mineral Point. Ohio. . . .
Port Washington, Ohio.
Springfield, Ohio
Springfield, Pa
Springfield, Pa
17 34
12.74
11.70
534
5.45
45-25
50.45
49.20
59 95
70.70
55.62
56.12
28.77
35.90
27.80
33 85
21.70
38.5s
37.48
Pure silicate of alumina mclls at 1830° C.
Fire bricks should stand continuous exposure to high temperatures
of the furnace without decomposition or softening; should stand up
under considerable pressure without distortion or fracture; should be
unaffected by sudden and considerable variations of temperature; should
not be affected by contact with heated fuel.
Fire Sand
435
Fire brick should be regular in shape and uniform in character. The
size of the ordinary straight fire brick is 9 by 4I/2 by 21/2 inches, and the
weight is 7 pounds.
Cupola brick are usually 4 inches thick and 6 inches wide radially.
Slabs and blocks are made in sizes up to 12 by 48 by 6 inches.
Silica Brick
Silica brick are used for resisting very high temperatures. They are
composed mostly of silica in combination with alkaline matter.
They are somewhat fragile and need careful handling.
Analysis of Silica Brick
Silica
Alumina
Ferric
oxide
Lime
Magnesia
Potash
97.5
90.0
14
30
• 55
.80
.15
.20
.10
.10
.6
Canister
Canister is made from an argillaceous sandstone, is a close-grained
dark-colored rock containing no mica. There is present sufficient clay
to cause the particles to become adherent under ramming, after the rock
has been ground. The rock is ground to a coarse powder and some-
times if the binding properties are insufficient a little milk of lime is
added during the grinding process. The composition of ganister will
fall in the limits as given below.
Constituents
Per cent
From
To
87.00
4.00
95.00
5. 00
I 50
.75
1. 00
.25
Alkalies
Fire Sand
An exceedingly refractory sand containing sometimes as much as
97 per cent silica. It is used in the setting of silica brick and in making
the hearths of furnaces.
Pure silica melts at 1830° C.
436 Foundry I ucls
MagttcsiU
Magncsite contains a small percentage of lime and ferrous silioites
with seqicntinc. The ferrous silicates are separated out; thereupon
calcining, magnesia is obtained. The calcined material is then mixed
with from 15 to 30 per cent of the raw material, and from 10 to 15 per
cent water, then moulded into bricks, dried and burned in the ordinary
manner.
Bauxite
This is a hydrated aluminous ferric o.xidc, containing usually about
60 per cent of alumina, i to 3 per cent of silica, 20 per cent ferrous oxide
and from 15 to 20 per cent water. It is very refractory and, notwith-
standing the large amount of ferrous oxide contained, is practically
infusible.
Calcined bauxite is mixed with from 6 to 8 per cent of clay, or other
binding material and plumbago, then molded into bricks.
WTien heated the plumbago reduces the iron of the bauxite, producing
a most refractory substance.
Such bricks are far more durable than the best fire bricks. They resist
the action of the basic slags, as well as that of intense heat.
They become extremely hard after exposure to continued heat.
CHAPTER XIX
THE CUPOLA
The cupola is used in ordinary foundry practice in preference to the
air furnace, not only on account of its simplicity, but because it melts
more rapidly and economically. There are many forms manufactured.
All of them are good, but it is doubtful if any furnishes better results
than have been obtained from the ordinary old-fashioned cupola so
commonly in use, such as is shown in the sketch below.
For the advantages of the various styles offered for sale, the reader is
referred to the manufacturers' catalogues.
The cupola is essentially a vertical hollow cylinder, lined with refrac-
tory material, having the top open and the bottom closed, with pro-
vision for admission of the charges of fuel and iron part way up on the
side, also for admission of air below the charges and for drawing off
the melted metal at the bottom.
The cupola is divided into five zones.
First: The Crucible, extending from sand bottom to the tuyeres.
Second: The Tuyere Zone, extending from the crucible to melting
zone.
Third: The Melting Zone, reaching from the tuyere zone to a point
about 20 inches above the tuyeres.
Fourth: The Charging Zone, extending from melting zone to charging
door.
Fifth: Stack, from charging door to top of furnace.
The Lining
The lining is usually made of two thicknesses of arch brick placed
on end with the flat sides in radial planes. Several standard rectangular
brick are placed in each ring or course to facilitate the removal of the
rings when necessary. Angle iron rings are riveted to the shell at
intervals of about six feet, to support the upper sections, when a lower
one is removed for repairs.
The outer lining is kept about 34 inch away from the shell to pro-
vide for expansion, and the interval is filled in loosely with sand and
broken brick.
437
4i8
The Cupola
The distance from the sand bottom to the charging door should be
about 3!v to 4 times the inside diameter of the lining. For cupolas
""TT^TT^^^^T^^^^^^^^^^^^^^!^
Fig. 123.
under 48 inches, one door is sutTicient; for larger sizes two are more
convenient. The doors may be hung on hinges or shde on a circular
track above the openings. It is not necessary that they should be lined.
Tuyeres
439
At the level of the charging door the lining should be covered with a
cast-iron ring to protect it during the charging.
The bricks are laid with very close joints in mortar composed of
fire clay and sand. The interior lining is daubed with a mixture of one-
half fire clay and three-fourths sharp sand for a thickness of three-
fourths inch. Any joints are well filled. A handful of salt to a pail of
daubing will cause the interior of the shell to be glazed over and will
reduce the amount of chipping required. Washing the daubing with
strong brine and iire clay serves the same purpose.
Tuyeres
The tuyeres may be circular or rectangular in section with the bottoms
inclining slightly toward the interior of the shell so that the drippings
may not run into the wind box. Castings for tuyeres should not be
over ^8 inch thick.
The area of the tuyeres is made from lo to 25 per cent that of the
inside lining at the tuyeres; 20 per cent gives good results. As a matter
of fact the tuyeres cannot be made too large. A continuous tuyere
having an opening about 2 inches in height and extending all around the
lining is frequently used.
An excellent plan is to have an air chamber
all around the outer lining and inside of the
shell in the vicinity of the tuyeres; at the
level of the bottom of the tuyeres place a
cast-iron ring, in sections, on top of the
double lining. On this, at intervals of from
7 to 10 inches, so as to divide the circum-
ference of the interior of the lining into equal
parts, place hollow iron blocks 2 inches wide,
3 inches high and 7 inches long. On top of the
blocks place another segmental ring, which
should be kept 3 or more inches away from the interior of the shell.
Upon this ring the upper courses of the lining are built. This forms
a nearly continuous tuyere, broken only by the iron blocks.
This construction involves a contraction of the lining at the tuyeres
of about 8 inches. The bottom of the tuyeres should be from 10 to
20 inches above the sand bottom, depending upon the quantity of
melted iron to be collected before tapping. \\^here the iron is allowed
to run continuously from the spout, as in stove and other foundries
doing light work, the tuyeres may be even lower than 10 inches.
Frequently an additional row of tuyeres, having about one-eighth of the
main row in area, is placed just below the melting zone. These upper
Fig. 124.
440 riu- Cu[M)la
tuyeres should be arranRcd so ih.il the admission of air through them
ma,\' be regulated. The object is to supply the necessary air to convert
\vhatc\er carbonic oxide is formed in the tuyere zone into carlwnic acid
at the melting zone. The heat de\eloped at these upper tuyeres is such
that the lining near them is often badly cut, therefore, care must be
exercised as to the admission of air at this point.
A row of adjustaljle tuyeres about lo inches above the melting zone
is most effective in producing the combustion within the charges of
carbonic o.xide, forced above that zone, effecting thereby not only a
saving of fuel, but the suppression of flame at the charging doors. The
admission of air above the melting zone must be carefully regulated so
that only enough will enter to burn the carbonic oxide.
The "Castings" for September, iyo8, illustrates a cupola designed
by Mr. J. C. Knoeppel, which presents an admirable arrangement of
tuyeres and provides for the object above outlined.
Two or more of the lower tuyeres, should have slight depressions
in the bottoms, to permit the slag or iron, should either reach that
level, to run out upon sheet lead plates placed in the wind box in
the line of these depressions. By the melting of these plates, and
the discharge through the resulting holes, warning is given to the
cupola tender, and the accumulation of slag or iron in the wind box
avoided.
Unless the blast is much higher than good management permits, it
will not penetrate the fuel in the cupola for more than 30 inches radially.
Therefore, where the inside diameter of the cupola is over 6c inches,
it should be contracted at the tuyeres to 60 inches or less diameter;
or in place of this a center blast may be used. Large cupolas are fre-
quently made oval in section with the same object in view.
In the wind box directly opposite each tuyere there should be a small
door 5 inches in diameter, fastened with a thumb screw, for access to
the tuyeres, to remove any stoppages in front of them; each door should
be provided with a peek hole 1'.. inches in diameter covered with mica.
The Breast
The breast is made by taking a mixture of one-half fire clay and one-
half molding sand, thoroughly mixed and just moist enough to be
kneaded. A quantity of this is placed around a bar lU inches in diam-
eter and made into cylindrical shape, 4 or 5 inches in diameter and about
6 inches long. This is placed in the opening for the breast, and the bar,
while held in a nearly horizontal position, forced down until its bottom
is on a line with the sand bottom, and ^i inch above the upper side of
Sand Bottom 441
lining to trough. The inner end of the clay cylinder should be flush
with the inside of the cupola lining.
Ram hard around this cylinder with molding sand and fill opening
for breast completely. Care must be taken that this clay cylinder is
well secured in place. Remove the forming bar and enlarge the hole
toward inside of cupola, leaving only about 3 inches in length of the
original diameter from the front.
The slag hole is made up in same way, but should be only one and a
half inches long. A core about 2H inches in diameter may be inserted
for the slag hole, and this dug out, when tapping for slag, until opening
is sufficiently large, say about i inch diameter.
It sometimes happens that the breast gives way during the heat.
In such an event, the blast is shut off and the cupola drained of iron and
slag. The defective part of the breast is removed, and replaced with
stopping clay, which is hammered with the side of a bar, well against
the surrounding portion of the breast. The remaining hole is then filled
with clay, carefully packed so as not to be driven to the interior of the
cupola. Through this clay a tap hole is made by gently inserting the
tapping bar and enlarging the hole after the ball of clay has been pene-
trated. In from fifteen to twenty minutes the clay will have been
baked hard. The blast can then be turned on and melting resumed.
This operation must be conducted with great care, as the operator is
in danger of being severely burned.
Swab the lining from the bottom to 2 feet above the tuyeres with
clay wash and salt, and black wash the tapping hole formed as above
described.
Sand Bottom
The sand bottom is made from gangway sand passed through a No. 4
riddle. This bottom should be about 8 inches thick. It must be well
rammed, especially next to the lining, where it should join with a liberal
fillet. It must not be too wet. Care must be taken not to ram the
bottom so hard that the iron will not lie on it quietly. The bottom
should slope in all directions towards the tapping hole, the slope being
one inch in four feet, and it should reach the tapping hole exactly on a
level with its lower surface.
Black wash the bottom, build a light wood fire and dry out the lining
thoroughly. The bottom doors should have a dozen or more %-inch
holes drilled through them to allow any moisture in the bottom to
escape. The doors are held in place by an iron post under the center,
which can readily be knocked out to drop the bottom. The breast
should be made up before the bottom.
443 Till' ("uiKila
Zones of Cupola
The crucible zone extends from the s;in(l lx»Uom to the tuyeres.
The object of this zone is to hold the melted iron and slag. If the tap
hole is kept open continuously, this zone may not be over 4 to 6 inches
in depth from sand bottom to bottom of tuyeres. If it is to hold a
large quantity of melted iron, the tuyeres must be correspondingly
high. Metal can be melted at a higher temperature with low tuyeres,
(collecting it in a ladlcj, than by holding it in the cupola.
Tuyere Zone
This is where the blast enters in contact with the fuel. Here com-
bustion begins. This zone is confined to the area of the tuyeres. The
combined area of the tuyeres should be about one-fifth that of a section of
the cupola at this point, and should also largely exceed that of the outlet
of the blower. It is important to keep the tuyeres as low as the condi-
tions of the foundry, as to amount of melted iron to be collected at one
tap, will permit. With low tuyeres the iron is hotter, there is less oxida-
tion and the fuel required on the bed is less.
Melting Zone
The melting zone is the space immediately above the tuyeres. It
extends upward from 20 to 30 inches, depending upon the pressure and
volume of the blast, increasing in height with increased pressure. No
iron is melted above or below it. The melting occurs through the upper
4 to 6 inches of that zone.
Charging Zone
This zone is that part containing the charges of iron and coke, and
extends from the melting zone to charging door.
The stack is the continuation of the cupola from charging door through
the roof. Contracting the stack above the charging door has no influ-
ence upon the elTicicncy of the cupola.
The spouts should be lined with fire brick. Above the fire brick
bottom at center of trough, there should be iM inches of moulding
sand. From the center the sand should slope rapidly each way to
sides. The sand lining of trough at center should be ?4 inch below
the tap hole. After lining, trough should be black washed and dried.
Stopping material is made of one-half fire clay and one-half moulding
sand.
It is the common practice to leave the top hole open until iron begins
Chemical Reactions in Cupola 443
to run freely, in order to prevent freezing at the hole. This causes
the oxidizing of considerable metal, and is unnecessary. The following
method may be pursued. Just before the blast goes on, close up the
inner end of the tap hole with a ball of greasy waste, then ram the
remainder of the hole full of moulding sand. This is easily removed
with the tapping bar, and does away with all the annoyance of escaping
blast and sparks.
Chemical Reactions in the Ordinary Cupola with
Single Row of Tuyeres
When the air blast comes in contact with the burning coke, its oxygen
unites with the carbon of the coke to form carbonic acid (CO2), as the
result of complete combustion. As the temperature above the tuyeres
increases to that necessary for melting iron, part of the CO2 seizes upon
the incandescent coke, takes up another equivalent of carbon and is
converted into carbonic oxide (CO). If the supply of air is in excess
of that required, the CO, being combustible gas, takes up another
equivalent of oxygen and is burned to CO2.
Again some of the CO2, parting with an equivalent of oxygen to the
iron for such oxidation as occurs, or by the acquisition of another equiva-
lent of carbon from the coke; or by both, is reconverted into CO. These
reactions take place at or near the melting zone.
After passing that zone, no more air is supplied, and the products of
combustion, consisting of CO and CO2 pass up the stack without further
change until reaching the charging door. Here air is admitted, the
CO is supplied with oxygen and is burned to CO2.
If the air supplied at the tuyeres is insufficient for complete combus-
tion, the evolution of CO is increased and the efi5ciency of the furnace
reduced. On the other hand, an excessive supply of air is objectionable,
as a reducing flame (that from CO) is desirable to prevent oxidation
of the metal.
For the complete combustion of one pound of carbon, there is required
12 pounds, or about 150 cubic feet of air, developing 14,500 B.t.u.; but
the combustion of one pound of carbon to CO requires only one-half the
air, and the resulting heat is 4500 B.t.u.; hence for whatever portion of
the fuel is burned to CO, there is a loss of over two-thirds its heat-
producing value.
For the purpose of saving this waste heat, an upper row of tuyeres,
just below the melting zone, is employed; and to utilize the heat which
escapes above the melting zone, tuyeres have bee;n introduced with
good results, at from 5 to 10 inches above that zone. By the use of
444
'Jhc CujKilu
ihu latter tuyeres the heat developed is al>sorbed by the charRCs in the
stack, and the flames at charging dcK)r are suppressed. Where such
tuyeres arc used, they must be provided with means for easily regulating
the admission of air.
The following table taken from West's Moulders' Te.xt Hook gives
the quantity of air required for the combustion of one pound each of
coke and coal.
Combustibles,
I pound weight
I'.iii.i.L of oxy-
gen consumed
per pound of
combustible,
pounds
Quantity of air con-
sumed per pound
of combustible
Total heat of
combustion
of I pound of
Pounds
Cubic feet
at 62" F.
combustible,
units of heat
Coke, desiccated
2.51
2.46
10.9
10.7
143
141
13.5SO
14.133
By reason of the contact of the molten iron with the fuel, changes in
atmospheric conditions, the amount of air used, and other conditions,
the same mixture may produce different kinds of castings at different
times; and there may also be variations in the same heat.
Chemical Reactions in the Cupola
The complete combustion of one pound of carbon to COj requires:
2.66 pounds of oxygen
or 12.05 pounds of air
and develops 14,500 B.t.u.
The burning of one pound of carbon to CO requires:
1.33 pounds of oxygen
or 6.00 pounds of air
and develops 4500 B.t.u.
Therefore one pound of coke, having 86 per cent fixed carbon requires
for complete combustion
2.66 X 0.86 = 2.29 pounds o.xygen
or 12.00 X 0.86 = 10.32 pounds air
and develops 14,500 X 0.86 = 12,470 B.t.u.
The 10.32 pounds of air less 2.29 pounds oxygen leave 8.03 nitro-
gen.
Wind Box 445
Taking the specific heat of oxygen at 0.218, carbon at 0.217, nitrogen
at 0.244. The temperature resulting from the complete combustion of
one pound of coke to CO2 is
^^'^70 -47i8°F.
0.217 X 0.86 + 0.218 X 2.28 + 0.244 X 8.03
That resulting from the combustion of one pound of coke to CO is
3870 ^ O p
0.217 X 0.86 + 0.218 X 1. 15 + 0.244 X 4.015
Hence for every pound of coke burned to CO, instead of CO2, there is
a loss of 8600 B.t.u., and a reduction of the resulting temperature of
1983° F. Taking the specific heat of cast iron at the average of temper-
atures between 2120° and 2650° F. as 0.169, ^■nd the latent heat of fusion
as 88 B.t.u., and assuming the temperature of the escaping gases at
1330°, then the heat wasted is (i33o°-7o°) X (0.217 X 0.86 + 0.218
X 2.28 + 0.244 X 8.03) equals 3330 B.t.u.; and the heat available for
melting iron is 12,470 — 3330 = 9140 B.t.u. for each pound of coke
having 86 per cent fixed carbon.
For I pound of iron melted at 2650° F. (or 2580° F. above atmosphere)
the number of heat units required is 2580 X 0.17 = 439 to which must
be added the latent heat of fusion giving 439 + 88 = 527 B.t.u.
Therefore, = 17.34 pounds of iron, which should be melted by
one pound of coke, if all the carbon was converted into CO2 and the gases
escaped at 1330° F.; also neglecting the heat lost in the slag and by
radiation.
Wind Box
The area of cross section of the wind box should be three or four times
that of the combined area of the tuyeres, in order that there may be
sufficient air reservoir to permit a steady pressure. There should be
two or more doors in the box for ready access in cleaning out when
necessary; and also for admission of air when the wood fire is started.
As before stated, there should be small doors opposite each tuyere.
The blast pipe ought, if the situation will permit, to enter the box on
a tangent, and box should be continuous. If it is necessary to divide
it into two boxes, on account of the tapping or slag holes, there must,
then, of comse, be a blast pipe for each box and they should enter the
boxes vertically.
The bottom of the box should be provided with at least two small
openings opposite the alarm tuyeres, which are covered with sheet lead.
These should be so placed that slag or iron running through them will
be at once seen by the tapper.
146
The Cupola
The manufacturing of cuixjlas for the trade has become an important
industry, and although the designs of the various makers diflcr largely
in details, the essential features in all are the same.
Perhaps the names best known to the foundry industry are: CoUiau,
Calumet, Newtcn, Whiting.
All of these give good results. Tor special information reference
should be made to the manufacturers' catalogues.
The melting capacities based on 30,000 cubic feet of air per ton of
iron are given in the following table.
BuiLUKRs' Rating
Diameter
inside of
lining,
inches
1
Colliau
Calumet
Newten
24
30
36
42
48
54
60
66
72
78
84
Melting capacity,
tons per hour
I- i!i
3- 4
4- 6
6- 8
8-10
10-11
12-14
IS-16
17-20
25-27
I
2- 3
4- S
&-7
8-9
lo-il
12-14
13-17
18-20
21-24
24-27
iM- aH
3 - S
4 -6
8 -9
9 -II
11 -12
12 -14
14 -18
18 -30
20 -24
A wind gauge should be attached to the wind lx)x at a convenient place. The
charging platform should not be more than 24 inches below the bottom of charging
door for sizes up to the 48 inch; for the larger sizes not over 6 to 8 inches.
The Blast
The air for the blast is supplied Ijy centrifugal blowers of the Sturte-
vant type, or by Positive Pressure Blowers of the Root t^pe. Both are
cfi'icicnt, and it does not appear that either has any special advantage
not possessed by the other.
T'or successful melting a large volume of air at low pressure is required.
I'rom 8 to 10 ounces pressure will usually be found sulTicient; in no case
should it be allowed to exceed 14 ounces.
As a rule 30,000 cubic feet of air per ton of iron are allowed. This is
somewhat too small, especially if the air contains much moisture;
35,000 cubic feet per ton is better practice.
\\'ith blast at low pressure and with high temperature in the furnace,
iron may gain in carbon during the process of melting. The reverse
may occur, however, under contrary conditions. O.xidation increases
with the intensity of the blast.
The Blast
447
The castings produced by low blast pressure are softer and stronger,
the loss by oxidation is less, there is less slag, less expenditure of power
and less injiu-y to the lining of the cupola.
Coke requires less pressure and more volume of air, as well as greater
tuyere area than coal.
Low pressure, large volume, large tuyere area and good fluxing tend to
prevent choking at the tuyeres. However, too much air must be avoided
as it reduces the temperature of the furnace and may produce dull iron.
The main blast pipe should be as short, and the tuyeres as few as
possible. Its diameter should be greater than the outlet of the blower.
For each turn allow three feet in length of pipe. The minimum radius
of the turn should not be less than the diameter of the pipe. It should
be provided with a wind gate, and, where a pressure blower is used, an
escape valve, both under control of the melter. The wind gate should
be kept closed until after the blower is started to prevent gas from
collecting in the blast pipe. For the same reason, the blower should, if
possible, be located lower than the wind box.
At the commencement, the blast should be low, and gradually in-
creased to the maximum as the heat progresses, then dropped toward
its close.
The friction of air in pipes varies inversely as their diameters, directly
as the squares of the velocities, and as the lengths. The table below
shows the loss in pressure and the loss in horse power by friction of air
in pipes loo feet long; corresponding losses for other lengths can readily
be calculated therefrom.
Loss IN Pressure in Ounces and Horse Power in Friction
OF Air in Pipes ioo Feet Long
Diam-
eter of
cupola
inside of
lining,
inches
Tons of
iron
melted
per hour
Cubic
feet of
air per
minute
Velocity
of air
in feet
per
minute
Diam-
eter of
blast
pipe,
inches
Diam-
eter of
outlet of
blower
Loss of
pressure
in ounces
per square
inch
fiorse
power
lost In
friction
24
IS
87s
1600
10
8
.313
.099
30
3.0
1.750
2200
12
9
448
.311
36
4-5
2,600
2400
14
II
457
.320
42
6.0
3.300
2S0O
16
12
434
.40s
48
8.0
4,700
2600
18
14
417
.523
54
10. 0
5, 800
2700
20
IS
406
.653
60
12. S
7.300
2300
22
18
246
.48s
66
IS.O
8,750
2400
24
20
246
■ S94
72
18.0
10,500
2500
26
22
231
.582
78
22.0
12,800
2500
28
23
202
.507
84
25.0
14,560
2600
30
24
190
.498
Computed from catalogue of B. F. Sturtevant & Co., and from Foundry Data
Sheet No. 5-
.,48
The ('u[x)la
The following tables give the rapacities of centrifugal and pressure
Mowers. .Vs these are based on 36,000 cubic feet oi air [)cr ton of iron,
the selection of sizes somewhat larger than those given in the tables is
desirable, as the allowance of air is too small.
The Sturtevant Steel Pressure Bixiwer Appued to Cupolas
Diam-
Melting
No. of
Cubic
No. of
blower
eter of
inside of
cupola
lining
capacity
per hour
in
pounds
1.200
square
inches of
blast
feet of
air per
minute
Pressure
m ounces
of blast
Horse
power
required
I
32
4.0
324
4135
5
OS
3
36
1.900
5.7
S07
3756
6
10
3
30
2.880
8.0
768
3250
7
18
4
35
4,130
10.7
1 102
3100
8
30
S
40
6.178
14-3
1646
2900
19
5 5
6
46
8.900
18.7
3375
2820
12
9 7
7
53
12,500
24.3
3353
2600
14
16.0
8
60
16.560
32 0
4416
3370
14
22 0
9
72
23.800
43.0
6364
2100
16
35 0
10
84
33.300
60.0
8880
I8I5
16
48.0
The Sturtev/Vnt Steel Pressure Blo\\t:r Applied To Cupolas
(Power saved by reducing the speed and pressure of blast.)
Speed
Pressure,
Horse
Speed
Pressure.
Horse
ounces
power
ounces
power
3445
5
.8
3100
4
.6
3000
6
15
2750
5
I.I
2900
7
2-5
3700
6
20
3560
8
4.0
2390
7
3 3
3550
10
7.4
3360
8
5.3
3380
13
12.7
21S0
10
9 4
2100
12
16.7
1900
10
13.7
i960
14
28.4
1800
12
22 s
1700
14
39 6
1566
12
31.7
Kent, page 519.
Pressure and Rotary Blowers
449
Buffalo Steel Pressure Blowers Speeds and Capacities as
.Applied to Cupolas
Square
inches
in blast
No. of
blower
Diam-
eter
inside of
cupola,
inches
Pressure
in
ounces
Speed,
No. of
revs.
per min.
Melting
capacity,
pounds
per hour
Cubic
feet of
air
required
per min.
Horse
power
required
4
6
8
II
14
i8
26
46
68
4
S
6
7
8
9
lo
II
12
20
25
30
35
40
45
55
73
88
8
8
8
8
8
10
10
12
12
4793
391 1
3456
3092
2702
2617
2139
1639
1639
1,545
2,321
3,093
4,218
5,42s
7.818
11,295
21,978
32,395
412
619
825
1125
1444
2085
3012
5861
8626
l.o
1.2
2.05
3.1
3.9
7-1
10.2
23.9
36.2
Speed,
Melting
Cubic feet
Pressure in
no. of revs.
capacity in
of air re-
Horse power
ounces
per min.
pounds per
hour
quired per
minute
required
9
5095
1,647
438
1.3
10
4509
2,600
694
2.2
10
3974
3,671
926
3.1
10
3476
4,777
1274
4.25
10
3034
6,082
1622
5.52
12
2916
8,598
2293
9 36
12
2353
12,378
3301
12.0
14
1777
23,838
6357
30.3
14
1777
35,190
6384
43.7
Kent, page 950.
The Root Positive Rotary Blowers
Size
number
Cubic feet
per revo-
lution
Revolutions
per minute for
cupola melting
iron
Size of cupola,
inches inside
lining
Will melt iron
per hour, tons
Horse
power
required
2
3
4
5
6
7
5
8
13
23
42
65
275-325
200-300
185-275
170-250
150-200
137-175
24-30
30-36
36-42
42-50
50-60
72 or %5
2!'^-3
3-4^3
42/^-7
8-12
I2H-l6%
I7?^-22%
8
II ^^2
nH
27
40
Kent, page 526
45°
The Cupf)^
Diameter of Blast Pipes for Pressure Blowers for Cupolaa
li. ]•'. Sturlevant & Co.
The following tabic has been constructed on this basis, namely, allow-
ing a loss of pressure of one-half ounce in the process of transmission
tiirough any length of pipe of any si/c as a standard; the increased fric-
tion due to lengthening the pipe has been compensated for by an
enlargement of the pipe, sufficient to keep the Ijss still at ',i ounce.
TaE Blast
i;;-...w ;.... .
feet
Cubic
feet of
Lengths of blast pipe in
feet
Cubic
feet of
air
Lengths of blast pipe in
air
trans-
SO
100
150
200
300
trans-
SO
100
ISO
30O
JOO
mitted
mitted
per
per
minute
Diameter in inches
minute
Diameter in inches
360
sH
6H
m
7W
7^i
1.872
loH
i2!-i
I3U
nl^
IS
S15
6%
7^i
7?4
8^
m
2.679
I2'4
14
is! 6
16
i7!4
63s
6%
7?4
8W
9
9H
3.302
I3U
is'/i
i6'/i
i7'/i
18-^6
740
7'/4
8Mi
9
9'A
io'/4
3.848
li%
16!^
17^^
i8Ji
20^
Blower No. 2
Blower No. 7
504
6«
7H
7%
8!4
8;-i
2.592
12
I3?4
IS
iS^/i
17H
721
7M
8K4
9
9!-^
10! 1
3.708
13^/i
i5'/6
I7»
i8H
I9?4
889
7l^
9
9M
loH
II
4.572
I5I6
I7-H
i8Ti
I9'^6
21H
1036
SH
9^6
io?6
II
11%
S.238
16
18,4
20
21 H
23
Blower No. 3
Blower No. 8
720
1%
8M
9
9V^
loM
3.312
I3M
15H
16! i
I7^i
1876
1030
m
9H
10^
II
II?4
4.738
IS'/4
17H
19I*
20^^
21-^
1270
PV^
10%
II !i
11%
12^4
S.842
i656
igJ^i
20^4
22
23?6
1480
9H
II
12
12H
13W
6.808
17H
20M
22^6
22H
25H
Blower No. 4
Blower No. 9
1008
8V4
m
loVi
10^6
ii5i
4.320
14?4
17
i8->6
1954
21 W
1442
914
loH
iili.
I2'/2
13^6
6.180
17
19H
21 U
22 1 4
24%
1778
\oH
liji
1274
13^6
i45i
7.620
18?^
21 Vi
23 V«
24H
26Vi
2072
II
12^6
izV*
I4W
ISV4
8.880
I9!'2
22>6
24W
26
38W
1
Blower No. s !
Blower No. 10
1440
qV^
I07^
11T6
12^6
i3?i
5.760
I612
19
205fe
21^6
23M
2060
II
1256
I.^?4
I4'/6
15^4
8.240
l8Ti
2I?4
23^4
2S16
27H
2S40
ii?i
I3H
I4Ti
i.S^i
16^8
10.160
205i
23?4
25"i
27?i
29H
2960
I2?i
I4V4
IS?i
i656
18
11,840
22^
2SH
27 V4
29S^
3m
Kent, page 520.
Dimensions, Etc., of Cupolas
451
The quantities of air in the left-hand column of each division indicate
the capacity of the given blower when working under pressures of 4,
8, 12 and 16 ounces. Thus a No. 6 blower will force 2678 cubic feet of
air at 8 ounces pressure through 50 feet of i2;i-inch pipe with a loss of
H ounce pressure. If it is desired to force the air 300 feet without an
increased loss by friction, the pipe must be enlarged to 17H inches
diameter.
The table below gives the important dimensions, distribution of
charges and melting capacities of cupolas from 24 inches to 84 inches
diameter inside of lining. The table is based upon the consumption
of 35,000 cubic feet of air per ton of iron and represents the best aver-
age practice.
Higher fuel ratios are frequently realized and the foundrymen must
vary the fuel and air supply as the conditions indicate. It is unwise,
however, to strive for high fuel ratio at the risk of a dull heat. The
loss on castings from one melt may far outweigh the saving on coke,
as between the ratios of 10 to i and 9 to i, for many heats. Coke is
one of the cheapest articles about the foundry; while hot, clean iron is
an item of the highest importance.
In general the cupola should furnish 20 pounds of melted iron per
minute per square foot of area of the melting zone.
Dimensions, Etc., of Cupolas
Height
Diameter
of cupola
inside of
lining,
inches
Height
from bot-
tom-plate
to charg-
ing door,
feet
from
sand bot-
tom to
underside
of tu-
yeres,
inches
Area of
tuyeres,
sq. in.
Pounds
of coke
on bed,
]pounds
First
charge
of iron,
pounds
Suc-
ceeding
charges
of coke,
pounds
Suc-
ceeding
charges
of iron,
pounds
Pres-
sure of
blast,
ounces
24
9.0
8-10
90
225
320
40
320
5- 7
30
10. 0
8-10
142
370
s6o
62
560
6- 8
36
10.6
8-12
204
460
850
85
850
6- 8
42
10.5
10-12
277
530
1200
no
1200
6- 8
48
12.0
10-12
362
820
1500
140
iSoo
8-10
54
13.0
10-15
458
1 100
1900
180
1900
8-10
60
is-o
10-18
565
1400
2500
225
2500
10-12
66
16 0
10-18
684
1900
3000
275
3000
10-12
72
18.0
10-20
814
2400
4000
320
4000
12-14
78
19.0
10-20
955
3000
5000
400
5000
12-14
84
19.0
10-22
1 108
3600
6000
500
6000
14-16
45-2 The Cupola
Dimensions, Etc.. of Citolas. — {ConlinunD
Size of
Num-
Volume
UiametiT
of blast
Siicof
Root
.Num-
ber of
I^Iorse
Sturte-
vant
ber of
revolu-
Hone
power
Melting
capac-
of air per
pipe not
blower
revolu-
power
blower
tions
re-
ity per
minute,
cu. ft.
over 100
feet long,
inches
required,
no.
tions per
minute,
revs.
required
H.P.
re-
quired,
no.
per
minute.
revs.
quired,
H.P.
hour,
pounds
875
10
I
300
2
3
3S0O
2
3.000
1. 750
12
2
300
5
>
2900
SS
6.000
2.600
14
4
175
8
('i
2800
10
9.000
3.S00
16
4
230
12
7
2600
IS
I3.000
4.700
18
S
200
20
8
2300
33
16.000
S,8oo
20
SVi
190
25
8
2500
2S
30.000
7.300
22
6
180
33
9
2200
35
25.000
8.700
24
6],i
170
4S
10
1800
45
30.000
lo.soo
26
7
ISO
55
10
2000
SS
36.000
12.800
28
7Kj
ISO
70
2-8
2500
60
44.000
14.S00
30
7H
170
80
2-9
2200
70
S0.000
Charging and Melting
In preparing the cupwla for raclLing, a bed of shavings is spread evenly
over the bottom; on this a layer of kindling wood; then enough cord
wood cut in short lengths to come well abo\e the tuyeres. The doors
in the wind box or, two or more of those covering the tuyeres, should be
left open to admit air to the fire. The wood should be covered with coke
for a depth of from 12 to 15 inches. Where wood is scarce or expensive,
the coke may be lighted directly with a kerosene oil blow torch. To use
the torch place two strips of boards 3" X i" on edge from the tap
hole to center of cupola. Then place other strips of same size crosswise
of the bottom forming a shallow trough about 6 inches wide in the shape
of a T. Large pieces of coke are placed over the trough to form a
cover, and on top of this coke is spread uniformly for a depth of about
15 inches. The torch is then applied at the tap hole.
After the fire is lighted and the top of the coke bed becomes red,
enough coke is added to bring the top of the bed 20 inches abo\-c the
tuyeres when the wood has burned out.
The necessary amount of coke for bottom is determined by gauging
from the charging door. The proper depth of bed is a matter of great
importance. Too much is as bad as too little. With too much coke,
the melting will be slow and dull; with too little the iron after commence-
ment of heat becomes dull, the cupola is bunged up and the bottom
may have to be dropped.
The Charging Floor 453
There should be sufficient coke to locate the top of the melting zone
about 20 inches above the tuyeres, and the subsequent charges of coke
should be just enough to maintain this position.
With proper depth of bed, the molten iron will appear at the spout in
from 8 to 10 minutes after the commencement of the blast. The first
and subsequent charges of iron should be of the same weight, and these
should be small.
The amount of coke between each charge of the iron and the preceding
one should be 10 per cent of the iron. In many foundries the coke
between the charges is made less than this, but 10 per cent is good
practice. It is not the best policy to run the risk of making a poor heat
by cutting down the coke. The charges should be continued as indi-
cated until the cupola is filled to the charging door.
In charging care must be taken to distribute both iron and coke uni-
formly.
The pig iron (broken) should be charged first, beginning at the lining
and proceeding toward the center, pigs should be placed sidewise to the
lining. Next comes the scrap; if there are large pieces, they should be
placed in the center of the cupola with the pig surrounding them.
The iron must be kept well around the lining and care exercised to
avoid cavities. If the scrap is fine, it must not be charged so closely as
to impede the blast. After the iron comes the coke, which must be
evenly distributed throughout. After the second or third charge, hme-
stone, broken into pieces about iH cube, is added. From 25 to 40
pounds of limestone per ton of iron is used according to the character
of pig and scrap as to sand and rust, and to that of coke as to ash.
The top of the bed should not be permitted to drop more than 6 or
8 inches during the heat. This determines the weight of iron for each
charge as well as that of the coke, the latter having a depth of 6 or 8
inches. The weights of all the materials going into the cupola should be
kept separately. The melter should be furnished each day with a charging
schedule giving the composition and the weight of each charge.
The fire should be started about two hours before the blast is put on,
to allow the charges in the stack to become well heated. The openings
in the wind box are closed immediately after starting the blast.
The egg-shaped section at the melting zone, which the cupola gradually
assumes by use, should be maintained.
The Charging Floor
The charging floor should be large enough, if circumstances permit, to
accommodate all the materials for the heat. Each charge of pig iron
and scrap, after weighing, should be piled by itself and in the order in
454
The Cu[K;I;i
wliicli it is to be used. The proj)cr amount of coke for each charge is
placed in oins or baskets. In larger works where the material is brought
to the platform on charging cars, the
cars are arranged so as to reach the
cupola in pro[)cr order.
The cuts show two different meth-
ods of charging at large foundries.
.At one the charging is done by hand
and at the other by machine.
While the material is handled more
ra|)idly and at less expense by the
latter method, it is doubtful if the
saving effected compensates for irregular melting and lack of uniformity
in product, which is likely to result from unequal distribution of the
charges.
i IG. 125. — Charging Floor.
Fig. 126. — Cupola Charging Machine
in Normal Position.
Fig. 127. — Cuixila Charging Machine
in Charging Position.
Melting Losses
Melting losses in a well-managed cupola should not exceed 4 per cent
for the annual average. Instances are known where the losses for long
periods were not over 2 per cent. The following records are taken from
the report of the secretary' of the American Foundry men's .Association,
and cover the results from 41 cupolas. The percentage of castings
made and the returns are calculated from the quantities given and added
to each table.
Light Jobbing
Table I. — General Jobbing
455
Numbers
Usual tonnage
Time melting
Blast pressure
Fan or blower
Pig iron
Per cent southern
Fuel used, lbs
Scrap bought
Pig iron used
Scrap used
Castings made
Scrap made
Per cent melting lost
Per cent melt in returns. . . .
Per cent in good castings. . .
10
I hr. 15 m,
80Z.
Fan
Coke
None
Coke
Mach.
10,400
9, 600
16,49s
1. 352
10.7
66
82.4
3
I hr.
Fan
Coke
Coke
Med. mach
3200
3200
SS04
620
4-3
97
I hr. 15 m.
Fan
Coke
None
Coke
Mach.
2657
2886
3916
872
13.6
IS. 7
70.6
3
2 hrs.
80Z.
Blower
Coke
None
Coke
Stove
268s
388S
4057
1873
9-7
28.5
61.7
80Z.
Fan
Mach.
20,000
20,000
3S.20O
2,200
6.5
6.5
Average melting loss 7.6 per cent
Average of melt in returns 8.8 per cent
Average of melt in good castings 83 .0 per cent
Table II. — Light Jobblng
Numbers .
Usual tonnage
Time of melting
Blast pressure, oz
Fan or blower
Pig iron
Per cent southern
Fuel used
Scrap bought
Pig iron used, lbs
Scrap used, lbs
Castings made
Scrap made
Per cent melting loss
Per cent melt in returns . .
Per cent in good castings .
72
3 hrs. 30 m.
13
Blower
Coke
None
Coke
102,000
42,000
108,300
27,500
57
19.1
75.2
I hr. 30 m.
6.5
Fan
Coke
None
Coke & coal
Stove
4.S00
7,Soo
10,300
1,200
4.2
10
85.8
16 .
2 hrs. 30 m.
Fan
Coke
None
Coke
Lt. mach.
19,200
12,800
21,000
9,100
6
28.4
65.6
2.S
ihr.
Fan
Coke
None
Coke
Med. mach.
3200
1800
4000
800
4
16
80
Average melting loss 25 . s per cent
Average of melt in returns 20.8 per cent
Average of melt in good castings 73-6 per cent
45^
The ("iii)<)hi
Taui-i; III. - I.r'.MT Macuineky
Numbers.
Usual tonnage
Time of melting
Blast pressure, 02
Fan or blower
Pig iron
Per cent southern
Fuel used
Scrap bought
Pig iron used . lbs
Scrap iron used, lbs
Castings made
Scrap made
Per cent melting loss
Per cent melt in returns
Per cent melt in good castings.
I hr. 10 m.
Fan
Coke
Coke & coal
None
16,000
4,000
13.220
4.500
6.5?
22.6
66.1
2 hrs.
Fan
Coke & ch. coal
Coke
Med. mach.
6,000
6,000
10,000
900
9.2
7.5
83 3
Numbers.
3 S
I hr. 30 m.
7
Blower
Coke
None
Coke
Lt. mach.
3900
27SO
3738
2762
2 3
41 S
56.20
Usual tonnage I S
Time of melting I hr. 30 m.
Blast pressure, oz 1 5
Fan or blower Fan
Pig iron Coke
Per cent southern So
Fuel used Coke & coal
Scrap bought | Med. mach.
4500
4280
7640
800
3 9
91
87
Pig iron used, lbs
Scrap iron used, lbs
Castings made
Scrap made
Per cent melting loss
Per cent melt in returns
Per cent melt in good castings.
15
2 hr.
7
Blower
Coke
35
Coke
Lt. mach.
14,000
16,000
20,500
6,000
II. 6
20
68.3
40
6 hrs. 40 m.
Fan
Coke
50
Coke
Stove
56*00
24,000
60,000
16,000
5
2,000
75
There is an error in this record. The loss should be 11.3 if the statement as to
castings and scrap are correct.
Average melting loss 7-33 per cent
Average of melt in returns 19-55 per cent
Average of melt in good castings 73o per cent
Stove Plate
Table IV. — Heavy Machinery
457
Numbers.
Usual tonnage
Time of melt
Blast pressure, oz
Fan or blower
Pig iron
Per cent southern
Fuel used
Scrap bought
Pig iron used, lbs
Scrap used, lbs
Castings made
Scrap made
Per cent melting loss
Per cent melt in returns
Per cent melt in good castings
i6
13
2 hrs.
6
Blower
Coke
SO
Coke
Mach.
14,720
11,130
18,845
4,870
8.4
18.8
72.9
15
2 hrs.
10
Blower
Coke
70
Coke
H'vy mach.
20,000
10,000
21,300
7,200
5
24
71
21
4 hrs.
9
Blower
Coke & coal
17
Coke
Mach.
25,740
16,270
37.760
7,560
4
18
78
IS
2 hrs.
14
Blower
Coke
20
Coke
15.S00
ll.Soo
19,000
6,000
7-4
22.2
70.4
Average melting loss 5.8 per cent
Average of melt in returns 20.6 per cent
Average of melt in good castings 73.6 per cent
Table V. — Stove Plate
Numbers.
Usual tonnage
Time of melt
Blast pressure, oz
Fan or blower
Pig iron
Per cent southern
Fuel used
Scrap bought
Pig iron used, lbs
Scrap used, lbs
Castings made
Scrap made
Per cent melting loss
Per cent melt in returns
Per cent melt in good castings.
20
2 hrs. IS min.
14
Blower
Coke
100
Coke and coal
Stove
20,000
20,000
24,000
14,200
4.5
35. 5
60
15
I hr. 30 min.
II
Coke
SO
Coke
Stove
18,000
12,000
20,192
9,000
2.7
30
67.3
10
13
Blower
Coke
25
Coke and coal
11,863
7,906
11.750
7,624
38.5
59-4
Average melting loss 3.3 per cent
Average of melt in returns 34.3 per cent
Average of melt in good castings 62.3 per cent
458
The Cupola
Taiii.k VI. — Sanitary Ware
N'umbcrs.
36
L su;il tonnage
Time of heat
Blast pressure, oz
Fan or blower
Pig iron
Per cent southern
Fuel used , lbs
Scrap bought
Pig iron used, lbs
Scr.ip used, lbs
Castings made
Scrap made
Per cent melting loss
Per cent melt in returns
Per cent in melt good castings
2 hrs.
S
Fan
Coke
None
Coal and coke
Medium
11,800
12,200
17,228
6,048
3
25 4
71.7
W
3 hr. 15 m.
14
Blower
Coke
Coke
411, wx>
12,234
65
19.4
74
38
3 h. 15 m
14
Blower
Coke
60
Coke
None
56.000
20.000
51.61.:
18,38'.
24.1
67.9
16
2 h. 30 m.
SO
Fan
Coke
Coal and coke
Med. macb.
9.87s
22.625
- • .>r6
] 6
24 7
71.6
Numbers
-•-
JH
29
30
25
3 h. 45 m.
14
Blower
Coke
3 h. 45 m.
40
3 h. 45 m.
5
Fan
Coke
None
Coal and coke
Medium
35.560
47.210
59.400
21,960
1.7
26.5
71-7
23
3h.
Blower
Coke
Blower
Pig iron
Coke
Coke
None
31.470
17.960
35.956
11.270
4.1
22.9
73
Coke
Coke
None
33.000
19.850
37.250
11.300
8.1
21.3
70
29,000
17.SOO
33.38s
Scrap made
Per cent melting loss
Per cent melt in returns
Percent melt in good castings
ii.Soo
3 5
24 7
71.8
Average melting loss
Average of melt in returns .
Average of melt in good castings.
4.84 per cent
23.60 per cent
71 . 50 per cent
Railroad Castings
Table VII. — Agricultural
459
Numbers
Usual tonnage
Time of heat
Blast pressure, oz
Fan or blower
Pig iron
Per cent southern
Fuel used
Scrap bought
Pig iron used, lbs
Scrap used, lbs
Castings made
Scrap made
Per cent melting loss . . .
Per cent melt in returns
Per cent melt in good
castings
80 45
4 h. 20 m.|3 h. IS m.
15
Blower
Coke
50
Coke
Ag. No. I
80,000
80,000
108,800
42,700
5-3
26.7
67. S
Blower
Coke
Coke
Ag. No. I
45 ,000
45,000
61,200
24,300
5.2
27
67.7
41
3 h. 30 m.
13
Blower
Coke
so
Coke
Med. Mach.
45,700
35,800
62,960
15,600
3.6
19.2
77.2
9
2 hrs.
12
Blower
Coke
so
Coke & coal
Stove
7,071
10,674
11,845
5,200
4
29.3
67
95
I h. 20 m.
9
Blower
Coke
None
Coke & coal
Stove
7.500
11,600
7,450
10,650
53
55.7
39
Average loss in melt 4. 77 per cent
Average of melt in returns 26. 73 per cent
Average of melt in good castings 68 . 4 per cent
Table VIII. — Railroad Castings
Numbers.
38
Usual tonnage
Time of heat
Blast pressure, oz
Fan or blower
Pig iron
Per cent southern
Fuel used
Scrap bought
Pig iron used
Scrap used
Castings made
Scrap made
Per cent melting loss
Per cent of melt in returns ....
Per cent melt in good castings .
47
5 hrs. 20 m.
16
Blower
Coke
None
Coke
None
66,500
28,500
60,400
28,900
6.1
30.3
63. 5
32
6.5
3 hrs. 45 m.
2 hrs.
4
9
Fan
Ch. , coal and coke
Coke
60
None
Coke and coal
Coke
None
25,000
6,765
39,000
6,23s
54 ,000
10,000
7,500
2,38s
3.9
4.7
II. 7
18.3
84.3
76.9
Note. — No. 37 is an average of 27 heats. No. 38 is an average of 25 heats.
Average melting loss S . 64 per cent
Average of melt in returns 22 . 43 per cent
Average of melt in good castings 72 . 22 per cent
4^>o Tllc ClifM)!;!
Tahi.i; IX. — Floor Platks. Grate Bars, i.tc.
Numbers...
Usual tonnage
Time of heat
Blast pressure, oz
Fan or blower
Pig iron
Per cent southern
Fuel used
Scrap bought
Pig iron used, lbs
Scrap used , lbs
Castings made
Scrap made
Per cent melting loss
Per cent melt in returns
Per cent melt in good castings.
30
3 hrs. 40 m.
16
Blower
Coke
None
Coke
Med. mach.
20,000
40,000
47.400
8,200
7 3
13.7
79
3
ihr.
Pan
Coke
Coke and coal
Light mach.
None
6,000
5. 100
S2S
6.2
8.8
8S
Average melting loss
Average of melt in returns
Average of melt in good castings.
7 . 23 per cent
8.88 per cent
8s per cent
Table X. —
Car Wheels
41
200
7 hrs.
10
Blower
Wheel
2.1
Blast pressure, oz
Fan or blower
Per cent melt in returns
Per cent melt in good castings.
From the above tables, the following table showing the average results
for each class of work is compiled.
Table XI
Percentage
o.a
>>
ill
E
>>
>> b
> a
1
0.
a
>
0
Co
h
3
■1
<
"0
is"
8
5
Number of records.
Per cent melt in
4
83.9
8.2
77
4
73.6
20.8
S-S
6
73 01
19 SS
,33
4
73.6
20 6
5.8
3
62.3
34 3
3-3
8
71. S
23.6
4.84
s
68.S
26.7
4.77
3
72-3
22.43
S.24
2
79-S
13.2
7.2
1
Per cent melt in
0
Per cent melt lost .
Note. No. 12 was omitted in obtaining these averages. Evidently there was
something wrong about this heat as shown by the excessive returns.
Melting Ratio 461
The figures in the preceding table are to be taken as approximations.
The loss may be reduced in practice by careful management.
When the weight of the coke on the bed, and the weights of the iron
' and coke in each charge are known, to determine the necessary amount
of iron which must be melted to produce a desired melting ratio:
Let X = the total iron;
Y = the total coke;
A = weight of coke on bed;
B = weight of coke in each charge;
C = weight of iron in each charge;
D = the desired melting ratio.
(i) Then j? = ^, ^ ^ D *°^^^ ^°^^ ^^^
(3) and -p; = the number of charges.
The total coke is found in equation (4)
(4) F = (|-i)5+4.
From equations (2) and (4) X = -—^ :f—--^ . (5)
Having found the total amount of iron, the total coke and number of
charges are found from (2) and (3).
By applying these formulas to a 54-inch cupola as given in table on
pp. 451-2 the required weight of iron to be melted to produce a melting
ratio of 9 to I may be found.
Melting Ratio
Weight of coke on bed ^ = 1100 poimds
Weight of coke to each charge B = 180 pounds
Weight of iron to each charge C = 1900 pounds
Required melting ratio D = 9 to i pounds
From equation (5)
1900X9(1100-180)
1900 — 9 X 180 0,0,
Y == — '- = 6243 pounds.
9
And the number of charges
56,185
^-^ — ^ = 29.57.
1900 ^^'
Coke may be charged from dumps, as it lan be uniformly spread.
462 The Cuf)ola
The cupola should be kept full to the charging door until all the iron
is in. J.atcT the sweepings from the charging platform may be thrown
on. The platform should, if possible, be large enough to accommo<Jale
the materials for the entire melt. Kach charge of pig and scrap should
be weighed and piled by itself; the coke kept in convenient charging
buckets, and the broken limestone in a bin from which it may be charged
by measure, above the coke.
Appliances about Cupola
The conditions will indicate the necessity for elevator and charging
cars. In every foundry yard there should be a cinder mill and scrap
breaker. In many foundries the cinders arc frequently ground in the
tumbling barrel. It is purely a matter of convenience; but locating
the cinder mill in the yard promotes cleanliness, especially when broken
fire brick are ground.
The cinder mill is made up of cast-iron staves from 8 to 10 inches wide
and of convenient length, placed about polygonal heads; the latter
mounted on trunnions, and the whole rotated slowly by any suitable
means. The staves are so placed that there is not over an eighth of an
inch opening at the joints, in order that the shot iron may not escape.
^Magnetic and hydraulic separators are frequently used to recover the
shot, and they cflect large savings.
The scrap breaker is located conveniently to the cars, or placed
where heavy scrap is received. It consists of a derrick and ball with
hoisting apparatus. The height of the derrick should be from 30 to
40 feet and the ball should weigh 2500 to 3000 pounds, both depending
1 on the probable dimensions of the
largest scrap.
The sketch below shows a simple
and effective device for tripping the
ball.
Ladles
Hand ladies, and shank ladles
holding 200 pounds or less, are best
made of sheet steel, as they are
much lighter and are easily repaired.
These, as well as larger sizes, to be
handled by cranes, are furnished by
the foundr>- supply houses.
It is usually best to tap into a fore ladle. This is kept under the
spout, and has sufficient capacity to hold one entire charge. From it
2)
c
The Bod Stick 463
the smaller ladles are filled. By making large tappings, the various
grades of iron in the cupola become thoroughly mixed in the fore ladle.
The iron in the ladle is kept hot by covering the surface with charcoal
or slacked lime.
In English practice the Fore Hearth is largely used instead of the fore
ladle, but its use has not met with favor in the United States. An illus-
tration of this arrangement is shown on page 248 of McWilliams and
Longmuir's General Foundry Practice.
Lining of Ladles
The ladles are lined with a mixture of one-half fire clay and one-half
sharp sand. With small ladles the lining is from •% inch to 114 inches
thick on the bottom and gradually tapers to yi to % inch thick at the
top.
Large ladles have first a lining of fire brick, then the clay daubing.
After the linings are completed they must be thoroughly baked either
by placing the ladles in an oven or by building wood fires in them. It
is customary to reline the small ladles after each heat. The larger ones,
if completely drained of iron, may, by chipping out and patching, be
made to last over many heats. The skulls from ladles are rattled with
the cinders. Shanks for ladles holding 100 pounds and upwards are
commonly made with single and double ends. The better practice is
to make both ends double, the helper's end having a swivel joint. With
this type of shank the helper can use both hands in carrying and two
men can handle a 200-pound ladle easily. The iron bottoms of the
larger ladles should have 10 or i2-?i-inch holes through them to permit
the escape of moisture.
Tapping Bar
The tapping bar is usually made of i-inch gas pipe, having a long
tapered point (24 inches in length) welded to it at one end. Frequently
the tapper stands along one side of the spout, and opens the tap hole
with a single-handed bar. He carefully picks away the center of the
bod, imtil a hole is made through it, then enlarges the hole to % inch, or
an inch, according to the stream desired.
The Bod Stick
The bod stick is an iron bar about i inch in diameter, having at one
end a flat disc 2 k' inches in diameter. To this disc is attached the
clay bod, used in stopping up the tap hole. In stopping the stream
of iron, the bod, placed above the stream at the tap hole, is forced down-
464 riic Cupola
Table Showing Capacities of LAni.rs wirn Rottom Diaueteks
Depth
Diami-tir of 1
30
22
-'I
Vj
'-■
34
36
Ins.
2
4
6
8
10
12
14
16
18
20
22
24
26
28
30
32
34
36
38
40
42
44
46
157
318
483
652
825
1002
1 183
1368
1557
1749
1946
2149
191
334
58S
788
997
1210
1427
1648
1873
2102
2337
2576
2821
227
459
696
938
I185
1436
1693
1954
2221
2492
2769
3050
3337
3630
267
538
815
1096
1383
1676
1973
2276
2585
2900
3221
3548
3880
4218
4560
309
624
945
1272
1604
1942
2286
2606
2992
3353
3720
4093
4472
4807
5248
5645
356
717
1084
1457
1836
2221
2612
3009
3412
3821
4237
4660
5089
5525
5968
6417
6871
7329
403
812
1228
1651
2080
2516
3142
3408
3863
432s
4793
5268
5750
6238
6734
7237
7747
8261
8781
1.860
2,342
2,830
3.326
3.829
4J39
4.8SS
S.378
5.9"
6.451
6.998
7.552
8.114
9.6S2
9.258
9.840
10.428
510
1.026
I.S50
2.085
2.62s
3.172
3.726
4.288
4.856
5.432
6.016
6.608
7.208
7.816
8.432
9.054
9.694
10.332
10.978
11,630
12.288
48
For steel add 5%
SO
52
54
56
S8
60
62
64
66
68
wards into the hole squeezing off the stream. Many severe burns have
been caused by stopping directly against the stream.
The spout is sometimes made with a side opening to carr>- off slag
running on the stream of iron. This opening is made about the middle
of the spout, and the trough in that vicinit)' is somewhat increased in
width. About 2 inches below the side opening a fire brick is placed
across the trough, leaving room below it for the iron to pass, but
being low enough to skim off the slag, which runs out of the side at
the opening. A swinging spout is occasionally used. This is himg
on a pivot below the spout proper, and in a transverse direction-
Capacities of Ladles
46s
Varying from 20 to 54 Inches, Slope of Sides i^^ to i Foot
Diameter of ladle at bottom, inches
Depth
38
40
42
44
46
48
50
52
54
Ins.
2
568
630
694
762
832
906
984
1,064
1,146
4
1,144
1,268
1,396
1,600
1,672
1,820
1,978
2.138
2,302
6
1,728
1,914
2,106
2.310
2,522
2.774
2,982
3.222
3.469
8
2,330
2,568
2,824
3.096
3.380
3,678
3,996
4.316
4.829
10
2,930
3,330
3,552
3.892
4,248
4,622
5,019
5.420
6.063
12
3.538
3,900
4,288
4.696
5,124
S.576
6,052
6.334
7.308
14
4.154
4,578
5,032
S.510
6,012
6,540
7,09s
7.6S9
8.564
16
4.776
5,264
5,784
6.332
6,910
7,514
8,149
8,784
9.831
18
5,406
5,958
6,546
7.154
7,816
8,498
9.213
9,930
10,711
20
6,044
6,660
7.316
7,994
8,730
9,492
10,287
11,086
11.936
22
6,690
7,370
8,094
8.844
9.654
10,496
II. 371
12,253
13.212
24
7,344
8,088
8,880
9,702
10.588
11,510
12,465
13,422
14,479
26
8,006
8,816
9,676
10,570
11,532
12.533
13,569
14,623
15,757
28
8,676
9,552
10,480
11,446
12,486
13.566
14,683
15,826
17,046
30
9,354
10,296
11,294
12,334
13,450
I4.6c9
15,808
17,038
18,346
32
10.040
11,048
12,116
13,232
14.424
15.663
16.943
18,261
19,657
34
10.734
11,810
13.943
14,140
15.408
16,727
18,089
19,495
20,979
36
11,436
13,580
13.788
15,059
16,402
17,801
19.249
20,740
22,312
38
12,146
13,358
14,618
15,988
17.406
18,885
20,412
21,996
23,657
40
12.864
14,144
15.496
16,927
18,420
19.998
21.591
23,263
25,014
42
13.590
14,940
16,364
17,876
19.443
21,083
22,782
24,541
27,070
44
14,322
15,712
17,240
18,835
20,476
22,197
23.985
25,830
27,761
46
16,550
18,122
19,014
19,802
20,776
22,198
21.519
22,573
23,637
23,322
24,557
25,703
25.197
26,420
27.654
27.130
28,441
29,763
29,152
48
For steel
add 5%
30,555
SO
31.920
52
24,711
26,859
28,899
31,096
33.397
S4
28,032
30.155
32,441
34.336
S6
29,223
31.422
33,798
36,287
S8
30,256
32.690
35, 166
37,750
60
33.979
36,545
39,225
62
35.279
37,941
39.343
42,312
40,712
64
66
The foundry
42,211
43,729
68
1 1
46,011
While the stream is running it can be tipped so as to let the iron
run into a ladle at either side. In rapid melting this obviates stop-
ping up when ladles are changed.
Applying Metalloids in Ladle
Where metalloids are added to the iron, if the amount to be used is
sprinkled into the stream as it flows through the spout, a more intimate
mixture is obtained than results from placing the material in the ladle
and drawing the iron on to it.
466
The C'u|)olu
Cranes
The e<iuipmcnt of cranes as to size, style and motive power is indi-
oitcd entirely by the character and volume of production. Ample and
convenient lioistin^ facilities are absolutely essential. A mistake is
seldom made in pro\iding cranes of too great cajjacity.
Most of the modern foundries are fitted with electric traveling cranes,
which not only have access to the cupola, but sweep over the moulding
floors. In addition to the electric crane, post and wall cranes are
supplied for special requirements. There should be a small jib crane
attached to the cupola for handling the fore ladle.
The manufacture of cranes has become a specialty, and the reader is
referred to manufacturers' catalogues for special information.
Spill Bed
In many foundries the excess iron, and iron on the bench floor, is
frequently dumped into holes in the sand heaps or floors. This is a
slovenly practice and greatly injures the sand.
.\ very convenient and simple spill bed is sho\^^l in Fig. 129. This
is so made that the iron is collected in pieces weighing from 60 pounds to
80 pounds, of convenient size to be handled in charging.
A small bed of same character serves an excellent purpose when placed
near the snap floors.
Dumping Spill Bed
Mb^.JJ^#^.#A^Jj
'"'"VWW/>/->^W/?/////W//^/WW//.>/W^-^^/J''/^//^///^^y>///^///.
I
1
Fig. 129.
Gagger Mould
Gagger Mould
467
Fig. 130.
By a little care all the excess iron may be put through beds as above
and sent to the cupola in good shape for melting.
The usual practice is to allow the bottom to remain where it drops
until the next morning, simply wetting it thoroughly.
Below is shown a sketch of a large rake. If the bottom is dropped
on this and the mass pulled out from under the cupola (by means of a
Fig. 131.
chain passing through a snatch block to the crane) and then wetted
down, it will be found in much better shape for picking over in the
morning.
The pieces of unconsumed coke should be picked out and used in
core ovens, or as part of the last charge of coke, in the cupola. Little
savings of this kind, although small of themselves, amount to an impor-
tant item in the course of the year, particularly if the operations are
extensive.
CHArTKR XX
MOULDING SAND
MouLDiNr. sand contains from 75 to 85 i)er cent silica, with varying
proportions of alumina, magnesia, lime and iron.
The essential properties arc:
Cohesion, Refractoriness,
Permeability, Durability,
Porosity, Texture.
Cohesion or Bonding Power
Moulding sand must possess suflkient cohesion, not only to remain
in position after ramming, but to resist the pressure of the molten
metal, and its abraiding action while being poured.
Pure sand has no cohesive strength, but clay (double silicate of
alumina) has, and as moist sands cohere more strongly than dr>',
the bonding power must depend on the amount of clayey matter and
water contained. The moisture must not be in excess, otherwise the
sand will pack too densely.
Permeability and Porosity
Permeability is the yirojurty which sand possesses of allowing liquids
or gases to filter through it, and depends on the size of the pores.
By porosity is meant the volume of pore space.
These properties are not the same. A sand may contain a few large
openings through which the liquids or gases may readily escape and yet
have a small pore space. On the other hand, the total pore sjjace may
be large, but by reason of the small size of the pores, permeability by
either liquids or gases might be dilTicult.
The permeability of sand may be influenced:
By the tightness of packing;
By the size of the grains;
By the fluxing elements in the sand.
By tamping or packing, the space occupied by a given weight of
sand may be reduced, as the grains are forced into their closest arrange-
ment producing the minimum pore space. Fine-grained sands have
larger pore space than coarse-grained.
468
Texture 469
If silt or clay are present, and segregated, the sand will pack more
closely than if the grains are cemented together in the form of com-
poimd grains. In the latter case the permeability and porosity would
be larger than if the grains were separate.
The decreased permeability under increased tamping explains why
some good sands behave badly. Permeability of sand is also influenced
by the amount of water present. The relation between permeability
and fluxing impurities is shown in the process of casting. If the clayey
particles filling the interstices of the sand fuse when heated by the metal,
their coalescence in melting will close up the pores to some extent. For
this reason, in part, a high percentage of fluxing impurities is undesirable.
The proper permeability of a moulding sand is a matter of vital
importance. A pathway must be opened for the escape of the gases
to avoid blowing. The finer the sand the lower its permeability.
Refractoriness
A moulding sand must be sufficiently refractory to prevent complete
fusion in contact with molten metal. Highly siliceous sands are, there-
fore, the more desirable. At the same time a high percentage of silica is
gained at the expense of alumina and a consequent loss of bonding power.
Generally silica should not exceed 85 per cent. Silica is refractory, does
not shrink when heated, but has no cohesive nor bonding power.
Alumina, a most important component, is present in moulding sands
in amounts varying from 4 to 12 per cent. It is refractory, has great
bonding power, but shrinks greatly when heated. Too high a percentage
of alumina makes the sand impermeable.
Durability
Sands begin to lose some of their desirable qualities after one or
more heats and become dead or rotten. The injury to the sand arises
from its dehydration, or loss of combined water by the heat of the molten
metal, whereby its bonding power is destroyed. The water of com-
bination cannot be restored.
The amoimt of sand burned is a layer of varying thickness next to
the casting.
Texture
By texture is meant the percentage of grains of different sizes. This
is determined by passing the sand through a series of sieves of decreas-
ing mesh and noting the percentage remaining on each sieve. Mr. W.
G. Scott pursues the following method:
"Ten grams of sand are placed on the 100- mesh sieve, together with
ten Me steel balls, and shaken with a circular motion for one minute.
Modeling Sand
?S
^ C> PO t>. t e
• O O '^ O '^ C.O "P P< ^ VJ^O I
vo r*r»rooo rOfON rO'^-r^l'-— ^*yf*)06»O i/)O<)0 ■
o»QNi-it^a»PO»oo>Nvc*^Nt>.a.NoO'^iONM ^-^o t^'O i oo « *o rn
rPtMM M Hiiro u^NWMrOi-<r^r<5oi MMMfO r^« mm
O Nooo^M -r-T'N rooo N o -r« "t 0*0 ■^00000000 O fivooo^ t^**<0 Q Q
^NNNOCO'*<**»^dpO'*rO^*COOWONMoOOO^«OCO^'^WOOO
t^i-« -rri-i*2S t^Tj-Tft^MOiO •"• 0000 c^c»o o o-it^i^toc>f':oovo r*io r*<o
pj * ■«?■ •'TO M-^-rj-i-" O HI MM cirocivO'fMi/^Ooor'iMin
N 00 00 00 -^VO -rfSQO O N O 000 NQO Q Q "rr-JoOQOOC'OvO -I-TmO^OO ^
MfONMN rOM N « •^•^mW.-. t-iN(S N»0
u^ M pi M ^ tov5 -(to M roo M u^o M cS-tO OM mi/>cnw t^o -r-rrot^ir
M*fOdw«t^'*l-«M PO M O-^ MW MVJM *0
MMMNPOM ir MM
88"
"as. : :§
r<5vO
-^ 2
. <u IS
:2 > o
0.2 ?--
o a
a> o
■5 ^t":::'^^
■Q2>iS
i-i -o
c" £
o l-
is '
.a
u 3
2: owwOtjJ ai So5a3a;4
Texture
471
The sand passing through is weighed and credited to the loo-mesh sieve.
That which remains, together with the balls, is emptied on the 80-mesh
sieve and the operation repeated. In like manner sieves of varying
size up to 20 mesh are used. The preceding table shows the texture or
sand from different localities."
Lime is a fluxing element. If present as a carbonate, it loses its
carbonic acid under heat, and in excessive amount the gas causes the
mould to flake or crumble. Caustic lime fluxes and forms slag on sur-
face of castings.
Magnesia is also a flux, and to a modified extent has the effect of lime.
Iron, as a carbonate or an oxide, if present in the mould near the
casting, is converted into ferrous oxide, which is a flux.
Combined water is present in all sands containing clay, carbonate of
lime or gypsum. It is driven off at a low red heat and increases the
porosity of the sand.
Moulding sands are not always used alone. One or more grades are
frequently mixed together. Blending is extensively practiced at the
pit as well as at the foundry. In addition to blending to increase cer-
tain physical properties, foreign substances, such as ground coal, graph-
ite, molasses, flour, beer, linseed oil or cinders are used, either to increase
the bonding power or permeability of the material. A sand deficient
in its natural condition may be greatly improved by "doctoring."
The sand from any one deposit does not always run uniformly, and with-
out previous careful examination of the shipments, unfavorable results
may appear in the foundry.
The following table, taken from "The Iron Age," gives the analysis
of eight different samples.
Constituents
Silica
Alumina
Ferric oxide ....
Lime
Magnesia
Potash
Soda
Water
Organic matter.
92.08
5.41
2.49
91.90
5.68
17
41
92
90
81. so
9.88
3.14
1.04
.65
85
Sands which contain the largest percentage of silica, suflScient alumina
to impart cohesiveness and plasticity, with from i to 3 per cent of
magnesia are the best for facing. Such sand should be entirely free
from lime.
472
Moulding Sand
Spcdfications of \V. G. Scotl, Racine, Wis.
"Moulding sand for iron work generally conUiins from 75 to 85 per
cent of silica; 5 to 13 per cent of alumina; less than 2.5 per cent lime
and magnesia; not over 0.75 per cent soda and potash and generally
less than 5 per cent oxide of iron; not more than 4 per cent of water."
Sand for Brass
Sand for brass may contain a much higher percentage of iron and
lime without detriment.
.\11 moulding sands contain more or less organic matter. Carbonate
of lime must not exceed 1.5 per cent for iron sands, nor 2U per cent for
brass. Iron oxide must not exceed 5.5 per cent for iron nor 7 per cent
for brass sand; organic matter not to exceed i per cent. Any sand
showing an excess of 13 per cent alumina will be rejected.
Analysis
Constituents
Silica
Alumina
Iron oxide
Lime
Lime carbonate . .
Magnesia
Soda
Potash
Manganese
Combined water.
Organic matter. . .
Specific gravity..
Fineness
For light
iron work
82.21
9.48
4-25
2.64
.28
2.652
85.18
For
medium
iron work
85. 85
8.27
2.32
• SO
.29
.81
.10
.03
Trace
1.68
• IS
2.6S4
66.01
For hea\*y
iron work
88.40
6.30
2.00
.78
.50
.25
1.73
.04
2.63
46.86
For light
brass
78.86
7.89
S.4S
.50
1.46
1.18
.13
09
Trace
3.80
.64
2.64
94.88
.\ny of these sands would answer very well so far as their chemical
composition is concerned, for any class of work; but it is absolutely
necessary that they should possess the proper degree of fineness.
The finer sands are less siliceous and as a rule carrj' higher percentages
of alumina and fluxes than coarser grades, as shown by the following
table.
Size
60
80
TOO
100
Silica
95.92
1.29
.56
.10
2.13
97.87
94. 35
1.47
.56
.04
3J?
96.42
94.66
1.47
.40
■ 34
3.13
96.87
91.06
4 57
.80
.72
2.8s
Total
97 IS
Testing Moulding Sand 473
The greater the average fineness, the lower the permeability.
Prof. Ries, from whose paper the above notes are e.xtracted, concludes
that the chemical analysis of moulding sands are not of as much impor-
tance as their physical properties.
To test the "temper" and strength of sand, the moulder squeezes
a handful into a ball. If it takes the impression of his hand readily
and leaves the hand clean, it is considered sufi&ciently damp. Its
strength or binding power is tested by lifting the lump from one end,
or by carefully breaking it apart; or he may squeeze a ball of sand about
a little stick or nail and see if it can be lifted by the stick. He then
blows through it to test its porosity. Such crude tests are in constant
use and, conducted by experienced moulders, serve the purpose.
A. E. Outerbridge instituted a series of experiments to determine
these characteristics more definitely. The following is extracted from a
paper read before A.S.M.E., at their New York meeting in 1907.
"A number of test bars of green sand 6" X i" X i" were made
under uniform conditions of pressure, dampness and quality of material
used in forming the ordinary mould. These little test bars were placed
upon a smooth metal plate with sharp square edges. The bars were
then pushed over the edge of the plate until they broke, when the amount
of the overhang was measured. It was soon found that there was a
great difference in the length of the overhang, which was regarded as
a quantitative measure of the toughness of the sand. These differences
were not even noticeable in the crude ball test.
Samples taken from different parts of a small sand heap that had been
uniformly dampened, or tempered, varied greatly in this respect, owing
no doubt to the irregular distribution of the alumina or clay binder;
and the correctness of this inference was subsequently confirmed by
simple analytical tests. After a sufiicient number of these test bars
had been made and broken to prove the reliability of the method, further
tests were devised to ascertain whether the usual methods of riddling
and mixing the sand for the moulder's use affected its quality either by
increasing or decreasing its toughness, as shown by the amount of over-
hang of similar test bars of green sand. It was proved that the more
thoroughly the sand was worked, the greater the overhang, due, as al-
ready stated to the more uniform distribution of the binder.
"The ideal moulding sand is a material in which the individual grains
of silex, constituting approximately 90 per cent of the mass, are com-
pletely covered with an overcoat of alumina or clay and the more
uniform the grains are in size and shape, the better is the sand with
respect to porosity in relation to the average size of the grain.
" It was found on passing a sample of sand a number of times through
474
Moulding Sand
a haiidriddle, and making test bars from the sample after each riddling,
that the overhang was increased measurably. Thus, a sample of sand,
which, after tempering and mixing by hand with a shovel, showed an
overhang of less than two inches of the test bar, increased to nearly
three inches after a dozen riddlings. It would not be practicable to
treat large masses of sand in this manner, nevertheless, the informa-
tion thus obtained was (4uite valuable and led to imjwrtant practical
results.
"Another novel observation was concurrently made, viz., that the
increased toughness and porosity noticed in these tests might be partly
due to "aeration" or to the separation of the grains of sand when
falling from the sieve to the floor. In order to discover the truth or
falsity of this view, a quantity of sand was shaken in a box with a closed
lid for several minutes and test bars were made before and after shaking.
The correctness of the theory was quickly shown, for the shaking with-
out sieving proved to be more effective than the sieving without shaking.
Tests for porosity were also made, but these were not ver>- satisfactory
owing possibly to lack of suitable means of controlling and measuring
the compressed air."
Using one of Wm. Seller's & Co. 's centrifugal sand mixers, the develop-
ment of which was largely due to Mr. Outerbridge's experiments, a series
of tests were made with facing sand prepared as follows :
Strong Sand
Parts
Strong Lumberton sand (new) 14
Gravel (new) 7
Flour sand (old) 6
Coal dust 2
fe-^'^M?^^^-'^/f:";^'T ''"'¥'■ ''■P?!
--H-i-r:
■rt-->M-;i-v-',t..;-'
|-v.h-.--p':i
Fig.
CrL'cn Sand Test Bars made from One Sample of Sand.
"Fig. 132 is from a photograph showing eleven bars 6" X i" X i",
made from strong sand under uniform conditions of quantity, temper
(dampness) and pressure.
Testing Moulding Sand
475'
"The bar labeled o was pressed from a sample of the sand after
having been dampened and turned over several times, with a shovel,
and only partly mixed. The object of such preHminary mixing is
simply to prevent the coal dust from flying out of the centrifugal ma-
chine on subsequent treatment.
"The other bars were made from the same pile of strong sand, after
passing through the centrifugal machine from one to ten times. These
bars were laid side by side upon the smooth metal plate, resting upon a
table, and were slowly pushed over the edge of the plate until they
broke. "
The following table gives the measurements of the overhang of each
bar as nearly as the somewhat irregular shape of the break permitted.
Inches
No. o length of overhang 2H
No. I
No. 2
No. 3
No. 4
No. 5
No. 6
No. 7
No. 8
No. 9
No. 10
3
SV*
3^
3^
3H
3V^
3'^
3%
3H
"It will be observed that the first treatment increased the overhang
H inch, the subsequent treatments increased the overhang in some
cases H inch, and in some cases not measurably. The first treatment
was, therefore, the most effective, and for practicable purposes one
treatment is often sufficient to insure good mixing of the materials and
thorough disintegration of any lumps.
"The strain tending to break the sand beam is increased by the
additional weight of the increasing length of the overhanging portion,
and also Uy the increased moment of its center gravity. It is readily
seen, therefore, that an increase in length of the overhang of % inch
on the first treatment in the centrifugal machine means an increased
tenacity of 75 per cent. In like manner an increase in overhang of
50 per cent means an increase in strength of sand of 225 per cent.
The illustration, Fig. 133, shows the fractured surfaces of the same
bars.
" Bar No. o shows the heterogeneous components of the partly mixed
sand, while the other fractures show increasing uniformity due to more
thorough mixing, and disintegration of lumps up to No. 3, after which
no further increase in uniformity is observable to the eye.
476
Moulding Sand
.. ijj. — Lnd V lew uf the
Test Bars in Fig. 132.
The illustrations convey a very fair impression of the actual appearance
of the bars. The appearance of the fractured surfaces coincides with
the tests for ovcrhanp, and shows that a single treatment in this machine
is in many cases sutVicicnt, and two
treatments are all that are usually
needed with any sand mixtures.
In mixing core sand containing flour,
the efTectivcness of this method is still
more strikingly evident, owing to the
almost total disappearance of the white
flour, due to its thorough commingling
with the sand and coal in one treat-
ment.
The centrifugal machine is especially
efficient in mixing sharp sand with lin-
seed oil for cores. When so used it is
run at a lower speed than when used for
tempering and mixing moulding sand.
Two treatments are sufficient to insure
thorough mixing of sharp sand and oil for cores.
There are many other devices for tempering and mixing sand mechan-
ically, such as, shakers, revolving reels, etc., which are effective.
The amount of cohesive matter, or binder, in moulding sand should be
limited to that which will permit good ramming, without destroying its
porosity, so that the gases will escape readil}-, without allowing the iron
to penetrate.
The sand in a mould next to the casting is burned and loses much or
all of its cohesion. This is due to driving off the water of combination
in the alumina which cannot be restored. The thickness of the layer
of burned sand depends upon the size of the casting and temperature of
same.
It is impossible to separate all of this burned sand after the removal
of the castings. Much of it gets mixed in the sand heaps, which must
be strengthened from time to time with new sand.
Aside from the loss of combined water and increase in iron content,
chemical analysis shows little difference in the composition of new and
burned sand. This is shown in the table on page 457, made by analyz-
ing the same sand before and after using.
Tn general, moulding sand must possess the following requirements.
It must be sufTiciently porous to allow the free passage of air and
the gases generated in casting.
It must resist high temperature without fusing.
Moulding Sand Requirements
477
It must permit of easy removal from the cold castings.
When rammed into shape it must be firm and sufficiently compact
to resist the pressure of the liquid metal.
It must be strong enough to resist the abraiding action of the stream
of metal entering the mould.
Constituents
New
Burned
Silica
83.49
7.25
4-71
.36
.35
1.30
.41
■ 30
1.66
82.32
7.80
3.98
.54
.41
1.64
.81
.22
■ 19
2.38
100.28
60.80
Alumina
Lime
Magnesia
Potash
Soda
Water
Total
99.86
64.50
For Dry Saiid Moulding
Any sand which, when rammed, will permit of drying into a compact,
coherent but porous mass, will answer the purpose of a dry sand mix-
ture. Many green sands dry into friable masses.
Such sands must be mixed with some substance to give them strength.
For such purpose, flour, stale beer, molasses-water, or clay-wash may
be usid. When flour is used, it is mixed in the proportion of one to
twenty or thirty, depending upon the character of the sand.
With some sands the flour may be dispensed with and the sand
strengthened sufficiently with molasses-water or clay wash. In dry
sand moulds, only one or two inches of the sand next the pattesn are of
the prepared mixture. The remainder of the flask is filled with ordinary
heap sand. This should be as open as possible to permit the ready
escape of the gases. The facing should likewise be as open as can be
safely worked. The amount of moisture should be about the same as is
used in green sand. Dry sand facings must be thoroughly well mixed.
Mr. West gives the following mixtures for dry sand facings.
For Large Spur Gears Parts
Lake sand 12
Strong loam, sand 12
Moulding sand 4
Coke, amount i-io
Flour iM
Wet with water.
47^ Moulding Sand
Ur Pari
Moulding sand i
Jersey sand i
Fire s;ind i
Sen coal 1-16
Wet with thin clay wash.
I'or Close Facing p^^
Moulding sand 6
Lake or bank sand i "-i
Flour i-so
Wet with clay wash.
This mixture may be used for blacking, using ilour 1-40.
For Cylinders p^^
Fair loam 4
Lake sand i
Sea coal or coal dust 1-14
Wet with clay wash.
General Work _ _^
Part
Moulding sand i
Bank sand i
Flour 1-30
Sea coal 1-20
Wet with clay wash.
Or Parts
Strong loam sand 6
Lake sand 6
Old drj' sand :;
Flour 1-40
Sea coal 1-14
Wet with water.
For Rolls n .
Parts
Dry sand 2
Lake sand i
Sea coal 1-12
Flour 1-18
Wet with clay wash.
For Renewing Old Dry Sand for Body of MoMs ^
Old sand 16
Lake sand 8
New loam 4
Wet with water.
Core Sand
479
Dry Sand Moulds
Old dry sand becomes very close. It should be passed through a
No. 8 riddle to remove the dust and very fine particles,
material mixed with new sand works well.
The coarse
Skin Drying
Instead of making dry sand moulds which are baked in the oven, moulds
are more frequently "skin dried." Skin dried moulds are essentially
the same as "dry sand" except that the drying does not extend to as
great depths and the facing is not as strong.
For skin dried moulds mix with ordinary heap sand about i to 30 flour.
After the mould is finished sprinkle with molasses water. The mould is
dried either with the kerosene blow torch, or fire of wood, coke or char-
coal, built in iron baskets which are placed in the mould. Often the
mould is covered with sheet iron and fires are built on top of the iron.
In drying copes, they are suspended and fires built under them.
Before drying, the moulds are brushed with black wash, made of plum-
bago and water, to which a little molasses water or clay wash is added.
Sometimes moulds are black washed after drying.
Core Sand
Core sand should be high in silica and low in alumina. A sand con-
taining much alumina does not permit the ready escape of gases after
baking.
Analyses of Core Sands
(W. G. Scott)
Constituents
Good
quality
core sand
Fair
quality-
core sand
Silica
94.30
1. 95
.33
1.63
69.31
4.76
1. 58
3.50
8.19
7.77
.12
2.95
1.82
Lime carbonate
.54
.05
1.05
.15
Alkalies
Combined water
Organic matter
"Since the greater portion of a core is to be entirely surrounded by
metal, the sand of which it is composed encounters conditions much
4S0 Moulding Sand
more st-verc than lliosc mul wiili l)y facing siinds. Three conditions
must be noted.
First. — The core is subjected to much handling.
Second. — The gases generated in casting must find egress through
the core and not through the metal.
Third. — The core has fmally to be removed from the casting.
"All cores, before entering the mould, are dried, and in this condition
must be hard enough to permit handling, and porous enough to admit
the free escape of gases. Yet the sand must not be burned or converted
into a compact mass by the heat; if so, it will be e.xtrcmely dilDcult t<3
remove from the casting.
"A sand high in silica should yield the best results. To such a sand
the necessary bond must be added. An ideal core sand is one in which
the silica is given bond by the addition of an organic substance, which
produces a firm core, capable of withstanding high temperatures and
resisting the penetrating action of fluid metal. Such a core is friable
in tlie cold casting, and is, therefore, easily removed.
"If bond is given to silica by clayey matter alone, then the metal
bakes the cores hard, and renders their removal dilUcult.
"A hard surface imparted to the sand by ramming is fatal, as fluid
metal will not lie on it, but a hard surface resulting from the binder
does not necessarily represent an impervious one, and fluid metal will
usually lie quietly on it. Heat tends to loosen a sand made hard in
this way, instead of fusing it.
Core Mixtures
"There should be just enough bonding material in a core mixture to
coat each individual grain of sand, without filling the interstices between
the grains, and the value of the core depends greatly upon the tliorough-
ness with which the mixture is incorporated. Too much attention
cannot be given to this feature. As a rule mechanical mi.xers give the
best results. The binders in common use are
Flour. Linseed oil.
Glue, Rosin,
Molasses, Rosin oil.
In addition to these there are many commercial binders of more or
less value, all of them designed to offer a binder cheaper than those
above mentioned.
Cores made with flour, glue or molasses soften quickly when exposed
to dampness. Therefore they must be kept in a dry place, or used soon
after they are made. The moulds in which they are placed should be
Dry Binders 481
poured shortly after the cores are set. If allowed to stand for a period
of 24 hours, the cores should be taken out and dried.
Cores made with glue are very friable when hot and must be handled
with great care. Less gas is given off by them than by those made
with any other binder. Glue cores leave a smoother hole and do not
require to be blackened as do flour cores.
Flour is mixed with sand in proportions varying from i to 18, to i to
30, depending upon the strain which the core is to resist. The weaker
the mixture, the more readily the gas escapes.
Glue is first soaked in warm water and then boiled until entirely dis-
solved. Glue water should consist of 2 pounds of glue to 3 gallons of
water. This mixture is sufficient to treat 100 pounds sand.
Rosin must be first pulverized; it is then mixed with sand in propor-
tions of I to 20, or I to 30, as required.
Rosin oil is used i to 18, or i to 24 as the requirements of the case
indicate.
Molasses, mixed i to 20 water is used more for spraying cores to give
a hard surface, than for entire mixtures.
Linseed oil with sharp sand, mixed about i to 30 furnishes the best core
of all binders. It is strong, porous and is easily removed from the
casting. For light, delicate cores, such as gas engine and automobile
work it is unequaled.
Large percentages of old cores, gangway sand and moulding sand may
be used in the core mixtures.
Core sand should be quite damp for use, but not so wet as to adhere
to the core box. Wet sands require much less binder than dry.
A saving may be made in the use of flour by boiling it thoroughly
and then using the paste (very thin) to wet the sand. As already
mentioned, the more thoroughly the binder is incorporated with the
sand, the better will be the cores.
Mr. A. M. Loudon made an extensive series of experiments to deter-
mine the comparative values of various core binders, and published the
results in a most interesting paper presented to the American Foundry-
men's Association at the Cleveland meeting 1906. From it the follow-
ing extensive extracts are made.
Dry Binders
Test No. I. — Flour sand core mixture. p
New moulding sand 2
New fire sand i
Flour I to 12 and i to 18
Wet down with thick clay wash.
4S2 Moulding Sand
Cures from this mixture are usually very strong. If not thoroughly
dried or if slightly burned or scorched, cause great trouble by blowing
or scabbing. Cores were removed from castings with difficulty. Be-
came damp in mould quickly, especially small cores.
Test No. 2. — Syracuse dry core compound mixture.
Old flour sand V4
New moulding ^
Sharp or beach V^
One part binder to 35 parts sand thoroughly tempered with water.
Cores made from this mi.xturc dried quickly, were clean and sharp and
left good surface on castings. Resisted dampness well.
Mr. Loudon states that the dampness test for each mixture was to
dij) a core partly in water, allowing it to stand after removal from the
water for two or three days to air dry only. Iron was then cast in an
open mould around the end which had been immersed.
Test No. 2. — Included the water test as did all the other tests for
dry and oil binders, the conditions being the same for all.
The binder used in Test No. 2 stood the water test in a manner en-
tirely satisfactory. The hot iron came in contact with the core without
any disturbance.
This binder in Mr. Loudon's judgment is best suited to large plain
work, or small round and square cores.
Test No. 3. — Dextrin or British gum mixture.
Per cent
Old flour sand 5°
New moulding sand 25
Beach or sharp sand 25
I part binder to 150 parts sand, tempered with water.
This mixture was valuable for large cores, strong, with sharp edges
and easily dried.
If the cores are burned in the oven, wash with some of the binder
dissolved in water, and dry in oven for ten minutes. They are thus
completely restored. For small intricate cores the following mbcture
was used.
Per cent
Old sand 33
New moulding sand 33
Sharp sand 33
1 part dextrin to 100 parts sand.
\ core from this mixture was treated by the water test, and allowed
lo stand for two days. It resisted the action of melted iron better than
cores from many nuxtures, when fresh from the oven.
Dry Binders 483
Test No. 4. — Wago core-compound mixture.
Per cent
Old sand 33
New moulding sand 33
Sharp sand 33
I part Wago to 30 parts sand.
Made a good core; did not gum the box, and gave off very little
smoke.
A second mixture made from Wago:
Per cent
New moulding sand 50
Sharp sand 50
I part Wago to 35 parts sand.
Unusually strong, true and sharp, but not as easily removed from
casting as the first mixture with Wago.
One of these cores was dipped in water and left for two days to air
dry. The melted iron was perfectly quiet when poured around it.
Test No. 5. — Cleveland core-compound mixture.
Per cent
Old sand 33
Sharp sand 33
New moulding sand 33
I part binder to 30 parts sand tempered with warer.
Strong core, easily removed from casting, very satisfactory for general
use.
A mixture i part binder to 40 sand was tried, but cores were too soft.
Cores from the i to 30 mixture when submitted to the water test gave
excellent results.
Test No. 6. — Peerless core-compound mixture.
Per cent
Old sand 33
Sharp sand 33
New moulding 33
I part binder to 30 parts sand.
The mixture as above given was unsatisfactory, therefore, the follow-
ing mixture was tried.
I part binder to 20 parts sand.
This was satisfactory, being strong and true to box, but harder to
remove from castings than most of those previously tested. It gave
good results when submitted to the water test. The iron showed no
signs of blowing.
4S4 Moulding Sand
Tests Nos. 7, 8, 9 were made from sam|)lcs of flour submitted. Sand
mixed in same proportions as before.
Thus, tiic first sample of Hour was mixed with 15 sand,
the second sample of flour was mixed with 18 sand,
the third sample of flour was mixed with 20 sand.
These were made as comparative tests of the diflcrent samples of
flour.
1. Made tlie strongest core, but was the most difficult to remove from
the casting.
2. Good for general work.
3. Was too soft.
A mixture of i to 18 from 3 to 9 was good, better than Nos. 2 to 8 in
same proportion. Each of the above mixtures was subjected to water
test and failed. When withdrawn from the water and held in hori-
zontal position, thej' broke at the line of submersion. Nos. 2 and 3 were
not as good in this respect as No. i.
The cores from the peerless compound and most of the others resisted
the water so that it could be wiped off with a rag without injuring the
cores.
Test No. 10. — Paxton dry compound mixture.
Percent
Sharp sand 33
New moulding sand 33
Old sand 33
I part compound to 30 parts sand, made a very soft core.
When mixed i to 20 it made a very strong core.
One of these when subjected to the water test went to pieces, while
the last mixture made a strong open core. It is readily affected by
moisture.
Liquid Core Binders
Test No. II. — Holland linseed mixture.
Parts
Sharp sand 30
Oil I
Made a strong core for small and medium shapes, but required vent-
ing. A core from this mixture immersed in water for half an hour was
returned to the oven and dried. It was then as good as any which had
not been immersed.
Test No. 12. — Syracuse core oil mixture.
Parts
Sharpsand 35
Oil I
Moulding Sand Mixtures 485
Tempered with water and well mixed. These cores were excellent;
without vents were not satisfactory.
A core from this mixture was immersed for 15 hours, taken out and
dried in the oven for 15 minutes. Molten iron when cast about it
showed no disturbance.
Tests Nos. 13, 14, 15. — Sterling oil samples from each of above were
mixed at same time.
Mixture Parts
Sand 3S
Oil I
Nos. I and 2 of these samples showed too much oil. No. 3 was about
right.
Another mixture was then made.
Parts
Sand 45
Oil I
Nos. I and 2 dried out quickly and made good strong cores, but when
subjected to the water test the moisture acted quickly upon them,
more so than on the other sand and oil mixtures. The cores were
strong and were easily cleaned from the castings, but moulds which were
left over night, and poured the next day blew very badly.
Test No. 16. — Gluten or Esso mixture. Percent
New sand 33
Sharp sand 3^
Old sand 33
Gluten I part to 30 parts sand
Cores were so hard that the iron would not lay to them.
One part gluten to 50 parts sand, — cores were good, sharp and
strong. Iron somewhat disturbed. The gluten was mixed with water
and the sand tempered with water.
One part gluten to 70 parts sand.
These cores were soft and did not stand the fire as well as the others.
When subjected to water as before
I to 30 stood very well,
I to 50 became soft,
I to 70 melted like sugar,
showing that for a free core, one not inclined to blow, i to 70 took
moisture very quickly.
Test No. 17. — Glue melted in hot water mixture. p^j. ^^^^^
New moulding sand 25
Sharp sand 4. 25
Old sand 50
I pound of glue to 100 pounds of sand for small cores.
I pound of glue to 150 pounds of sand for large cores.
486 Moulding Sand
Lump or granulated glue, llic ( hcajK-r llie IjcUcr.
The glue water was made by dissolving two pounds of glue in three
gallons of water.
Cores from the first of the glue mixture when submitted to the water
test absorbed water but hold their shajjc. After redrj'ing were as g(xxl
as when first made. Should such cores be burned in the oven, washing
them with a mixture of plumbago and glue water restores them.
Mr. Loudon highly recommends the first of the above glue mixtures,
using it for cores without vents for small port cores.
Cores made from it can safely be used for all purposes, taking care to
iiave them thoroughly dried.
Cores for large beds have remained in the mould three and four days
without causing trouble.
Test No. 18. — Glucose melted with hot water mi.xture. „
Per cent
Sharp sand 33
New moulding sand ^^
Old sand ^^
I pound of glucose to 100 pounds of sand.
Cores of every description were first class, easily dried, easily cleaned
from casting, emitting no smoke. They acted like green sand cores,
dried and gave good results in every respect.
Parting Sand
The particles of burned sand, having been deprived of combined mois-
ture will not cohere. Such sand, taken from the cleaning room, is used
to separate the parts of the moulds and is also dusted on patterns to
prevent the moulding sand from adhering to them.
A most excellent parting sand for intricate work is made by saturat-
ing very fine burned sand with kerosene or crude oil, and setting fire to
the mixture.
Lycopodium is also used for parting in particular work, but the high
price subjects it to adulteration.
Facings
When molten iron comes in contact with a sand mould it tends to
penetrate the pores of the sand and to fuse the particles in immediate
contact, leaving a rough surface or scale, varying in thickness from H*
to H of an inch, depending on the weight of the casting.
Facing sands containing large p#rcentages of carbonaceous material
are used to prevent this difficult}' and to lea\'e smooth surfaces on the
castings. The carbon of the facing is decomposed by the heat, and the
Facings 487
gases generated prevent the hot iron from attacking the sand. Facing
sand which is composed of ground coal (sea coal), and sand in the pro-
portions of from I coal to 8 sand, and i coal to 20 sand, depending upon
the character of the work, is placed next to the pattern in a layer from
H to i^^ inches in thickness. Back of this and completely filling the
flask is the heap, or floor sand. By the continued use of facing the
floor sand becomes black with it.
The term facing includes
Sea coal, Coal dust,
Plumbago, Charcoal.
Talc (or soapstone) ,
It must adhere to the surface of the mould and cause the casting to
peel when shaken out.
Sea coal is a ground bituminous gas coal, free from sulphur and slate.
It is mixed mechanically with new moulding sand in the proportion
of I to 10, usually, and used generally on all work. For the purpose of
obtaining smoother and brighter surfaces than result from the use of
sea coal alone as a facing, the moulds are finished with plumbago or some
mixture of which plumbago is the base. Plumbago is the best of all
materials for this purpose.
Soapstone is used largely in connection with plumbago as an adulter-
ant, as also are coke dust and the dust of anthracite coal.
The facing is applied to the mould either by hand, with a camel's hair
brush, or it is mixed with molasses water and applied by a spray or with
a brush. The latter method is usually used on dry sand moulds.
Mr. W. G. Scott gives the analysis of Yougheogheny gas coal, from
which the best "sea coal" facing is made as follows:
Per cent
Moisture i . 00 Sulphur 0.33
Volatile matter 35 • 00 Ash 5 ■ 60
Fixed carbon 58 07 Specific gravity i . 28
Cannel coal is also used as facing and analyzes as follows:
Moisture 3 . 30 Sulphur o. 20
Volatile matter 48 . 50 Ash 6 . 00
Fixed carbon 42.00 Specific gravity 1.229
"Sulphur and ash are the two constituents of sea coal to be guarded
against. If sulphur exceeds 0.75 the coal is inferior, and if sulphur is
in excess of 1.5, the coal is unsuitable for facing.
"Facing containing over 11 per cent ash ought not to be used.
"Slack and culm are often ground and used as adulterants, but are
readily detected by the amount of ash present.
488 Moulding St.uifl
Graphite Facing
"Pure gr;ii)hile contains al)oui <)') per <ent carbon, but this degree
of purity is not found in the natural product. A high grade natural
graphite contains 75 per cent carbon; inferior grades contain from 15
to 65 per cent.
"As the regulation method of determining carbon in facings is to
burn oil a weighed amount of sample and call the loss carbon, an un-
scrupulous dealer may add coke or anthracite dust sufBcient to raise
the carl)on content to any desired point.
"Adulterations of this sort may be determined in several ways.
"If several small beakers arc filled with water and pure graphite,
coke dust, anthracite dust, soft coal dust or charcoal are carefully
sprinkled on the surface of the water, each in a separate glass, none of
the powder will settle except the coke dust and some charcoals. This
test eliminates coke dust and non-greasy charcoals. By shaking in a
test tube M gram of the sample with 15 c.c. of acetone and allowing
the mixture to stand 10 or 15 minutes, it will be seen that the pure
graphite settles clear, leaving the liquid colorless. Coke imparts a
gray to the solution and remains in suspension a long time; anthracite
coal imparts a faint brown color and settles more rapidly; soft coal
dust imparts a deep brown color.
"The above tests are qualitative onl}'. Equal parts of glacial acetic
acid and sulphuric ether answer as well as acetone for this test."
The following analyses from Scott of graphite, coke dust, coal and
charcoal give a general idea as to the character of the different forms
of carbon.
Chemically Pure Graphite
Per cent Per cent
Moisture o . 02 Sulphur o . 00
Volatile matter 0.09 .\sh o-. 10
Fixed carbon 99-79
Commercially Pure Graphite
Per cent Per cent
Moisture o. 15 Sulphur trace
Volatile matter o . 79 .^sh 4 . 46
Fixed carbon 94.60 Specific gravity 2.293
Stove-plate Graphite Facing
Per cent Per cent
Moisture o. 75 Sulphur o. 20
Volatile matter 5.29 .\sh 37-66
Fixed carbon 56. 10 Specific gravity - -363
Facings
489
The Composition of Ash in Above Sample is
Per cent Per cent
Silica 25 . 60 Lime i . 07
Alumina 5.25 Magnesia o . 80
Iron oxide 4-94
Cheap "Green Sand" Facing
Per cent
Moisture o . 45
Volatile matter 5 . 75
Fixed carbon 41-49
Sulphur 0.62
Ash 51-69
Specific gravity 2 . 489
Per cent
Of which the ash analyzed.
Silica 32- 13
Alumina 2.77
Iron oxide 6 . 78
Lime i . 64
Magnesia 8.32
This sample was said to contain 25 per cent soapstone.
The following analyses are given for comparison.
Coke Dust
Per cent
Moisture o. 19
Volatile matter i . 40
Fixed carbon 86 . 89
Per cent
Sulphur 0.98
Ash 10.54
Specific gravity 1.886
Anthracite Coal Dust
Constituents
Selected
lump,
per cent
Screenings,
per cent
Moisture
Volatile matter.
Fixed carbon . . .
Sulphur
Ash
Specific gravity
-OS
4.40
92.00
.57
2.98
1.565
3.50
3.99
5.70
.86
r.9S
C-590
Analysis of Soft Coal
Constituents
Selected
lump,
per cent
Screenings,
per cent
1.39
33.82
58.68
.96
S.iS
1. 321
4.44
32.79
37.61
3.10
22.06
1.486
Sulphur
Ash
400
Mouldiii)^ S;in(l
Analysis ok Wood Charcoal
c .
Common
variety,
per cent
Medicinal,
per cent
38j
26.57
66.63
None
a. 97
1.363
3.66
33. IS
58.52
None
4.67
I 412
Ash
Analysis of Soapstone and Talc
Constituents
Vermont
soapstone,
per cent
French
talc,
per cent
SI. 20
8.4S
5.22
1.17
26.79
717
61.8s
■ 25
2.61
Trace
34. 52
.77
Iron o.xide
Magnesia
Water
Mr. Scott gives the following as a test for the presence of anthracite
coal in graphite.
"Treat 0.5 gram of sample with 50 c.c. of strong nitric acid, boiling
about 10 minutes. Then add 0.5 grams of pulverized f)Otassium chlo-
rate and boil until most of the chlorine is oCF. Dilute with 30 c.c. of
cold water and filter, reserving the filtrate for examination.
The filtrate from pure graphite treated in this manner should be
clear and colorless unless iron is present, in which case it may be some-
what yellow in color.
The filtrate from any kind of coal and charcoal will have a distinct
amber brown color, the soft coals giving a deeper color than the hard
coals or charcoal.
To confirm the test add 30 c.c. of stannous chloride solution and
note the change in color. The graphite filtrate will be reduced to a
colorless liquid if iron is present, or remain unchanged if free from
iron; whereas the filtrate from the coal having an amber color will be
much deeper in color and in some cases nearly black. The only caution
to be observed in this test is sulTicient boiling to remove all of the hydro-
carbon coloring matter in the coal.
The determination of magnesia is the onl)- method to be relied upon
for detecting the addition of soapstone to graphite. Mi.xed with graph-
Facings 491
ite or anthracite dust, it answers very well for certain classes of work.
Facing made entirely of anthracite or mixed with a low grade of
natural graphite is termed Mineral Facing and is represented by one
or more letters X to designate the fineness. Such facings may be added
to wet blacking; or mixed with graphite, may be used on heavy work.
All facings should be kept in a dry place as they readily absorb mois-
ture. A high grade of plumbago makes the most suitable facing for
producing bright clean castings. A good plumbago must not only
have the proper chemical analysis, be of such refractory nature as to
withstand the hot iron from cutting into the mould, but must also be of
such a nature as will not retard the flow of the molten metal."
CHAPTER XXT
THE CORE ROOM AND APPURTENANCES
Tin: important relation which the core room bears to the foundry
product demands the most careful consideration as to location, con-
struction and equipment. Unfortunately for the core maker, such con-
siderations have been neglected in many foundries. Whatever could,
htus been made to serve so long as the imperative demands were
satisfied. Good castings cannot be made without good cores. Their
production requires the same attention and forethought as the making
of good moulds.
Constant intercommunication between the moulding floors and core
room, the handling of sand, fuel and ashes, etc., point to a location
affording the greatest accessibility to the moulding floors and to the
storage for sand and fuel.
The core room should be well lighted and ventilated. The space
allotted should be ample, not only for the convenience of the workmen
but for storage of supplies, movable equipment, core plates, etc., so that
the place may be kept neat and orderly. The arrangement of the
work benches, machinery, cranes, racks, etc., must be governed by
circumstances.
The oven is the important feature in the core room. WTiere the cores
arc not very large and the demand for them not ver\' great, some form
of fxjrtable oven may answer the purpose. Many varieties are made,
adapted to small and medium work. The convenience offered by them
in placing and removing cores before and after baking, the small floor
space occupied and the small fuel consumption commend them for
light work. Most large foundries have one or more of these ovens.
\\Tiere great quantities of small cores are required, some form of con-
tinuous oven is frequently used. An oven with a revolving reel is very
desirable for medium-sized work.
The sketch below is taken from West's ".\merican Foundry Practice,"
page 133-
"The oven is round, with an upright cast-iron shaft, having five
flanges on which to bolt plates or arms A'A', the shape of which is
shown at B. This oven is built with an 8-inch brick wall to form the
outside and a cast-iron plate for the top, on which plate is a box D, to
492
The Core Room and Appurtenances
493
which a cap can be bolted to hold the top of the shaft, the bottom of
which rests in a cast iron seat.
"The fireplace should be outside of the circle, as shown, so that the
cores will not get the direct heat from the fire. In building the walls,
hinges HH, should be built in for hanging the oven door.
Fig. 134.
"This door should be made in two pieces, so as to open to the right
and left, and should be the full height of oven, to provide for putting
cores on the top shelves.
"The chimney should have a top flue, as well as a bottom one, as
shown at PP and dampers in both, so as to throw the heat down or
up, as required.
"When starting a fire, both dampers should be open, and when the
cores to be dried are on the top shelf, the bottom damper may be closed,
and vice versa.
"This style of oven is very handy for drying cores that can be lifted
by hand, and will hold and dry more cores with less fuel than any oven
I know of. Should you want to dry a single core quick, put it on the
top shelf and turn it round to the fire.
"This oven can be filled with cores and they can be taken out again
without going farther than the door, which alone is of great value to
the core maker.
"The size of this oven was about 8 feet in diameter and 7 feet high."
The oven was heated with a cast-iron fire basket.
On page 135 of same book is shown a sketch for a small oven of which
Mr. West speaks very highly. The advisability of building such an
oven is somewhat doubtful, however, in view of the great variety of
portable ovens on the market which can be purchased at a reasonable
price.
4*)4
I'liL- Core RiKtin .imi Appurlcnances
For larKC cores the dimensions of llie oven arc governed entirely by
llie re(|uiremcnts of the foundry.
Unless tlic drying of large moulds is comtcmj)lated, it is not advisable
lo make an oven more than 12 feet wide by 20 feet long. Where greater
capacity is required, it is better to duplicate it, on account of the greater
loss of fuel in large ovens, which are not stored to their full limits.
S^ Firina
^^^mmmmmm^mm^^^
Fig. 135. — Core Oven
Among the sketches of large ovens shown bj- Mr. West, that on page
227, "Moulders' Te.xt Book," presents a most excellent design. An en-
larged sketch is given above. The dimensions may of course be varied
to suit the requiremenls.
Mr. West in descriliing ovens of this design says: "They surpass
any 1 know of for properly drying moulds or cores. Although we use
The Core Room and Appurtenances 495
slack or soft coal for the fires, a mould or core will when dry, be almost
as clean as when first put into the oven. Another important feature
is that the ovens will dry rapidly and still not burn a mould or core. "
Three ovens are fired from one pit, the draft flues being at the
extreme ends of the oven and the channel for heat to travel being di-
verted from side to side. There is but a small chance for heat to escape
entering through the joints and thickness of the boiler plate up into the
oven, before it can enter the flue at F, H and K. The arrow-like lines
represent the heat passing from the fires to the flue. The partitions X
divert the direction of the heat and also support the covering plates
and carriage tracks.
The covering plates, 2, 3, 4, 5, 6 and 7 are boiler iron !4 inch thick,
cut into sections the width of the flue partitions.
The plates on the outside of the track are free at any time to be
lifted in order to clean out the soot. Where the fire enters the first
flue or partition," the boiler plates are left out, and in their place a cast-
iron plate '/2 inch thick, having prickers 2 inches long (on underside)
and daubed up with fire clay is used.
This is to prevent the direct flame from buckling and burning out the
plates.
There are no holes whatever in any of the plates, the heat passing
through them and their joints, which of course are not air tight, heat
up the oven.
Were there holes in the plates, they would seriously injure the draught
of the under flues, and also let much of the smoke into the ovens, thereby
destroying essential points to be overcome in using slack for firing.
To be able to fire with sl?rtk or soft coal, and still keep moulds and
cores free from soot is something that will be appreciated by all moulders
and core makers that work around ovens. Not only does soot make
everything look dirty, but it is more or less productive of rough castings.
"Another arrangement which I doubt being found in any other
foundry oven is that for preventing smoke. Upon each side of the fire-
places, about on a level with the fire, are ?6-inch openings, seen at E
in elevation. In the rear of these openings the brick is left open about
4" X 6", running the entire length of the fireplace. This opening gives
a reservoir in which the air becomes heated before being drawn into
the fireplace. This is, I believe, claimed to be beneficial in assisting
'smoke burning' or combustion."
The grate surface for the fire contains an area equal to about 32" X 38".
"The fireplaces are all faced with one thickness of fire bricks, and the
tops of fireplaces are arched over with fire bricks. Under the large
oven are two fireplaces. The one nearest core oven is used for heating
496 The Core Room and A|jpurlenanccs
llic same, and is so constructed with damper arrangement, that should
an extra heat be required in the large oven, both of the fires can be turned
on to it.
"As shown at D in elevation of oven, each one has a small manhole
door, whereby liie flue leading to the chimney K can be readily cleaned.
"The lops of the ovens are covered with a series of arches.
" Upon tlic toi)s of these ovens we store anfl keep shop tools, etc. The
way the tops arc formed, tons of weight can be laid ui>on them and do
no harm; and the comljined area of the tops makes a splendid store-
room for systematically keeping foundry tools."
" .'Vltogether the ovens are a success, and a credit to their designer,
the late Mr. Halloway. "
Note. — Only one of the ovens is shown in the sketch. The other two
are in all respects the same as the one shown.
Another excellent design for a large oven is shown on page 129, West's
"American Foundry- Practice." A description of one good oven is all
that can be permitted here.
The essential requirements for an oven are good draught and means
for regulating it. Where the fire is made directly in the oven, as is
frequently the case, there should be openings into the chimney at the
top and bottom, with dampers for changing the direction and regulating
the draught. There should also be a damper on top of the chimney
so as to retain the heal when the fire is not urged. Aside from coal and
coke, crude oil and natural gas are used for heating.
The temperature of the ovens should range from 450° to 900° F. and
must be varied somewhat according to the core sand mi.xtures.
Flour sand requires a higher temperature than rosin or oil. The
workmen soon learn the part of the oven in which the drying is most
rapid and place the cores where they will dry quickly or slowly as re-
quired.
A pyrometer is a most valuable attachment and will often prevent
the destruction of cores by overheating.
The doors to these ovens are usually made in one piece of sheet iron
and arc provided with counter weights, so as to permit of being raised
or lowered easily. In some cases they are made of overlapping, plain or
corrugated strips, which are wound upon rollers.
Core Oven Carriages
These are mounted on wheels having anti-friction bearings. The
top of the carriage extends over on each side as far us convenient. The
carriages have usually three or more decks as required. The whole
Wire Cutter 497
is made up of bars and angles properly trussed, and left as open as
possible, for the passage of hot air to the cores.
The track should be evenly laid, so that there may be no jarring as
the car passes over it.
Mixing Machines
Machines for this purpose are of greatest value to the core room.
The worth of a binder and that of a core depends largely upon the
thorough incorporation of the components of the core. Each individual
grain of sand should receive a coating of the binding material, but the
latter should not be present in such quantity as to fill up the pores of
the sand. To accomplish this result requires long-continued manipu-
lation. The best results are obtained by a mechanical mixer, driven by
power or by hand, as the conditions permit. A machine of this sort is
indispensable in a well-appointed core room. There are many different
kinds on the market. The centrifugal machine is, perhaps, the most
desirable.
Sand Conveyors
Many of the large foundries are provided with sand elevators and
conveyors, whereby the sand after mixing is carried to the bench of
each core maker and delivered through spouts. The necessity for
appliances of this sort will be indicated by the extent and character of
the work, simply bearing in mind that the core maker should have the
sand delivered to him.
Rod Straighteners
Core wires and rods by use become crystallized, and bent in all manner
of shapes; so that it is not unusual to find about core rooms, large
heaps of material of this kind, which are picked over by the core maker
in search of what he requires. In this condition it is practically worth-
less; therefore the expense for wire and rods is not inconsiderable. By
annealing they may be softened, and if then passed through a straight-
ener are rendered serviceable. Both hand and power machines for
this purpose are made.
Wire Cutter
A. machine for this purpose is very useful where there are many small
cores of a kind to be made. Otherwise the common hand cutter serves
the purpose.
408
Tin- Core Room Jind Appurtenances
Sand Driers
A SJind drit-r is frequently very <lisir.il)le. A simple one can l>e made
by taking a sheet-iron cylinder from 15 to 20 inches in diameter,
and say 5 feet long. Surround this by an inverted sheet-iron frustum
of a cone, having a diameter at the base sudi that the space Ijetween
it and the cylinder may contain any desired amount of sand. Near the
intersection of the cone and cylinder there should be two or more small
sliding doors. Mount the cylinder on a grate for coke; provide a
cover for the top for checking the fire. This costs little and will dry
sand very rapidly. The cut below shows a drier in freciuenl use.
The Champion Sand Dryer
Capacity, 20 tons dail)-.
Reciuires less fuel and has greater capacity than any of the dr>'ers
now in use, and being made of cast iron throughout, will outlast any
_^_, made partially of sheet iron.
The parts, being made interchangeable, can be
replaced at any time.
Set the dryer upon a solid foundation, and first
placing casting No. i. in position, follow up with
the other casting as numbered.
No.
.Vsh pan and base.
Flat rings, with slides.
Wide ring of outside casing.
Fire box.
Rings with which to form casing.
Center pipe.
Outside pipes.
Plates to secure top of pipes.
Cover for pipes and seat for stove pipe.
Flaring ring.
'■ II. Slide.
" 12. Door.
Nos. 13 and 14. Grates.
Fire lightly, being careful not to get the dryer too hot. Never leave
the dryer full of sand with a lire in it; and do not attempt to use it for
heating purposes, as it radiates no heat outside the casing.
Core Plates and Driers
\ great variety of core plates, varying in sizes, is required. These
plates are usually rectangular and for sizes less than 12 X 20 are it inch
Cranes and Hoists 499
thick. Larger plates are thicker. Each must be smooth and true on
one side; on the opposite side are cast stiffening strips. Larger plates
are of sizes and shapes required. For work of extreme accuracy, the
plates should be planed on one side. The exposure of these plates to
frequent heating and cooling finally warps them to such an extent that
they become unserviceable. There should be racks for the storage of
these plates so that any size desired may be quickly found.
Irregular shaped cores which cannot be turned out on flat plates, or
which must be supported in drying, require iron shapes made to conform
to one of the surfaces of the core. The shapes are in reality portions
of the core boxes. The cores are baked on them, thereby retaining the
original form when dried.
The expense for driers is often great, therefore they should be handled
carefully, and put away with the core boxes to which they belong.
Core Machines
Wliere great numbers of small cores of uniform cross section, round,
square, oval, polygonal or rectangular are used, a core machine is
of the greatest value. One of these machines will make 200 or 300
linear feet of small core in an hour. The cores are pushed out of a
former as sausage from a sausage machine, on to metal drying trays.
The cores are cut up into lengths as required and pointed to fit the
prints.
There are several different machines of this kind made, but the
differences are not important.
Machines
Moulding machines are used in making cores for plain work, where the
demand for the product warrants.
Machines for making straw rope. These are little used except in
pipe foundries. It occasionally happens in a jobbing foundry that a
rope body for a core is required. In such a case the rope is made by
hand. Straw rope is furnished by supply houses at low cost.
Cranes and Hoists
The requirements and location of these implements are regulated by
the character of, and demand for, the work. Where the work is large
there should be a traveling crane covering the track and the "big floor. "
Circumstances will dictate in such cases.
500 The Core Room and Appurtenances
Oilier ai)i)lianccs arc screw clamps, spike claws, glue heaters, clay
tubs, horses, etc. In view of the great number of implemenlii
nccdetl about a core room, the necessity for adequate room, that the
place may be kept neatly, orderly, and as cleanly as possible, will be
apparent; and as the production of good castings depends upon the
character of the cores, as well as upon that of the moulds, the neglect
to provide proper facilities for the core maker is inexcusable.
CHAPTER XXII
THE MOULDING ROOM
Too much attention cannot be given, in selecting a location for a
foundry, to the character of the ground; good drainage is a primary
requisite. Gravelly subsoil is altogether desirable. If the natural
features of the situation do not permit proper drainage, the surface
should be raised b}' proper filling so that the floor may be at least one
foot above the ground exterior to the foundry. Much damage often
results from the flooding of the floor during severe storms.
Pits of greater or less depth have frequently to be made in the floor
for heavy castings, and if the ground is not well drained great expense
may be involved in keeping the pits dry.
In preparing the moulding floor the surface soil should be removed
and replaced with coarse sandj'^ loam. After this is leveled it should
be covered with from 2 to 3 inches of moulding sand, rammed and
leveled.
Provide gangways of liberal width, one leading from the cupola and
others perpendicular to it. The number and location of the gangways
and the subdivisions of the floor are dependent on the character of the
business.
The main gangways, particularly the one leading out of the foundry,
should be supplied with railroad tracks of standard gauge, connected
to the switching sj'stem.
Where it will best serve the purpose, ample space should be set aside
for the Foundry Oflice and Pattern Loft. In the selection of this
space regard should be had for access to the pattern storage. If at
one end of the shop, it may be overhead.
The proper lighting of a foundry is a matter of the greatest impor-
tance. The windows should be large and close together, and all light
possible admitted through the roof. The monitor roof is generally
adopted, but the saw tooth or weaving shed roof serves well. What-
ever style is adopted, it should carry provisior for good ventilation.
No investment can make larger returns than that expended in procuring
a well lighted foundry floor.
Lavatories and closets are located where most convenient.
SOI
502
'I'lic Moulding Room
Cranes
Unless the shop is small, or all the work light, a traveling crane is
indispensable. The capacity and span of the ciane is governe<l by the
conditions. Electric cranes are most commonly used and arc probably
tlic best for the i)uq)osc. The necessity for wall and post cranes will
1)0 indicated by the requirements of the business. Liberality in supply-
ing cranes of lifting jwwer in excess of the proljable needs is never mis-
placed. Occasions arise in every foundry which tax the cranes to their
utmost capacity. Wire cables, instead of chains, for cranes are alto-
gether preferable. Warning is always given of weakness in a cable,
whereas a link in a chain may break at any moment.
.\bundant head room is a matter of great imjjortance. Too fre-
cjuently the inability to raise a heavy weight a few inches higher than
the head room permits, occasions the greatest annoyance.
Hooks and Slings
For the strength and dimensions of hooks, see Table, page 172.
For chains, see Table, page
173-
Chains and hooks should be
frequently annealed. They
arc liable to give way at any
time and seldom give warning
of weakness. There is an
endless variety of cliains and
hooks dexised by the ingen-
uity of the moulder to meet
exigencies which continually
arise. Fig. 137 furnishes ex-
amples of those in ordinary
use.
Hooks and Chains
Figs. I, 2, 3, 4 and 5 show
heavy hooks for the crane.
No. 1 is the t\pe of heavy
^ -=;-,book for crane block.
- — >} No. 2 is an unattached
hook which is often found
very convenient.
Nos. 3, 3, 3 show different forms of change hooks. They are used in
shifting a load from one crane to another.
Fig. 137.
Lifting Beams
503
Nos. 4 and 5 "S. & C. " hooks, made very heavy, are in frequent
demand in connection with heavy lifting.
No. 6 is the form of hook usually attached to slings for lifting iron
flasks. They are made with flat or chisel points from ili to 3 inches
wide.
No. 7 is the ordinary chain hook.
No. 8 is a claw hook for shortening hitches and adjusting chain
lengths.
No. 9 represents beam slings for hoisting copes, rolling flasks, etc.
The hooks should be flat and thin,
so as to engage easily in the long
links A, A. There should be two
or more of these long links in each
chain, spaced at equal distances.
Several pairs of these slings about
every foundry where the lifting is
by cranes are most convenient.
No. 10 shows a most serviceable
sUng. It is usually fitted with grab
hooks like No. 6.
No. 1 1 is a rigid beam sling used
on flasks with trunnions. There
should be two or more pairs of
this type of sling. Another form
of trunnion sling is made of a large
strap ring to which is attached a
short chain with hook or ring for
engaging the crane chains.
No. 12 is the ordinary turn-
buckle, an invaluable implement;
of which there should be several pairs of varying strength.
Fig. 138.
Lifting Beams
No. 13 shows a light forged beam, or spreader. This is most con-
venient especially for light work.
The usual lifting beam is made of cast iron with notches for slings.
While such a beam is very serviceable, it is too heavy to handle for
moderate weights and unsafe for heavy loads.
No. 14 shows a beam made of oak reinforced with iron straps.
Such a beam is light and may be used for moderately heavy
loads.
S04
The Moulding Room
Fig. 139.
No. 15 for licavy loads.
The fjeam should be made
of steel I beams, or chan-
neb, and to carrj' any load
to the full capacity of the
crane.
Where very large and
heavy cojjcs are to be lifted,
the beam is frequently made
in the form of a cross, so
that attachment can be made
in four or more places, dis-
tributing the strain on the
cope as desired.
The following table gives
the dimensions of I beams
and loads they may safely
carry. The tabic is calcu-
lated for an extreme fibre
stress of 12,000 pounds per
square inch.
Safe Loads for Lifting Beams
Safe load for
Depth of
Weight
Area of
Width of
extreme fibre
between
slings
I
beam,
per
foot.
section,
square
Thickness
of web
flange.
stress of
12,000 pounds
inches
pounds
inches
per square
inch, pounds
8
6
16
4.7
.26
363
4.772
10
6
16
4.7
.26
3.63
3.818
8
8
22
6.S
.27
4.S
8.983
10
8
22
6.S
.27
4S
7.18s
10
10
33
9-7
.37
5.0
I2.goo
12
10
33
9-7
.37
SO
I0.7S0
10
12
40
II. 7
.39
S.SO
I8.7S3
13
12
40
II. 7
.39
S-SO
IS.627
14
IS
80
23.S
.77
6.41
29.937
16
IS
80
23. S
.77
6.41
26,aoo
16
20
80
23. S
.60
7.00
36.22s
18
20
80
23. S
.60
7.00
32.200
18
24
80
23. S
•SO
6.9s
38.136
20
24
80
23. S
.SO
6.9S
34.323
Binder Bars
S05
No. 16 shows a cross with detachable arms. This is frequently used
for large copes or rings, where the points of attachment must be dis-
tributed equally. It does not answer for very great weights. Crosses
with shorter arms cast in one piece are often of great service.
The foundry supplies itself with such appliances as occasion requires.
n
Fig. 140.
Binder Bars
Binder bars are usually made of cast iron, except for very heavy work,
when steel beams are used. The binders are ordinarily made in open
sand with the ends slotted for bolts. For heavy work holes are made
in the ends instead of slots.
.. ■- upper Rib for Heavy Sars
Fig. 141.
The binders are held by bolts to similar bars under the bottom board
of flask, or are fastened to anchors in the floor. For safe loads on steel
I beams employed as binders, multiply the loads given in the table
on page 504.
Binder bars for supporting sides of flasks are of same character as
those for holding down copes, except that they are shorter and not as
heavy.
5o6
The Moulding Room
Clamps
There arc many types of clamps on the market. Adjustable, steel
and malleable iron, but it is extremely doubtful if anything has lx^cn
found to take the place of the common, old fashioned, cast-iron cUimp
and wooden wedge.
A large assortment of the sizes in ordinar>' u.sc should l>e kept on
hand. Where vcr>' long ones are required D wrought iron bars arc
bent to shape. It is the better practice, howe\er, to use binders in
place of exceedingly long clamps.
^
i7 ^
Fig. 142. Fig. 145.
Iron flasks are frequently held together by short clamps on tie flanges.
Flasks
The wood flask has been used for ages and has served its purpose
most admirably. Wood, however, is becoming so ex-pensive that the
iron or steel flask is rapidly superseding it.
Cast-iron flasks arc so durable and so easily made, that an assortment
covering the ordinary range of work is almost indispensable.
The ordinary wooden flask is nothing more than a plain box. For
light work it is made of 2-inch plank, of width and other dimensions to
suit the requirements.
Fig. 144 shows the ordinar}- wood
flask for light work; the ends are
gained into the sides ]n inch and
spiked. The upper part is called
the cope and the bottom the nowel
or drag. The depth of these parts
depends entirely on the pattern.
It is essential that the joint at
"A" should be a plane surface.
or as the workmen say, "out of
wind. "
Fig. 144. £.j(,], f\^^ jg provided with a
bottom board B. This is made of boards one inch thick, nailed to
battens.
The limit for copes made with no support for the sand except that of
Nowel oFDrscj^^^ I [
fmmmW}w/////////W^77m7m
<k
2>
Flasks
507
the wood sides is about 20 X 20 depending largely upon the character
of the moulding sand.
For larger flask-bars, boards iV4 inch thick are placed crosswise
of the cope and about 6 or 8 inches apart. The cope is also strengthened
by rods at the end .r running from side to side. The rods should have
large washers under the nuts. There should be one or more rods at
each. end depending upon the depth of the cope. The lower edges of
the bars are chamfered to sharp edges, and the edges are kept from
?4 to I inch away from the pattern, the bars having been cut to con-
form to the general shape of the pattern. Where the distance between
the edges of the bars and the surface of the pattern is more than ?4 inch,
nails are driven slantwise into the bars so that their heads may come
within three-quarters inch of pattern.
The cope is coated with thick clay wash before placing it in position
to receive the sand. The ordinary medium-sized wood cope is gener-
ally made as shown in sketch below.
(t
^ui
-M^
<
■^^
-•^^
°)
Fig. 145.
H^l
^
The short bars A, A are used where the copes are over 24 inches
wide.
The following table showing the thickness of plank desirable for
flasks of different dimensions is copied from the Transactions of the
American Foundrymen's Association. The table is based on a depth
of 6 inches for copes and drags. For each additional depth of 6 inches,
the thickness should be increased 25 per cent.
5o8
'I'hc Moulding Rckjiti
Square flasks.
Sides,
Bars.
inches
inches
inches
34 and under
jH
I
24-36
2
1^4
36-48
24
ll-i
48-60
3
l''i
Rectangular flasks
18x48
3
I
18x60
2
I
18x72
2]^
I
18x84
2]ri
I
24X48
2
iH
24x60
2
iM
24x72
2!^
1K4
24x84
2M
iW
36x48
2\<i
l'/4
36x60
2\h
m
36x72
2\<i
m
36X84
2H
iW
48x48
3
i!.^
48x60
3
1 4
48X72
3
li-i
48X84
3
iW
Bars should nol be o\er 8 inches apart, center to center.
Square flasks, from 24 to 36 inches square should have one row of
short cross bars running through center of flask, connecting the long
bars that extend from side to side.
Sizes from 36 to 48 inches square should have at least one cast-iron
bar, preferably two, and should also have one row of short cross bars.
Sizes from 48 to 60 inches square should have two iron bars and two
rows of short cross bars.
With rectangular flasks, the statement that connecting bars are not
needed until the flasks are 36 inches wide does not accord with the
usual practice. Ordinarily connecting bars are used in flasks over
18 inches wide.
Rectangular flasks over 60 inches wide should have one cast bar
crosswise in the center. Flasks over 48 inches wide should have two
rows of cross bars and two cast bars at equal distances from the end of
the flask.
.\11 copes should have a 'i-inch bolt ruiminu from side to side at each
end. and where the cope is longer tlian three feet it should have a bolt
in the center. Where copes are over 6 feet long, the bolts should be
Flasks
50Q
spaced every two feet apart. All bolts should have large washers at
each end.
Drags should also have bolts at each end, but as conditions often
prevent their use in the center,
long-nosed clamps placed cross-
wise every iS to 24 inches and se-
curely wedged are recommended.
The form of flask shown above
is that most commonly used
when they are made of wood.
It is a short-lived affair, being
quickly knocked and racked out
of shape, and soon goes to the
cupola for kindling wood. Such
flasks may be greatly strength-
ened and their durability in-
creased by bolting cast-iron angles
in the corners or even reinforcing c[
the corners with blocks of wood,
well spiked to sides and ends.
^^'^ithout greatly increasing the
cost a far better flask is made
by making the ends of cast iron.
Such flasks are in common use
for making cylinders or other
Fig. 146.
castings, requiring large circular cores as per following sketch.
Flasks of similar construction
are often used for cylinders as
large as 20 inches diameter of
bore. The sides of the flask
must be made of plank from 3
to 4 inches thick depending on
the size. For rectangular flasks
made of wood and iron, the con-
struction shown below, offered
by Mr. P. R. Ramp, is excellent.
The suggestion to core the
trunnion, as at 4, is also valu-
able, as it greatly reduces the
^m^
Fig. 147.
chance of unsoundness at that point.
Flasks that are heavy enough to require trunnions should have iron
ends. The trunnions may be cast on the ends or on trunnion plates,
which are bolted to the ends.
5»o
The MouldiriK K6om
Iron Flsisks
Although the first cost is somewhat greater, iron flasks soon pay for
themselves by durability. They arc stronger, more rigid and reduce
the liabiUty to swells and run-outs.
The copes and drags of small iron flasks arc usually marJc each in
one piece. At the joints for flasks with straight sides, flanges e.\lend
all the way around the inside.
The handles may be of wrought iron cast in place, or, of cast iron, for
sizes requiring two men to lift the cope.
Some are made with sides turned
>U iL up edgewise like troughs, so that the
°~^{| [7"° greatest length and breadth will be
at the middle of the section.
These arc more expensive to mould
and present no advantages over
the flask with flat sides as shown
in fjg. 148.
Fig. 148.
Fig. 149.
An assortment of small flasks of this description, ranging from 12 X 14
to 16 X i8 is of great value to any foundr>-.
Iron flasks of medium and large sizes are best made in sections and
bolted together.
Flasks of this stjde are made and fitted up very quickly. .\ few
[)attcrns answer for a large assortment. With proper stop-ofi's, the ends
and sides can be lengthened or shortened as desired.
Where the copes are too large to be lifted off by hand, bosses are
cast on the end. These arc drilled to receive a yoke and the cope may
then be lifted by crane and turned.
If the flask is heavier than can be safely lifted with such a yoke,
trunnions may be made on the ends and heavier lifting gear emplojxd.
The requirements for hea\"y flasks are so varied that it is impossible
to specify any general type.
By making them in standard sections as much as possible, having
Iron Flasks
511
the parts interchangeable, a rectangular flask of almost any required
dimensions may be constructed. By so doing the number of flasks is
greatly reduced.
Section A-B
15
a
0 0 goolpogj 0 0
0 0 1 0 0
0 0^1^ j3 0 00 0 0 ,£1,0 0
a
1 m
a
0 o'T'o 0 0' 0 0 'H'o 0
00 00 000
0000 ooooo
9y
Fig. 150.
Care must be taken to number and store the parts systematically so
that they may be readily accessible.
It is seldom that a large flask will need to be less than 6 feet by 8 feet,
and 12 inches deep. Starting with the end pieces 6 feet X i foot, and
having four distance pieces, each i, 2, 3 and 4 feet long, ends can be
assembled 6, 8, 10, 12, 14, 16 and 18 feet long; by duplicating the parts,
the depth of cope or drag can be made any number of even feet.
Where the depth of cope or drag is over one foot, it is desirable to
break joints in lapping the sections.
It is better to have the trunnion plates loose, so that they may be
bolted to any of the 4 or 6 feet lengths.
o C
Fig. 151.
The top and bottom edges must be planed and the holes in ends and
sides drilled to templets.
Flanges top and bottom must be from $H to 4 inches wide, and the
4 and 6 feet sections drilled at the center of flanges for pins. The
si;
'I'hc MouMiiiK Room
pl:ine<I surface need only be ?« inch wide; lli:' ll.inKes should drop away
from edges from H to ^\n inch.
The ucIj of sections should be ':>> iiicii thicii and the
flanges i ' < inches.
Tlic lifting is in most cases done by attaching to
the flanges, but wiierc the weight is loo great to be
-;ifely borne by these flanges, heavy wrought-iron
loops are bolted to the sections, for points of attach-
ment.
On page gS, "American Foundr>- Practice," Mr.
West shows an admirable form of extension flask for
moderate sizes.
"The handles W, W, are of wrought iron cast into
the flask. They are placed on a slant so as to be in line with the chains
when lifting. Guides A", A' should be cast on for driving stakes along
the side. The plate Y forms the end of flask. Should it be desired to
make the flask longer, distance pieces may be bolted in between the
flask proper and the plate Y.
TI
a ! i
Fig. 152.
^
r
N» I
:>0_
.J
afJ
1
TT
X"
I.
^r
Lim
ToTy
■oi)
"Tjo
Fig. 153.
"To accomplish the same purpose, the whole flask may be cast in one
piece, and the bottom edge of Y cut out ^i of an inch so there may
be no bearing on the joints. When a longer flask is wanted a section
may be bolted to it. Tliis is not as desirable as the form shown in
sketch. "
Flasks of this style are commonly used as copes to cover bedded work.
Iron Flasks
513
Where the conditions do not warrant the extension flask as above
described special flasks are more or less in demand.
30 0 0
Jo 0 0
000
0 0
000
000
0 0
000
000
0 0
000
000
0 0
000
0 0 or
0 0 0 [_
Jo 0 0
-.00
->o 0 0
000
0 0
000
000
0 0
000
000
0 0
000
000]
0 0
0 0 0 1
0 0 o[;
0 0 ,-
0 0 oL
Jo 0 0
-,00
Jo 0 0
000
0 0
000
000
0 0
000
000
0 0
000
000
0 0
000
0 0 or
° ° r
0 0 oL
Fig. 154.
The above sketch represents an ordinary heavy flask (cope) say
6' X 12' X 3'.
In making large door frames, where the interior of the flask is not
used, or for similar work, it is customary to have the flask follow the
outline of the pattern and leave the interior vacant as shown in sketch
below. , ,
"^
T1
^3 t=^
Fig. 155.
Flasks are made in all sorts of irregular shapes both in plan and eleva-
tion, as necessitated by the patterns. The bottom plates of heavy
flasks are made of cast iron. These are fastened to the bottom flange
of the drag by short heavy clamps. Thus.
Circular flasks are in common use. They
serve as copes to wheels cast in the floor
and for other purposes. For large wheels
which are swept up, instead of sweeping out
the face in a pit, large rings are used for the
cheek. The arms and hub are made with ^^^- ^5^'
cores and interior of wheel swept up and not disturbed subsequently.
514
The Moulding Room
The check is rammed up against segments, and when hfled gives free
access to all parts for finishing.
Fig. 157
For wheels 16 to 18 feet in diameter the cheeks are commonly made
in si.\ segments, which are bolted together.
Fig. 158
Flasks made of sheet steel pressed to shape are light and convenient.
They are, however, mudi
more expensive. They are
not as durable as cast-iron
flasks, and when worn out
are of no value; whereas
with the cast flasks, noth-
ing is lost but the labor.
The cuts following from a
manufacturer's catalogue
show standard tj-pes of
light and heavy flasks.
^l.
^fil
Fig. 159.
Sterling Steel Flasks
515
Sterling Steel Flasks
The scarcity and increased cost of good flask lumber is making it
necessary for foundrymen to consider other flasks than wooden ones.
The line of steel flasks shown herewith combine strength, durability,
lightness and efficiency. They will give splendid service. They have
in many instances entirely supplanted wooden flasks, to the advantage
of the user in every instance.
Style "A" Square Ribbed Tight Flask
Sheet Steel with Malleable Trimmings
Slock Sizes
Height cope and drag, 2H, 3, ^M, 4, 4H
and 5 inches.
Length cope and drag, 12, 14, 16 and 18
inches.
Width cope and drag, 12, 14 and 16
inches.
Weight less than one-half as much as cast
flasks and practically indestructible.
A complete small square-ribbed steel flask for general work in all
foundries, made in above standard sizes, from which innumerable
combinations can be made.
Can be made in special sizes when it is required and a suflacient num-
ber ordered to warrant the extra work in manufacturing.
Fig. 160.
Style "B" Round Ribbed Tight Flask
Sheet Steel with Malleable Trimmings
Slock Sizes
Height cope or drag, 2H, 3, 3H, 4, /^H,
and 5 inches.
Diameter, 12, 14, 16, and 18 inches.
From the above dimensions many com-
binations can be made.
The illustration gives a clear idea of
round-ribbed steel flask for general cir-
cular work, when the snap flask is not
desirable.
Weighs less than half as much as a cast flask, and is unbreakable.
5i6
The Moulding Room
Stvlk "C" Square Convkx Tight Flask
Sheet Steel with M;illcai>li- Trimmings
Slock Sizes
Height cojK- ot drag, 2'i, 3, 3)4, 4, 44
and 5 inches.
Length cope or drag, 12, 14, 16 and
18 inches.
Width cojx- or drag, 12, 14 and 16
inches.
Tig. 162. Made in the above stock sizes, which
admit of countless combinations of sizes.
This flask is particularly adapted to brass, bronze, or any special
metal foundry work. It is a new departure, having conve.x sides and ends
for holding the sand. It does nice work, and while not half as heavy
as the cast flask, is much more durable.
Style "F" Channel Iron Floor Flask
Fig. 163.
Slock Sizes
Size,
inches
Depth,
inches
Cope,
inches
Drag,
inches
Price
20X24
20x28
24x30
24X36
30X36
30X42
10
10
12
12
14
14
5
S
6
6
7
7
S
5
6
6
7
7
Snap Flasks
517
This is a decided departure in flask manufacture. It is constructed
of structural channel steel with flanges to the outside, having a smooth
wall on the inside. The interior is provided with staples arranged at
intervals to permit of inserting corrugated swivel gaggers for sand
supports.
This type of flask does away \vith the flask maker entirely, as each
moulder arranges his gaggers or sand supports to suit the necessity.
An equipment of these flasks is an excellent investment.
1. They cut out the use of expensive material (lumber).
2. They practically do away with the flask maker.
3. They eliminate expense of handling flasks.
4. They will remain in foundry and save storage.
5. And the most important feature to be considered is the increased
output, better castings, less scrap, all of which will appeal directly to
the proprietor.
These floor flasks are furnished with a complete equipment of corru-
gated swivel gaggers for sand supports which the moulder arranges
easily to suit requirements.
Snap Flasks
Snap flasks are used by bench molders for light work. They must
be easily and quickly handled, although snaps are sometimes made so
large as to require two men. The flask is removed from the mould, hence
one flask serves for an entire floor.
They are usually made of cherry or mahogany; the hinges should
lock and unlock quickly and be rigid when locked. The corners are
strengthened with iron comer bands, and the cope is faced on top with
5i8
The Moulding Room
iri)n. For special work ihe joint may be made to conform with the
parting. Rectangular snap llasks 3 feet long by 14 to 16 inches wide
are not uncommon. For some classes of work round snaps are required.
In the hands of a rapid, skillful moulder the snap flask is an indispen-
sable implement for a foundry ha\ing large quantities of small work.
I'ieces weighing as much as 100 pounds may be made in the snap
nask.
The cuts herewith illustrate the construction of the different kinds
of snaps referred to.
Snap flasks of standard dimensions from 1 2 X 1 2 to 1 2 X 20 can be
purchased of most of the foundry supply houses.
Where many moulds are to be made from one pattern, a match board,
on which the patterns arc placed, and upon which the parting is made,
is practically a necessity. If these matches are not to be preser\'ed,
and are on!)' to be used for a moderate number of moulds, they are made
of moulding sand and fine sharp sand, half and half, stiffened with molasses
water, or linseed oil, and dried; but if a permanent match board is desired,
a mixture composed of one-half new moulding sand, one-half parting
sand, '10 litharge, mixed with linseed oil and thoroughly dried will serve
admirably. The match should be varnished with shellac and kept with
the pattern. Such a match board is shown in Fig. 165..
Fig. 165.
Fig. 166.
The moulds made in snap flasks must be covered with weights before
they are poured. The w-eight should be about I'i inches thick and
should cover the cope entirely.
Where the contents of the flask arc quite heavy, or where the patterns
approach the sides of the flask closely, the moulds require to be sup-
ported by boxes, as well as to be weighted. For this purpose wood
boxes of i-inch lumber are made so that the interior shall have the
same dimensions as the interior of the whole flask (cope and drag);
this is shoved down over the mould and supports it against lateral
pressure. Care must be taken that the boxes are not so small as to
shave the mould nor so large as not to support it; they should just fit all
around.
These boxes are sometimes made of cast iron. Very serviceable ones
made of sheet iron can be purchased at moderate prices.
Pins, Plates and Hinges
S19
Galvanized Iron Slip Boxes
Straight Taper
Fig. 167.
The above are undoubtedly the best slip boxes on the market. They
are more durable than wood or cast-iron boxes, are lighter and will not
break by falling. They are made either straight or tapered, of No. 22
iron with a No. 9 wire in top and bottom and creased.
In ordering, state whether straight or tapered and give the exact
size of inside of flasks.
These boxes are for light handling and will not stand careless run-outs,
as the hot iron will warp them. They are very rigid, however, and with
the ordinary one-inch margin outside of pattern there will be no run-
outs.
When ordering taper jackets, give taper or degree per foot on side, or
make sketch giving size of top and bottom, also depth of drag.
Pins, Plates and Hinges
In order that the cope of a flask, when hfted from the drag after
ramming, may be returned exactly to its original position, so that the
two parts of the mould may match perfectly, guides must be provided
which will insure correct closing.
These are frequently made of
wood, and if kept in good shape,
serve the purpose admirably.
Wooden guides are especially
advantageous for long lifts.
Fig. 1 68 shows a wood guide,
of which there should be at
least three on the flask. The
moulder must exercise care when
preparing to ram up a flask, to
see that the guides and pins are securely nailed, that there is no lateral
play and that the cope may be lifted and returned to its place with-
out sticking at the pins.
Guides of this kind, while chiefly in use on wood, are sometimes
employed on large iron flasks. In the latter case wooden blocks are
J
ioU
Fig. 168.
520
The Moulding Room
securely fastened in the potkcts between flanges, and the guides nailed
tt> the blocks.
The usual guide for the ordinary wood llask is a common cast-iron
|)late and pin.
These are continually getting loose and
furnish no end of trouble to the moulder
Fig. 170.
as well as causing many castings to be scrapped. It is the most worth-
less appliance of its kind.
A very good iron guide may be made as per sketch. (I'ig. 170.)
7:
m
m
®r,
^
u
HEAVY HIMGE
Fig. 171.
! I Such a guide may be fastened
/\] to the flask with very little
i]|| more work, and the flanges give
1 good support. An e.xccllent
pin and guide is made tri-
angular in shape.
Cast-iron flasks either have
lugs to receive the pins and
holes, or where the flanges are
wide, pin holes are put in
' ■■— . . J ^jjp^
Fig. 172. — Light Hinges. p-^^^ f^^ iro^ flasks should
be accurately turned, the sizes should be standard, and those of each
-- VB.
Pins, Plates and Hinges
521
size interchangeable. An assortment of such pins should always be
kept on hand.
Fig. 173 . — Ball and Socket Hinge,
Fig. 174. — Heavy Hinge.
Standard Iron Flask Pin No. 2
For Iron Flasks
Fig. 175.
This is a nicely turned pin, with thread chased and hexagon nut.
designed especially for cast-iron flasks.
522
Tlie Moulding Room
Sweeps
Fig. 176. '
The above sketch shows the ordinary sweep used for making large
pulleys, fly wheels, etc. A large chiss of work, circular in horizontal
section, can be made with the sweep, thereby saving largely in the
expense for patterns.
To obtain accurate work by the use of tlie sweep, the stepping .4
must be firmly placed, so that the axis of tlic spindle B shall be vertical.
The upper support D must be held rigidly, either by braces to wall of
foundry or otherwise as most convenient. The box D may be made
with a flange surrounding it from which three or four rods lead away
to any suitable anchorages. These rods are provided with tumbuckles
so that the spindle may be held rigidly in a vertical position.
£ is an adjustable collar fasloncxi in position by a set screw.
C is an iron arm carrying the wood strikes. The bearings by which
this arm is supported should be farther apart tlian the width of the
arm, so as to avoid any sagging of tlie latter.
If these bearings are split in a direction parallel to the spindle and
drawn up witli clamp screws, lost motion can be taken up at any time.
Any play in the supports for the arm, or neglect to maintain the spindle
in a vertical position, will result in a distorted casting. Sweeps are
Aiu-hors, dascors and Soldiers
533
often wnstructed with olabvirate mediauical attachinoiits for making
gears, spiral wheels, spinil cones, ele.
Sometimes the steppinirs are placed permanenll}' on concrete piers,
where there are many wheels, etc.. to be made.
The strikes arc cut in aii\' desireil shape and are used for inside or
outside sweeping. Swept moulds arc usuall\- skin dried.
Anchors, Gaggers and Soldiers
These devices arc used for sui>-
IHKting the sand where tlic ordinar\-
bars ;ire insutVicicnt or inapplicable.
Fig. 177 sJiows an anchor used
for making pulleys. It txinsists
of six cast-iron segmental plates
about in inch thick, which aa^
so placed between the arms of
the pulley as to leave a space for
s;md, -^4 inch wide, all iux)und tliem.
The upper sides of the plates are
on the parting line of the arms.
The pUues are held together by
wrought iron loops, passing over
the arms, and cast in place. All
the plates are poured at once, and
in open s;uul. "■'• '"7-
Instead of wrought-imn loops, these cX)nneclions may be made bj'
c;\st-iron loops, furnishing a much stilTer anchor.
On the under side of each plate are east one or
more long conical pn.ij\vt ions, which serve as
guides by which to replace the anchor. Each
[liate is provided with an eye bolt long enough to
reach to the joint of flask.
The interior parting is maile on center line of
« |-j arms, s;ind is rammetl on toji of the anchor ami
,. 1 ■ I — , another parting made flush with the rim upon
LT 11 U which the cope is rammed.
.Vfter the cope is removed, the saml iwering
the arms is lifted out by hooking to the eye biilts
in anchor.
Fig. 17S shows an anchor for lifting out a
ir=
Fig. 17S.
deep pocket.
524 The Moulding Room
W'luTc the aiuliur cannot rest on ll>c bottom, IjuI must permit iron
to run under it, il is boiled to ihc cope and lifted out with it.
The necessities of the situation indicate the size and shape ot anchors.
!■ requentiy, the ixjcket is such that the anchor must be broken to remove
it from the casting. It is well to keejj down the weight of the anchors
as much as possible, relieving the cope to that extent.
\'er>- many cores, as well as moulds, require to be supported in this
manner.
Gaggers
Tn the use of gaggers it should be borne in mind, that they are heavier
than the sand; it is simply due to the cohesion of the sand, holding
Uiem up to the sides of the flask or bars, that they are of assistance in
supporting' the cope. The gagger is of use just in proportion to the
length that is surrounded with packed sand. All that part which pro-
jects above the cope is a detriment. They are first immersed in thick
clay wash, and placed flat up against the bars or sides of flask, having
about /» inch sand under them. They are made in the gagger mould,
already described, which is kept near the cupola. Costing practically
nothing, thcj' may be used freely. A good supply should always be
kept on hand.
Many shops use gaggers made of '^2 inch square bar iron bent to
shape. They are not as serviceable, however, as they do not ofTer as
good a surface to which the sand can adhere, and are more expensive.
Soldiers
Soldiers are simi)Iy jiicccs of wood about one inch square, cut from
boards, with clay washed and placed around the mould instead of gag-
gers, where the latter cannot be used; or to assist the gaggers in deep
lifts. The sand adheres to soldiers better than to gaggers.
The free use of either gaggers or soldiers is to be encouraged, as it
is better to place too many of them in a mould than to have a drop. At
the same time care must be exercised to have the ends well protected
by sand, so that the hot iron will not come in contact witli them, as
there will surely be a "blow" in that event.
Sprues, Risers and Gates
The following tables, giving the equivalent areas of round gates, also
of square and rectangular gates as compared with round ones, are taken
from West's "Moulder's Text Book," pp. 245 and 246.
Table of Equivalent Areas of Gates
525
Table of Equivalent Areas of Round Gates
One iJ'i inch is equal in area to two il
lU
2H
2^ "
2H
3
3K. ". "
3^ " "
3^4 "
4
4V4 " "
4H " "
4% « -
5
fe, three
J^,
or four
j4-inch gate
iM
I
" %
I J 16
I?'16
" 1
iJi
lVi6
" i^
i?4
1^6
" iH
115/16
1^4
" i^
2 '4
1%
" iH
2^16
1^/6
" iH
2^
2
" iM
2IH6
2?16
" iJi
2' Me
2^/16
" 2
3
2^15
" 2%
3?i6
2?^
" 2K
3?8
2 54
" 2?^
3?i6
25i
" 2H
Note. " The fractional parts of an inch as seen by the table are not carried out any
further than He, for the reason that the subject does not call for any closer figiu-es.
Therefore, the figures given will be understood as being ' nearly ' equal in area.
As given, the sizes can be readily discerned, and are also applicable to measurements
by the shop pocket rules commonly used."
Table of Equivalent Areas in Square and Rectangular
Gates to That of Round Gates
(See note above)
Round
Square
gates
Rectangular
Rectangular
Rectangular
Rectangular
gates,
gates
gates
gates
gates
inches
I inch thick
iH inch thick
2 inches thick
2],i ins. thick
I
iH
m
1^6
I?i6
I?4
2
2?'i6
iH
m
IX 2%
IX 3!'^
IX 4
IX s
2
I'/iX 2M6
I'/iX 2iMc
i5^X 3Ms
2'/4
2H
2%
2^18
IX 6
I'/iX 4
2x3
3
2IH6
IX 7H6
i!^x 4?4
2X39i8
3'/4
2ji
IX &V16
Ij-^X S'/^
2X4?i6
21-6X3946
3H
3'/i
IX 9^
IJ^X 6^8
2X456
2iiX3'/i
3%
3M6
iXilMe
iJ-iX 1%
2X5!^ i2
2i^X4M«
4
3? 16
IXI29'{6
iHX 89^
2X61/4
21-^X5
4H
3?4
IXI4?^6
iV^x 9'/^
2X7'/^
2^X556
4H
4
iXiS'Me
ii/iXio5i
2X8
2!.iix69i
4%
4^8
IXI7?4
iJ^Xll'Ms
2X8^8
2KiX7!4
S
4^8
IX19H
1HX13H6
2x91946
2i.iX7ji
"The term 'equivalent' used does not imply that two or more small gates having
a combined area equal to one large gate, all having like 'head pressure,' will deliver
the same amount of metal per second."
526
The Moulding Room
"The flow of metal is retarded by friction in proportion to the surface
area with whicli it comes in contact. Now although four 2^i-inch round
gates are of ecjuai area to one 5-inch round gate, we find the frictional
resistance to tiie flow of a Hke 'head pressure' through four 2!i-inclf
round gates to be douljle that generated in one 5-inch round gate,
simply because the comiiined circumferences of four 2J'i-inch round gates
are 31.416 inches, whereas the circumference of one 5-inch round gate is
15.708 inches. As gates are generally combined under varying compli-
cated conditions, the tables as given can be better practically used than
where they arc lumbered with the question of frictional resistance."
Risers are generally double the diameter of the pKJuring sprue. The
function of the riser is twofold. It
serves to catch and carry away any
dirt entering the mould from the pour-
ing sprue and also to furnish a supply
of liquid metal to provide for shrink-
age. Risers are placed either in con-
nection with the gate, or on some part
of the mould whence the deficiency
from shrinkage can be most readily
supplied. When located on the gate
the latter is usually so cut as to impart
a whirling motion to the metal ascend-
ing the riser. The metal enters the
riser near the bottom and flows to the mould through a channel opened
above the entrance.
In the sketch A represents the pouring sprue, B is the riser, C the
gate from sprue to riser which is cut tangential to B. D is the gate
from riser to casting. The gates should be somewhat smaller in area
than the pouring sprue so that the pouring basin E may always be kept
fuU.
Top Pouring Gates
The advantage of this form of gate
for large castings is that the dirt is
kept at the top of the pouring basin,
allowing the clean iron to flow into
the mould from beneath.
The first dash of iron may carry
some dirt, but the greater portion
of it will flow with the stream over
the gates; the runner being quickly
filled, no dirt can enter subsequently if kept full
Text Books," page 129.
179.
Fig. 180.
See West's "Moulder's
Horn Gates
527
Whirl Gates
The object of the whirl gate is to impart a rotary motion to the iron
in the basin and riser B, B.
By centrifugal force the metal is kept in contact with the exterior
of the riser, and the dirt is carried up in the middle of it.
. c-^ C .
Fig. 181.
The riser B should be larger than the pouring sprue A , and A should
be larger than C, in order that the pouring basin may be kept full.
It is best to have patterns made for whirl gates; they can be used in
either cope or drag.
The "Cross" Skim Gate
This as shown in Fig. 182 is an excellent device and is largely
used.
A is the gate leading from pouring sprue to
basin B, C is a core in which is the gate D,
leading to casting. The iron enters B, tangen-
tially, a whirling motion is imparted to it carry-
ing the dirt to the riser,
while the clean iron flows
out through D.
Another form of same gate is made as shown
in fig. 183.
It differs from the first form simply in having
a flat core E placed across the gate D, instead
Fig. 182.
Fig. 183.
of forming a part of it
Horn Gates
These are principally used for bottom
pouring, leading from the parting of
flask to the casting below.
They are made smaller at the point
joining the casting to permit of easy
removal and to choke the stream of metal.
Fig. 184.
The Moulding Room
Pouring liasins have 'rcqucntly skimming
corc^ f)laccd between the basin and the down
sprue to iiold the dirt in basin. A pattern is
usually made for them.
Strainers and Spindles
Fig. 185. Thin perforated plates from 'm to h^ inch
thick, and wide enough to cover the entrance to pouring gate arc fre-
quently placed in the runner
basin over the gate. When the
iron strikes the strainer it is held
back until the latter is melted
allowing the basin to fill partly,
raising the dirt to the surface
and furnishing clean iron to the
gate
purpose.
Weights
For medium castings, weighting the copes will be found more con-
venient than the use of binding bars. There should be about every
foundry a large assortment of weights depending on the class of work.
Weights to be handled by the crane will be found more convenient, if
made square in cross section and of whatever length desired. Holes
are cast in the ends into which bars are inserted for lifting. Weights
made in this way are more readily piled than if pro\ided with eye bolts.
Chaplets
Chaplets are properly anchors, and should come under that heading.
They are used mostly for securing cores in place in moulds. E.xcept for
special requirements the foundryman can procure chaplets from the
supply houses far cheaper than he can make them. Cuts and sizes of
the various chaplets in use are given below.
The Peerless Perforated Chaplet
Fig. 186. Spindle gate
Spindle gates consisting of many small gates serve the same
Fig. 187.
Liquid Pressure on Moulds 529
Manufacturers of all classes of castings requiring small cores will
readil}' observe the advantage in using a chaplet, such as is illustrated
above.
Made from perforated tin-plated sheet metal, insuring perfect ven-
tilation of the chaplet, eliminating all possibilities of blow holes, air
pockets, chills, etc., forming a perfect union with the molten metal,
thereby insuring an absolute pressure tight joint; something not ob-
tained with any. other chaplet on thin work. Through its use, not only
are time and labor of the workman saved in adjusting the cores to the
matrix of the mould, particularly on water backs or fronts, radiators, gas
burners, pipe fittings, gas and gasoline engine work, and similar castings,
but it also greatly lessens the liability of flaws, defects and consequent
losses in castings, such as commonly result from the ordinary chaplets
or anchors now in use.
Liquid Pressure on Moulds
The pressure of the Hquid metal at any point of the mould is deter-
mined by multiplying the distance in inches from that point to the top
of the metal in pouring basin by .26 pounds. The product is the pressure
in pounds per square inch.
To overcome this pressure laterally, reliance is placed on the rigidity
of the flask, supported, if necessary, in deep castings by binding bars.
The binding bars are of same character as those already described for
holding down copes. They are tied across top and bottom of flask by
rods, or otherwise.
The static pressure on the cope is ascertained by multiplying the area
of the casting in square inches, at the joint of the flask by the height
in inches from the joint of the flask to level of iron in pouring basin
and by .26 pounds.
In addition to this there is the pressure due to resistance in overcoming
the velocity of the rising iron, which pressure is measured by one-half
the product of the weight of the rising iron by the square of the velocity.
While this pressure may be accurately calculated with suflacient data,
it is usually difiicult to get them, and the results are, therefore, only
approximate.
However, when the mould is nearly full, the pouring is slackened as
much as possible without letting the dirt into the sprue, thereby reduc-
ing the head and velocity, and greatly lessening the shock as the iron
reaches the cope.
The formulae given for determining holding down weights for copes
are empirical. The moulder will not be led astray by calculating the
lifting area of the mould in square inches, multiplying this by the head
530
The Moulding Room
measured to pouring basin, in inches, and this product by .26 pounds.
.\(ld .;o per cent to the result, this will make ample provision for the
lift due to the blow of the rising iron.
The Peerless Perforated Chaplet
The following list will give an idea of the approximate number of the
various sized chaplets required to make a pound.
Length
Brciidth
Thickness
No. to the
%
poun^i
y*
W
;.<,
W
H
1400
h
^4
H
1200
'4
H
9i8
1 100
y*
?4
^U
600
I
I
y*
300
94
V*
V*
2SO
I
I
%
130
I
I
H
100
iH
l'/4
H
80
I
I
Vz
90
iH
I" 4
H
80
I
I
■)4
45
2V*
I
I
35
I
I
1
40
I'/l
lU
I
30
Over two thousand difTerent shapes, sizes and styles of these chaplets
are made. Many hundred standard sizes and shapes are kept in stock.
The prices depend upon the sizes and number required to make a
pound.
The Peerless Perfor.vted Chaplet. — {Continued)
(Net prices per pound.)
No. to the
Price per
No. to the
Price per
pound
pound
pound
pound
20- .(0
1
So 35
200- 250
So. 8s
40- 50
.35
250- .}oo
90
So- 60
.40
300- 3SO
95
60- 70
.45
350- 400
00
70- 80
■ SO
400- soo
05
3o- 90
.55
500- 600
10
90-100
.60
600- 700
15
100-125
.65
700- 800
20
125-150
.70 I
800- 900
25
ISO-I75
.75
900-1000
30
I7S-200
.80
lOOO-IIOO
35
Chaplets
531
Double Head Chaplet Stems
Plain or Tinned
• Made of ?i-inch round iron, 5^ to ili inches long (measur-
ing from face to shoulder).
Price per hundred, from H to i5s inches ... $4.00
Price per hundred, from iH to 2^6 inches. . . 5.00
Fig. iSS.
Fig. 189.
Double Head Chaplets with Forged Heads
Plain or Tinned
Made of ?s-inch round iron, from H to 2H inches long,
with head above Ji-inch diameter.
Price per hundred, from H to 1% inches. . $5 .00
Price per hundred, from il'^ to 2^^ inches. 6.00
With Square or Round Plates Fitted
Plain or Tinned
Fig. 190.
Square plates always furnished unless otherwise ordered.
Stems made of Me inch round iron from ?^ to i!'^ inches long.
Price per hundred, ?6 to % inch with plates any size $4 . 00
Price per hundred, ¥i to i inch with plates any size 4.50
Price per hundred, iH to iH inch with plates any size. . . 5 .00
Stems made from H-inch round iron from H to 2H inches long.
Price per hundred, H to i inch with plate any size $6
Price per hundred, i to i)'^ inches with plate any size. . .
Price per hundred, iJ^ to 2 inches with plate any size.. . .
Price per hundred, 2 to 2 J^^ inches with plate any size. . . .
532
I'lic Moulding Room
Price List ok Doui'le Head Ciiaplet Stems
(Plain or tinned with sriuare plates fitted, heavy «tfm and plate.)
Diameter
Diameter
of stem
Length
I'er loo
of stem
Length
Pm- 100
W
?H
$8.oo
«
H
Sio.oo
H
I
8. CO ■
^4
I
10.00
Vi
iW
9.00
(
iH
11.00
Vi
\\<l
10.00
'1
iW
12.00
»
IW
11.00
?4
i94
13.00
W
3
12.00
94
2
14.00
W
2W
13 -oo
94
^V^
15.00
\'i
2'/4
14.00
?4
aVi
16.00
Vi
2?4
15-00
?4
294
17.00
H
3
16.00
%
3
18.00
H
3M
17.00
94
3W
19.00
yi
3^4
18.00
94
34
ao.oo
w
3y4
19.00
94
33.
31 .00
H
4
20.00
94
4
32.00
w
4H
21.00
V<
4M
33.00
H
4^^
22.00
94
44
24.00
\i
4«
23.00
94
4^4
35.00
Vi
S
24.00
94
S
36.00
96
-A
9.00
Ti
J6
11.00
%
I
9.00
1%
I
11.00
96
iH
10.00 1
^/6
iH
13. 00
H
1^2
11.00 1
T6
1 4
13.00
H
154
12.00
^/6
i94
14 00
%
2
13.00
'/ft
3
15.00
96
2!4
14.00
?6
2I.4
16.00
96
2^
IS 00
'/6
24
17.00
96
2^
16.00
'/6
294
18.00
96
3
17.00
"•6
3
19.00
96
3H
18.00
'/6
3^4
30. 00
96
3V6
19.00
'/6
34
31 .00
96
3^4
20.00
?6
3?4
23.00
96
4
21.00
'/6
4
33.00
96
4W
22.00
?6
4M
34.00
96
4H
23.00
li.
44
- 35.00
96
4?4
24.00
?6
494
36.00
96
S
25.00
J6
5
37.00
Wrought-Iron Chaplet Stems
533
Wrought-Iron Chaplet Stems with Square or
Round Plates Fitted
Plain or Tinned
Fig. 191.
Square plates always furnished unless otherwise specified.
Prke per Hundred
Diameter of plates .
Thickness of plates
Diameter of stem. .
iVi ins.
Me in.
Vi in.
lYi ins.
lii in.
Vie in.
Vi ms.
H ins.
H in.
2 ins.
Hi in.
H in.
2]^ ins.
yte in.
58 in.
31ns.
H in.
?4 in.
Length, inches
3
3H
4
454
5
SH
6
6H
7
754
8
9
10
11
12
Net prices for curv-
ing plates to suit
diameter of core
$3- 10
3. IS
3-20
3-25
330
3.35
340
3.45
350
3 55
360
3-70
3.80
3.90
4.00
.35
$5. 10
5.15
5.20
5.25
530
5.35
S.40
5.4s
5. SO
5SS
5.60
S.70
S.80
5. 90
6.00
.SO
$6.70
6.80
6.90
7.00
7.10
7.20
7.30
7.40
7-50
7.60
7.70
7.90
8.10
8.30
8.50
.60
S11.30
11.45
11.60
11.75
11.90
12.05
12.20
12.35
12.50
12.65
12.80
13.10
13.40
13.70
14.00
■ 75
S20.00
20.25
20.50
20.75
21.00
21.25
21.50
21.75
22.00
22.25
22.50
23.00
23. SO
24.00
24.50
• 90
$31.25
31.62
32.00
32.37
32.7s
33.12
33. SO
33.87
34 25
34.62
35.00
35. 75
36.50
37.25
38.00
1. 25
534
The MouldiriK Room
Wrought Iron Chaplet Sterna
Plain nr liiiiu-d
Length,
measuririK from
face to stem,
inches
3
3W
4
5
6
6W
7
8
9
10
Fig. lyz.
Price per Hundred
$2.40
2.4S
2.50
2.SS
2.60
2.6s
2.70
2.75
2.80
2.8s
2.90
2.9s
3 00
3 03
3.10
DvamclKi
J3.6S
Vi
i
$4.50
% 8.2s
S13-00
3.70
4.60
8 ..40
13 25
3. 75
4.70
8.55
13. SO
3.80
4.80
8.70
13. 75
3.8s
4.90
8.85
14.00
3.90
5.00
9.00
14.2s
3. 95
S.io
9 15
14. SO
4.00
S 20
930
14. 75
4.0s
S.30
«.4S
1500
4.10
5 40
9.60
15.25
4.20
5. so
9 85
15.50
4.2s
5-70
10.20
16.00
4.30
s 90
10. 55
16.50
4. 35
6.10
10.90
17.00
4.40
6.30
11.25
17 SO
$19 20
19.60
20.00
20 35
ao.8s
21. ao
21.60
21 95
22 30
22.6s
23.00
23.75
24 so
25 2S
26.00
Gray Iron Chaplets
Fig. 193.
Length, inches. . . M H ^4 H H H i
Per hundred. .. . So. 72 $0.78 $0.84 $0.90 Si. 00 $1.10 $1.20
Length, inches. . . i!4 iH 1% iM i?i 2
Per hundred ... . Si. 40 Si.rio Si . 70 Si. So Sj 20 $3.cx3
Double Head Water Back Chaplets
Made of ^n-inch round iron, from '1 to j'.' inches long,
with heads about ""^ inch in diameter.
Price per hundred, from \* to i-^v inches. . . . $5 00
Price per hundred, from iH to 2yi inches. . . 6.00
Fig. 194.
Radiator Chaplets
535
Wrought-Iron Chaplets with Forged Heads
Plain or Tinned
Fig. 195.
Price per Himdred
Diameter of head. .
and i?46
iH
iM
Diameter of stem.
M, Ms
and \i
Length, inches
3
3^
4
4)^
5
SH
6
6'/^
7
vVi
8
9
10
11
12
Net price for point
ing
?2.4o
2.45
2.50
2.55
2.60
2.6s
2.70
2.75
2.80
2.8s
2.90
2.95
3 00
30s
3.10
.40
$3-65
3-70
3-75
3.80
3.8s
3-90
3-95
4.00
4.05
4.10
4.20
• 4.2s
430
4-35
4.40
.60
$4.50
4.60
4.70
4.80
4.90
500
5. 10
S.20
5.30
5.40
5. 50
S.70
S.90
6.10
6.30
.75
$ 8.25
8.40
8.55
8.70
8.85
9.00
9.15
9.30
9-45
9.60
9.8s
10.20
10.55
10.90
II. 25
$13.00
13.2s
13.50
13.75
14.00
14.25
14 50
14.75
15.00
15.25
15.50
16.00
16.50
17.00
17-50
I. 25
$19.20
19.60
20.00
20.35
20.85
21.20
21.60
21.95
22.30
22.6s
23.00
23.7s
24.50
25.25
26.00
1.50
Single Head Water Back Chaplets
Head \^ inch, stem ?i6 inch, length to order. For' price
list see Wrought-iron Chaplets with Forged Heads.
Fig. 196.
E
or
Fig. 197.
Radiator Chaplets
Head ?4 x V*, stem and length to order.
Special chaplets and plates made to order.
536
The Moulding Room
Round and Square Head Chaplets
*\ ] StcrTLs made of 'K-incli round iron, from ^s to i"i inches
" , I Plates '-J inch round and ?< inch square. ^U,H, H, H, H, Jt
Fig. 198. ^"^ ' '"'^'^ '""K-
Price per hundred, all sizes $3 00
Tinned Clout Nails
i;^
Fig. 199.
An indispensable article in the foundry. Do not rust like the ordinary
black cut nail. Shipped in 100-pound kegs. All lengths from H inch to
2 inches, inclusive.
List Prices
Inches Per jx
}und
3-8 $0
70
3)^-8
60
1-2
SO
4\i-9
45
5-8
43
5^2-8
41
3-4
40
6\i-9
39
7-8
38
I and longer
36
Pressed Tin Shell Chaplets
For certain classes of work these chaplets are inval-
uable. They form perfect union with the cast metal.
Sizes ^i inch to H inch inclusive are made in both
two and three prongs, 'Mb inch to i inch inclusive
are three prong only.
Fig. 200
Sprue Cutters
Price List
537
Size,
inches
Two prong,
per thousand
Three prong,
per thousand
Ms
%
iMa
I
$300
3.00
3.20
350
3-50
4.00
4.00
4SO
$3.50
3.50
3-70
4.00
4.00
4.50
4-So
5.00
S.oo
S.oo
S.oo
5.2s
5.25
5.25
Steel Sprue Cutters
These sprue cutters are all 6 inches in length.
They are made of steel and in four sizes, viz.:
No. I. — Yi inch at bottom, % inch at top.
No. 2. — 5s inch at bottom, i inch at top.
No. 3. — y* inch at bottom, 1% inches at top.
No. 4. — Ji inch at bottom, i54 inches at top.
Price 50 cents each
Brass Sprue Cutter
"i Made in one size only.
K-inch diameter, 10 inches long ... $4 . 80 per dozen
Fig. 202.
CHAPTER XXIII
MOULDING MACHINES
The moiildinR machine has become of such importance that no foundry
can aCford to be without it. The reduction of cost in the production
of the classes of work for which it is adapted and the superiority of the
product as compared with hand work render the machine absolutely
indispensable to the successful conduct of a foundry engaged in com-
petitive work.
While the moulding machine is in some respects invaluable, it must
not be supposed that its value can be realized without the exercise of a
high order of intelligence.
To produce accurate work by machine requires the utmost care and
accuracy in fitting up patterns and flasks. Appliances which may be
used successfully in hand moulding would entail disastrous results in
machine moulding. Again, no particular machine is adapted to all
kinds of work. It has a certain range for a certain character of pro-
duction. Without those limits its use is not warranted.
There are many kinds of machines, operated in various ways; by
compressed air, hydraulic pressure, mechanical pressure, gravity and
impact.
It is not the purpose of this book to discuss the merits of the different
machines. The various tj-pes have been in service long enough to
indicate the particular class of work to which each is best adapted.
One type of machine is best suited for light, small work; another to
stove-plate; another to car castings, etc.
In choice of machines the foundryman should profit by the experi-
ence of those who have preceded him in this field, and must be especially
cautious in not attempting to extend the range of any one tj-pe beyond
that for which it is i)articulariy fitted.
There are machines which simjily perform the operation of ramming;
others which only draw the pattern, the ramming having been done
by hand; while others perform both operations. In many instances
the character of the work determines the function of the machine.
It is doubtful, however, if hand ramming for deep pockets, etc., can
be dispensed with by use of the machine. In fact, except in cases where
the plainest character of work is produced, it is a mistake to believe
53S
Moulding Machines 539
that the moulding machine does not require the services of an experienced
moulder.
Mr. S. H. Stupakoff, in his compreliensive paper on the moulding
machine, referring to the object of the machine as one to save labor, to
increase the output, to decrease cost of production, to produce uniform
and better castings, etc., says:
"It is obvious that it would require a complicated mechanism to per-
form successively and successfully all the necessary operations to make
a complete mould, even if it were only the mould of a simple pattern.
In consequence the general equipment of a foundry which accom-
plishes this object must be necessarily quite an elaborate and expensive
matter. The majorit}^ of designs of moulding machines run in this
direction, whereas in most cases it would have been better if the energy
expended had been directed to their simplification.
"Such tendencies lead to complications which are altogether imsuited
for foundry practice; they meet with little favor and machines built
upon these principles are of short life. "
"Only the simpler moulding machines have a chance of meeting with
more or less success, even if they perform but a few operations, provid-
ing they perform these well. "
"The first step in the evolution of the moulding machine was a device
for withdrawing patterns from the sand. The next was to employ
stripping plates, then an attempt to ram the mould by machiner>^"
In these three operations lie the basic principles of all moulding ma-
chines: all subsequent improvements and additions have been matters
of detail; but to these improvements and to superior workmanship is due
the real success of the modern moulding machine.
In the chart (p. 549), given by Mr. Stupakofif, moulding machines
are divided into two classes — hand and power machines. The chart
gives the variations of each class.
The selection and arrangement of machines, etc., is a matter governed
entirely by the specific circumstances. Only hand machines are portable.
They effect a great saving in the cost of carrying sand, but their use
is limited by their size and weight. Mr. Stupakofif discusses the advan-
tages and use of pattern plates as follows:
"At first sight it may appear that the construction and manipulation
of pattern plates has but little connection with moulding machines, but
I hope that I will succeed in showing in the course of this work, that
they are not only intimately cormected with each other, but that they
are in fact the principal parts of all moulding machines. The lack of
intimate knowledge of how to make use of them to the best advantage,
the want of proper means to efifect this purpose and the wretchedly
vio MouldinK Machines
little effort which is made to calrh the right spirit of their nature, is
gtru-nilly the reason why a moulding machine jjccomes an elephant on
the hands of the moulder and an eyesore to its owner."
The recommendations given by Mr. Stupakoff for the adoption of
plate moulding by hand apply equally well to machine moulding.
1. Plated patterns give the best ser\ice when used continuously.
2. Castings which are to be produced in quantities are perferably
moulded with plated patterns.
3. Standard patterns are preferably plated for economic production
in the foundrj'.
4. Plated patterns should be made of metal to give good scr\-ice."
5. When plated patterns are used good flasks only will insure good
castings.
6. .Vccurate workmanship is one of the main requisites in plated
patterns.
7. The use of wood patterns on plates is not excluded.
8. AH patterns when placed on plates should be provided with
plenty of draft.
9. Plated metal patterns are preferably made hollow.
10. Rapping is destructive of plates and patterns."
The chapter on jigs is regarded of such importance that it is given
here in full.
The Moulding Machine
By S. H. Stupakoff, Pittsburgh, Pa.
Journal of llie American Foundrymcn's Association, Vol. XI, June, igo2. Part 1.
Jigs
The deduction arrived at in the foregoing chapter might make it
appear that plated patterns are not likely to find extensive use in
jobbing foundries, whereas this is really not altogether the case. There
is no doubt that plate moulding as now practiced, or rather as ordi-
narily applied, is practically excluded from jobbing shops. But, if a
plate is used in connection with a suitable jig, specially' prepared for the
purjjose, objections are not only overcome, but the application and use
of plates offer excellent advantages, even in such cases where only a
small number of castings of the same pattern are required at one time.
At best, the economic use of plated patterns is limited by the shape anrl
size of the castings. The fundamental principle involved in their
construction and application must be fully understood by the user,
if satisfactory results are expected.
Jigs
541
Irrespective of its relation to the moulding machine, it would seem that
this subject — on its own merits — is of such importance, that it should
be investigated by all fouiadrymen. It should specially interest the ma-
jority of our members. I have therefore somewhat enlarged the scope
of this treatise on the moulding machine by including a detailed study
of the construction and modus operandi of this particular contrivance.
To begin with, it should be understood that all plates are provided
with guide-pin holes, which are accurately fitted to corresponding guide
pins forming part of the flasks. Unless special flasks are used in con-
nection with such plates the customary flask pins should not be con-
founded with these guide pins, as they will never answer the purpose.
In order that misconceptions in this respect may be avoided, this term
will be adhered to in what follows, and strict distinction will be made
between flask pins and guide pins wher-
aver they may be mentioned in the
course of this work.
The guide-pin holes, G and G' , Fig.
205, are preferably arranged on opposite
ends of the plate, in even multiples of an
inch, and equidistant from its center and
on a line dividing the plate into two
equal rectangles. There are exceptional
cases, in which three or four guide pins
must be used. The most serious objec- ^*^ ^°^'
tion against this arrangement is the greater difiaculty experienced in
locating the patterns correctly.
Accuracy in preparing the plates becomes of the utmost importance,
as the magnitude of all errors occurring in the original laying out is
doubled by each subsequent operation. The guide-pin holes should be
drilled and reamed out at right angles to the surface of the plate, and it is
advisable to provide them with hardened and ground steel bushings.
All guide pins should be of uniform diameter irrespective of
the size of the plate. A pair of test pins should be kept on
hand, which snugly fit the guide-pin holes; one-half of one of
their ends should have been cut down to about Vi inch in
length, leaving as remainder exactly one-half of the cylindrical
portion (Fig. 204). If these test pins are inserted into their
respective holes and a straight edge is placed against their
„ flattened faces, it will serve for locating the base or the cen-
A* IP 2 O A
ter line of the plate, for marking off and laying out the dowel
pin holes, arranging the patterns and checking off all work relating
to it.
542
Moulding Machines
The exact location of the center of the plate, and likewise the center of
the llask, is found by dividing the base line from center to center guide-
pin hole into two equal parts. Let us drill a hole C in this place (Fig.
205), and let this hole serve as the starling jjoint for future oiHirations.
Now we will assume that we have procured a tri-squarc with a row of
holes drilled in each of its legs; these holes are spaced equally — say
Fig. 205.
I inch apart — care being taken that each row stand.s exactly in a
straight line, and that both rows include an exact angle of 90 degrees.
We place this square in such a manner on our plate that the hole in its
apex corresponds with the center hole C of our plate, and insert a good
fitting dowel pin through both. Thus we arc able to shift the square
over the whole surface of the plate by turning it around the center pin.
Next we bring one leg of the square over the base line of the plate and
insert a second dowel pin (which may be shouldered if necessar>-) through
G into the corresponding hole of our .square. Secured in this manner
the square sliould be absolutely rigid and .should not shake to right or
left on the surface of the plate. We now drill one hole each into the
plate through the guides // and / of the square, then we remove the pin
from G, turn the scjuarc around the center pin over 90 degrees, so that
one of its legs points upward and the other one to the left, insert a dowel
through the hole in the leg pointing upward into the top hole /' of the
plate, and drill the hole IP; finally we turn it again over 90 degrees,
secure it in the same manner as before, and drill the hole P. Fig. 205
Jigs 543
illustrates the square in the first position as located on the plate; the
holes H'^ and /-, which are drilled subsequently, are shown in faint lines.
In the future, we shall call these holes "pilot holes," in order to dis-
tinguish them from others in the same plate. These four pilot holes
include an exact rectangle or square, and each opposite pair is located
at uniform distances from the center of plate and flask. It will be under-
stood that it is not absolutely necessary to employ the square for drilling
the pilot holes. For instance, after one plate has been prepared in this
manner, this plate can serve as a jig for drilling any number of additional
plates in the same manner by a single setting. Such an original or
master plate is especially serviceable, if all holes are provided with good
steel bushings. The pilot holes in connection with the center hole will
serve us hereafter as guides for locating pattern dowels.
Our object in view is to use this plate as a base for any and all suit-
able patterns, and as an illustration we will arrange it for the reception
of patterns of a globe valve and a bib cock. We will assume that the
patterns are all in good shape and properly parted. However, they
shall originally not have been intended for use with either moulding ma-
chine or drawplate. Our plate and flasks are of a suitable size, but the
job is in a hurry — as all jobs are — and we must get out quite a num-
ber of these castings to-day. What are we going to do about it? Take
my advice and make it in the old fashioned way, unless you are pro-
vided with a suitable jig plate and an inexpensive, but a good small
drill press, which was never used by your blacksmiths or yard laborers,
but was expressly reserved for this purpose only, was always under the
care of a mechanic who understood how to handle it, and who took pride
in keeping it in good shape.
This jig plate (Fig. 205) should be provided with a number of holes,
two rows of which, at least, are drilled exactly in the same manner as
those in the above-mentioned square; the balance is laid out prefer-
ably, but not necessarily so, in straight and parallel hues, all equidistant
from each other. Its dimensions should be sufficient to cover one
corner, or one-fourth of your pattern plate.
If these things are part of your equipment you will have easy sailing,
and you will be better fitted to tackle the job than your competitor.
Place this jig in such a manner in one corner of your draw plate that
the hole 0 (Fig. 205) corresponds with the hole C in its center; hold both
together with dowel pins inserted into the pilot holes, and drill the holes
through the jig into your plate, which are required for securing the
patterns in the predetermined places. To avoid mistakes be sure that
the hole in that particular corner of the jig, which corresponds to the
one described as located in the apex of the square is distinctly marked
544
Moulding Machines
on both sides of the jig plate — in our figure marked O — and note
carefully which h<jlas in the jig were used for drilling the dowel holes
into the pattern plate. Thereafter turn the jig upside down on the
pattern i)late, insert the dowel pins again through the same holes O and
01 into C and /', and the third one through Oil into //-, and then, as
before, drill through the same guide holes of the jig the corresjKjnding
dowel holes into the second quarter
of the pattern plate. Repeat the
same process at the lower half of the
plate, being always careful that C and
0 remain together and your plate is
ready to receive the patterns.
That there may be no doubt as to
the method of operation, I suggest
that you will refer to the two plates
which are attached hereto, one of
which (Fig. 206) is made on transpar-
ent— so-called "onion skin" paper.
The cut on the latter represents the jig. In faint lines thereon is shown
the outline of the position of patterns, which corresponds to the arrange-
ment of the same on the pattern plate (Fig. 207). Horizontal and \ertical
■ . 1 1 1 1 1. 1 1 1
:ji_^ 3
0p
_II ^__I .
x_I^_
_± :±:
- 4::^::
XX
^XX 4--|
XX
^
' : I X-14-
ait
B-.-''
■ i ♦ ;_
■' ^
::^r-::-
; ^- . T ! • . !i . 4- : * •: M
Fig. 206.
Fig. 207.
lines, which are provided with identification marks, cross all the holes
in the jig plate. The holes which are to be used in this special case as
guides for drilling the neccssar>' dowel pin or screw holes in the pattern
plate are indicated by circles drawn in heavy. Thus, the holes // X
and 8* are used for securing the globe valve body pattern, // -|- and
Jigs 545
/// II for the body of the bib cock, and so forth. By placing the onion
skin in such a manner over the drawing of the pattern plate, that its
hole 0 corresponds with the center hole C of the latter, and 01 and OH
respectively with /' and //', it will be noticed that the outlines repre-
senting the patterns cover each other in both cuts. The jig placed in
this position over the pattern plate, and secured to it by the pilot pins
at 0, 01 and OH is used in this manner for drilling all dark lined holes
in the right-hand upper corner of the draw plate. This being done, the
pilot pins are withdrawn and the jig plate is reversed and turned into
the upper left-hand corner of the pattern plate, just as if it were hinged
at the line 01; the pilot pins are replaced into the same holes of the jig
as before and in this position they will secure it to the pattern plate by
entering its pilot holes C, I' and H'^. It will be observed that in this
position also, and equally well, the outlines of the patterns in both cuts
fall exactly together. The jig is used in this position as before, the same
guide holes which were used in the first position in the upper right hand
corner serve again as guides for drilling the second quarter of the pattern
plate. Identically the same process is then repeated at the lower left
hand and lower right-hand corners of the plate, by first turning the jig
plate aroimd the imaginary hinge center OH, and then around 01.
In order to prepare the patterns to suit the above conditions, we pro-
ceed exactly in the same manner, by securing one-half of each separately,
and always the one which has the dowel holes, at the previously deter-
mined place on the jig plate and drilling clear through them the holes
which coincide with those drilled previously into the pattern plate.
The second halves of these patterns are then placed in position against
the first (drilled) halves; they are prevented from moving sideways by
their original dowel pins, and they may be held together by suitable
clamps. These clamps are preferably made of a universal type which
adapts them for use with all kinds of patterns, their lower portion being
constructed in the shape of a frame which rests on the table of the drill
press without rocking and which is adapted for fastening the patterns
in such a manner that their parting faces stand parallel to the drill
table. The half of the pattern which has been drilled first with the aid
of the jig occupies the upper position in this clamp or drill frame, and
the holes in this one will now serve as guides for the drill to drill the
holes in the second half which stands directly underneath. Finally,
have the original dowel pins of the patterns removed and fasten all
parts separately in place on the pattern plate by either dowels or screws,
or both, whichever may be preferable and most convenient in your
particular case.
If I may call your attention again to the drawings, you will observe
546 Moulding Machines
that \vc have prepared the pattern plate in tliis manner with four com-
plete sets of patterns; yet we have used only two. The castings result-
ing from the use of these plates should be jx-Tfcct as to match. The
amount of labor required to withdraw the patterns from the sand is
reduced to a minimum; additional time is saved by the use of a station-
ary gate or runner on the plate, and double the quantity of castings can
be produced in this manner with the same number of patterns and in
the same number of flasks. .Ml this can be accomplished by making
an effort of no lonj^cr duration than it took to describe.
If you have followed the above description carefully, you may have
noticed that it is not necessary to have an individual plate prepared for
each set of patterns. Yet I thought it better to describe this method
of preparing pattern plates and patterns for plate moulding in detail,
than to leave room for any doubt or error. You can easily see that much
of the time which it apparently took to get the plate and patterns ready
for the moulder, can be saved by providing the entire surface of the plate
with dowel holes before putting it into use. This should be done with
the aid of the jig and in identicall)' the siime manner as has been suflfi-
ciently explained in the foregoing. Thus, only new patterns have to
be prepared for the purpose, and all others, which once have been fitted,
are easily replaced and secured to their correct positions on the plate,
providing their dowel holes were promptly provided with specific num-
bers, letters or identification marks. The additional holes in the plate
will not impair its working qualities, but they could be easily closed
up with bees-wax if ol)jectionable. Finally, it is well to note that
each plate can be used in connection with all patterns within its range,
and that it can be kept in continuous service, while the patterns may be
changed at will, and as often as desirable.
While the above description may appear somewhat too e.xtended, I
assure you that a serious mistake would have been made had the sub-
ject been slighted merely for the sake of brevity. At the same time I will
siiy in justification of my apparent digression, that my original sul)ject
has not been sidetracked. .\t first sight, it may appear, that the con-
struction and the manipulation of pattern plates has but little connection
with moulding machines, but I hope that I will succeed in showing in
the course of this work, that they arc not only intimately connected with
each other, but that they arc in fact the principal parts of all moulding
machines. The lack of intimate knowledge of how to make use of them
to the best advantage, the want of proper means to effect this purpose
and the wretchedly little effort which is made to catch the right spirit of
their nature is generally the reason why a moulding machine becomes an
elephant on the hands of a moulder and an eyesore to its owner.
Flasks 547
Flasks
Good flasks are especially important in machine or plate moulding.
To insure good results from moulding machines the flasks must be prac-
ticaUy perfect. They must be constructed to insure firm holding of
the moulding sand; must be stiff, light and durable.
"The pins must be accurately fitted. The flasks, if made in sets,
must be absolutely interchangeable. The pins should be square with
the flask surface, must not bind and still must not fit too loosely.
Copes and drags when assembled, must not rock or shake sideways.
Wooden flasks, such as are used in most foundries, are not likely to
give good results in moulding machine practice. However, if carefully
and substantially made, there is no reason why their application in
machine moulding should be absolutely condemned. '
Iron flasks are always preferable, especially since they do not shrink,
warp or get out of joint."
Pressed steel flasks are still more desirable.
If wooden flasks are used they should be faced with an iron ring,
this ring serving not only to maintain alignment, but also as a base for
securing flask pins. Taper steel pins secured to lugs by nuts give best
satisfaction. The holes in lugs on drags may be reamed tapering and
the lower ends of pins turned to fit, and tapped lightly into place. After
the flask is closed and clamped these pins may be
removed, thus making a few pins serve for any
number of flasks. When not in use they should
be removed from the flasks and properly taken
care of. The pins are sometimes cut away so as ig. 20 .
to give them a triangular cross section, so that sand adhering to them
may not interfere with readily inserting them in the holes.
By continued use the pins and sockets are so worn as to be unservice-
able. The pins, of course, are replaced by new ones, but the sockets
must be bushed by sleel thimbles. The old holes are drilled out to
standard size, so that the thimbles may be interchangeable. It is
advisable to have the pin holes bushed when the flasks are made, so as
to avoid subsequent annoyance.
"The makers of moulding machines are undoubtedly very well aware
of all the requirements which are covered by the observance of these
little details. They will appreciate their importance and must admit
that they are essential to make their machines a success. Yet to my
knowledge these facts have never been mentioned. Is this information
kept from the foundryman purposely, that he may not be scared from
the purchase of machines? If he should be told all this he might in the
first place think of the expense, and next that his moulders cannot get
54^ Moulding Machines
used to refinement of this kiml, which hy the way is not a very creditable
opinion. lUil if lie i)uys one or more of the machines olTercd, he cannot
help hndinj; all this out lieforc lon^;, to his own chagrin. He may throw
the machines away, or persist in the use of them and pay dearly for his
experience. .\11 this vexation could have been prevented in the first
place and at a reasonable cost, had he been furnished in connection with
the machine, with jigs, sample flasks, pins, etc., and above all with the
necessary information to which he was entitled." Many failures to
introduce and maintain labor-saving devices can be traced to the lack
of intelligent instructions sent with them.
Mr. StupakofI further discusses in detail the dilTercnt kinds of ma-
chines remarking: "It is a grievous mistake to think that a moulding
machine of any description will replace a skilled moulder. There is no
less ingenuity required to produce good castings on a machine than to
make them by hand.
"A moulder is aided by his experience and bj' his good judgment. A
machine hand (customarily selected from unskilled labor) has nothing
to offer but his muscle and good will. These qualities . . . are but
poor substitutes for the dexterity of an e.vpert. Therefore, under
ordinary circumstances the chances are but slight to obtain good cast-
ings and good results by mechanical means which are imperfectly under-
stood and subject to reckless abuse by hands which are unquestionably
green in the business.
Owners of moulding machines should not e.xpect mar\-el3 from an
inert piece of mechanism, but it is safe to say they will seldom fail in
their calculations if they are satisfied with a reasonable increased pro-
duction, provided they are willing to pay the best possible attention to
their manipulation."
Messrs. McWilliams and Longmuir in discussing the advantages of
moulding machines conclude their remarks as follows:
"With ordinary small work, such as is usually included in boxes up
to 14 inches by i5 inches, the greatest time consumers are (i) ramming,
(2) jointing , and (3) setting cores. Jointing is largely obviated with
a good odd-side, and altogether so with a plate. Ramming by the aid
of a press reduces the time occupied to that required for the pulling
forward of a lever.
Obviously, then, the greatest time consumers, wnth one exception,
Tna.y be very considerably reduced by the simple and inexpensive aid
offered by plate moulding and the hand press. "
The exception referred to is that of setting cores, which holds good
with all forms of mechanical moulding. Pattern drawing does not take
up so much time as is usually supposed. With machines, jointing and
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55© Moulding Machines
IKiUcrn drawing arc eliminated and in certain cases, the initial outlay
is comparatively small.
On standard, but changing work, our Ijcst results in machine prac-
tice have Ijccn obtained from the hand j)ress sup|)lemcnted. in case of
deep patterns, such as flanged \alve Ixxlics, etc., by the hand rammed
pattern ckawing machine. Accessories in cither case are not costly;
the output is high and the quality good. Our best results on standard
work, in which one plate could be run for at least 300 moulds, have been
obtained from a pneumatic vibrator machine.
If the same plate could be run over a period of four or five days
without changing, then production costs fall very con.sidcrably. . . .
Whatever may be said to the contrary, stripping plate machines
involve costly accessories, but this outlay is warranted if the patterns
are of a sufliciently standard character. These machines are esi)ecially
good on intricate patterns, such as small spur wheels or others having
little or no taper on the sides. While hand machines of any type
represent a low first cost, the cost of subsequent accessories must not be
forgotten.
Power machines represent a higher initial and maintenance cost,
but if they can be maintained in constant operation, they give a low
production cost. Finally, the chief drawback to the further develop>-
ment of machine moulding of any t>-pe occurs in core making and core
setting.
An improvement in the mechanical production of irregular cores will
result in a very considerable advance in machine practice."
The following remark is quoted from page 131, same book:
"As a rule we have found that while the initial cost of the machine
is not considered, the after cost of the accessories is cut down to the
narrowest possible margin. This is short sighted for if mechanical aids
are adopted, there must be no half measures, or failure will inevitably
follow. It cannot be too strongly urged that the cost of a machine
represents only the beginning of expenditure."
CHAPTER XXIV
CONTINUOUS MELTING
There are some large shops where the processes of melting and mould-
ing are carried on continuously. In some instances the moulds are made
in one department, taken on trucks to the neighborhood of cupola,
where they are filled; then to the dumping floor where the flasks are
knocked out, and sent along on same truck to moulding floor. The
manner of conducting this operation at the Westinghouse Foundry is
described by Mr. Sheath, and is given in substance further on. In
other shops, where work of the character of iron bedsteads is produced,
the operation is also continuous, but the pouring is done in the ordinary
way.
The management of the cupola is practically the same as in the ordi-
nary foundry, except that the melter must have means for controlling
the blast, so that he may increase or decrease the supply of air as the
demand for melted iron may be greater or less. The cupola is run con-
tinuously from 7 A.M. to 6 p.m. with an interval of one hour at noon.
In respect to the cupola Mr. Sheath's advice is: "See that the coke
bed is burning evenly all around, then charge just as you would for an
ordinary run, allowing an extra amount of coke for the dinner hour.
After running about an hour open the slag hole and keep it open, except
during the dinner hour. Use about 40 to 50 pounds of limestone to the
ton of molten metal — better use too much than too httle. Have the
cupola shell large enough, as it is easy to put in an extra hning for smaller
heats."
"The Westinghouse Company have in their foundry at Wilmerding,
Pa., three cupolas, one 60 inches, two 70 inches, inside lining. When
running full, i.e., night and day, we melt 280 tons, running each cupola
about ten hours. We have operated one cupola from Friday night at
6 o'clock, until Saturday noon the following day, closing down at
1 1 P.M. for one-half hour for lunch, and again at 6.30 in the morning for
three-quarters of an hour for breakfast. This is rather hard on the
lining so we do not make a practice of it. We have tried a great many
experiments with cupolas, but as yet have been imable to find any that
will give better results than the double row of tuyeres. It is not neces-
sary^ to keep the upper ones open all the time. Our blast pressure is
551
552 Continuous Melting
about II ounces in the cupola l)ustle. When running full we melt ten
to eleven pounds of iron to one pound of coke. . . .
All charges are the same from beginning to the end of the heat.
As the iron must come very soft and uniform we do not charge more
than 4000 pounds at one time.
In the discussion of his paper at the Cincinnati meeting of the Amer-
ican Foundrymcn's Association, May, 1910, Mr. Sheath gave much
interesting information, which is summarized briefly.
Blast pressure, 1 1 ounces.
Little metal is held in cupola, consequently tuyeres are ver>' low.
We are ready to tap almost after the whistle blows in the morning.
The melting is fast or slow as the moulds appear for jwuring.
More coke is used for a small heat and slow melting, than with a
large heat and rapid melting."
The sand is conveyed to the moulding machines by overhead redpro-
cating conveyors. Mr. Sheath's description of the pouring table is
as follows:
"I might describe how we handle what we call our No. 2 table for
No. 2 work. On that table there are castings, a great many of them
measuring only a few inches. Notwithstanding the small size of the
castings, we were running 52 tons ofif that table alone on a lo-hours run,
showing what a great amount of metal can be used up under the con-
tinuous process in pouring small castings. We move the table at the
rate of 20 feet per minute. .\ drag is put on. There are cores in it.
As it passes up the core setters set the cores. Then the cope is put
on. It then goes around to the casters in front of the cupola, which is
connected with an endless control system. The casters ha\e a ladle
which can be raised or lowered by hand. They step on the table and
travel with it, pouring anywhere from two moulds to a half dozen or a
dozen, and by the time they are poured ofif, they are off at that end, and
they can ride back to the cupola."
They do that all day long. The table is not supposed to stop,
but just goes right straight ahead. It moves at the rate of about 21 feet
a minute, which allows them to core up, cast, cover down and all. The
core-setters walk with the platform and become very e.xpert.
In some moulds we put in eight cores and two or three anchors
at the same time, and it would take more than one man to do the
coring.
Sometimes one man will core it, sometimes it takes two. The
casters move right along with the table, take their ladle, and travel with
it, the same as if they were on the floor.
One man handles a ladle that holds from 60 to 70 pounds.
Continuous Melting 553
The sand does not ball up, because we do not carry it very far
with the conveyor. In the iron foundry from the time we make the
mould and pour, until the mould is shalien out, that same sand is back
again in twenty minutes. The sand is not touched by the men in any
way. It simply goes down through the conveyor. The sand drops
through the grating and is wet there and then taken overhead to the
machine.
The lowest we have ever run was 40 to 50 tons. We have run as
low as 5 tons an hour. This takes a little more lining up.
The economy comes in the room occupied by the moulds and the
handling of the sand. The sand that we pour into, is back to the ma-
chine again in twenty minutes. We get the sand, the flasks and every-
thing back empty every twenty minutes. There is a very little jarring
about the platform. We have rebuilt one after running it nineteen
years.
There is very little shake to it if it is working right. We use both
the hydraulic and pneumatic moulding machines. . . .
The cutting of the cupola lining as compared with ordinary practice
varies in proportion to the length of time in blast. We do not have
any trouble from slag. At 12 o'clock all the metal is tapped out. We
tap for slag twenty minutes before twelve and run it all out. The
blast is shut off and metal run out before twelve. All the openings are
stopped up. Very little iron comes down after the blast is stopped.
The cupola is drained before starting to work again and the blast
put on at full pressure so as to heat up quickly. Perhaps 300 pounds
metal is pigged before operations are resumed.
The smallest output any one day was 50 tons. I do not consider
that the continuous process would pay if the production was as low as
20 or 30 tons per day. If there were no moulding machines the process
would be economical upon a basis of two tons per hour."
When asked as to injury from jarring, Mr. Sheath replied:
"We make some moulds that have thirteen pockets hanging down in
our smooth moulds; but there are much larger moulds which we have not
put on the table at all, because our green sand cores are just held by a
few fingers, and we would not risk putting them on. But we make
lots of moulds that have quite deep pockets hanging down, and there is
very little jarring to it. The table has a slow movement which elimi-
nates jarring.
The displacing of the sand in the mould gives very little trouble.
The continuous system is adapted only for heats where the metal
is of same character throughout. If two grades of metal are used they
should be melted in separate cupolas.
554 Continuous Moiling
The moulds may l)c m.idc by machine or on the floor, and the table
used for pouring anything j)laccd on it.
Our conveyor makes a complete revolution in twenty minutes. We
find in our line of work that the moulds and oistings will be cold enough
by the time they travel to the shaking out end.
The flasks are all iron and when shaken out arc immediately put
back on the tabic and carried to the moulding machine. They are
carried entirely by the conveyor.
Our castings are not hcaxy. The sand is hot when it is shaken out,
but when it is wet and elevated and shaken back and forward in the
reciprocating conveyor, by the time it gels to the machine and iron
patterns it is all right. We have to keep the patterns warm to prevent
the sand from slicking to them.
Cores placed in hot sand will draw dampness. This feature was
provided for. Our heaviest work is with flasks containing two castings
which together weigh 45 pounds. Other flasks contain from thirty-
two to forty castings, weighing a few ounces each.
I am familiar with a foundry where the cupola is 36 inches inside the
lining. It is run from 7 a.m. to 5.30 p.m., continuously. The product
is 60 tons per day. The sand is conveyed from the shaking out stand to
the machines. Casting is continuous.
I am unable to say how small an output could be economically' pro-
duced by this system. My experience is on a production from 50 to
280 tons. With us the casters do nothing but cast, the machine men
do nothing but mould and the shakers-out do nothing but shake out.
We have had no trouble with freezing at the tap hole during the
noon shut down. "
As regards melting losses, Mr. Sheath was uncertain whether there
were records or not. His opinion was that it runs from three to four
per cent. The gates and sprues are returned to the cupola without
cleaning.
"The pouring is done by a man moving with the table. The table
is large enough for a man to stay on it with the mould. There is an
overhead traveler, which travels with him as he is pouring. As soon
as he has poured off and is at the end of his trolley line, he steps off the
table and comes right back to the cupola. The coring is done by men
standing and dropping in the cores as the moulds pass, or maybe taking
a couple of steps, depending on the number of cores. The table does
not stop from 7.15 a.m. until 12 M. unless for some special cause."
Mr. G. K. Hooper, in the discussion on Mr. Sheath's paper, remarked
in response to the inquirj* as to the minimum production for which the
continuous process can be economically employed:
Multiple Moulds 555
"That it was not so much a question of tonnage as of the number
of moulds to be poured." The handling of a smaller tonnage than that
mentioned by Mr. Sheath, if distributed over a large number of moulds
would unquestionably be productive of great economy if performed
mechanically and continuously. The mould is the unit which must be
employed in determining whether the continuous system can be applied
to any particular production."
Mr. Hooper also states that 20 minutes are not necessary for the
manipulation and cooling of the sand. He had experience with a
plant where the sand was returned in six minutes.
His further experience is that the foundry losses are less than are met
with in the same class of work made on the floor.
Belts are more desirable than conveyors for moving sand. Rubber
belts are better suited for the purpose^than canvas. Flat belts are
better than those which are troughed, and wide belts moving slowly
are better than narrow ones at high speed.
A drag or scraper conveyor is the best for distributing sand to the
hoppers over the moulding machines. It is preferably made of wooden
troughs and flights.
Nettings, riddles, sieves, bolts and nuts are best made of phosphor
bronze.
It is possible to handle all the sand required by productions up to
100 tons of castings per day, or more, with two men; even though as
much as 100 tons of sand per hour may be passing through the system.
He has subjected moiflds to very rough treatment to determine the
liability of injury from jarring and confirms Mr. Sheath's statement
that no trouble arises from this cause.
Mr. Hooper commends a system wherein the moulds are carried by an
overhead trolley and allowed to swing freely except at the point where
the pouring was done. Less power is required, less wear entailed, and
the expense is less.
The continuous system is in no sense experimental. Its worth is demon-
strated by use through many years in many large shops. . . . By means of
mechanical handling systems in the foundry, the eSiciency of the workman
is increased from 10 to 50 per cent. The average wage can often be re-
duced somewhat; the foundry loss is decreased; the floor space reduced;
in fact by such appliances only can the full capacity of moulding machin-
ery be realized.
Multiple Moulds
When several moulds are stacked one on top of another and poured
from a common sprue connecting to each mould, the process is styled
multiple moulding.
5S6
Continuous Melting
The top and bottom sections arc like the coikj and drag of the ordinary
mould; each intcrmcdiule section forms the drag for that immediately
above and the cope for the one directly below.
A numljcr of these sections, perhaps ei^hl or even nine, are piled on
top of each other and the ixjuring gate extends from the top coi^c to the
jS
Fig. 209. — Ralhbone Multiple Moulding Machine,
bottom drag. The special advantages of the sj^stem result from the
reduction of floor space, the amount of sand used; the nimiber of flasks
required, and the labor of pouring off.
Mr. E. H. INIumford, in a paper presented to the American Foundry-
men's Association, stated: "That the reduction in the amoimt of sand
used and in the number of flasks is 37 per cent; and in floor space
88 per cent below that required for ordinary floor moulding. "
Multiple Moulds
557
The pouring may be done with a crane ladle; therefore, one of the
great difficulties encountered in pouring off machine floors is eliminated.
The great weight of sand, together with good clamping overcomes the
tendency of straining.
Fig. 2IO.
Fig. 211.
Fig. 212.
Fig. 213.
Fig. 214.
Fig. 215.
As originally practiced this method of moulding covered the piling of
ordinary moulds, one above the other, and pouring from a common gate.
The advantages were confined to reduced floor space and reduction of
pouring difficulties. Subsequently each intermediate section was
made to serve as a cope and drag; but the process was confined to pat-
558
Coiilinuous Melting
Icnis having |)lanc bases, lljc drag having simply a flat surface. Thb
limilaliun arose from the diflkully entountcretl in obtaining good
moulds by pressing the patterns into the sand to form the drag. Later
it was found that by bringing the drag up suddenly against the prcsscr
head, the sand was made by its inertia to take the imi)ression of the
pattern equally as well as when pressed from above. The scope of the
process was immediately enlarged and although the method is not as yet
c.\tensi\cly emjjloyed there seems to be a reasonable jirobability that
it may be extended to cover the range of moderately small work now
made by mechanical processes.
The cut above (Fig. 209) shows a machine of this character designed
for making chilled plow points.
The moulds in jwsition for clamping, and samples of castings made
are shown in cuts above (Tig. 210-215).
Permanent Moulds
Moulds of more or less pcrniancnc^- made in loam, and moulds for chilled
work, such as car wheels, etc., have long been in use, but moulds of a
permanent character have only recently been used for extended lines
of castings which are not chilled.
The management of the cupola, melting and pouring are ver>' much
the same as pursued in the continuous process already described.
The moulds are either mounted on frames near the cupola or are placed
on revolving tables.
The iron from which the moulds are made must be soft enough for
machining; it must be strong and of suitable composition to stand
repeated heating without warping; it must also have a close structure
to withstand the abraiding action of hot metal. The moulds are very
heavy so that the mass of iron may carry away the heat rapidly from
the casting and at the same time not permit its temperature to rise
above 300° or 400° F. Keeping the temperature within these limits
reduces the frequenc>' with which the mould may be used. The moulds
are machined at the joints and preferably hinged; the outside of the
lower half of mould is also machined on the bottom.
Mr. Richard H. Probcrt of Louisville, Ky., in a paper read at the
Cincinnati meeting of the .A.mcrican F"oundr\Tnen's Association gave
the following analysis for moulds which had gi\cn good results:
Si
s
Phos.
Mn
C. C.
G. C.
2.02
.07
.89
• 29
.84
2.76
Permanent Moulds 559
He also states that he had used moulds made from high carbon steels
for castings having sharp thin projections. In constant use these moulds
become roughened, but are not burnt or eaten away, as with cast-iron
moulds.
He likewise suggests that pressure applied to the moulds immediately
after pouring would result in castings presenting sharp clean lines of
great density and strength.
Mr. Edgar A. Custer of Tacony, Pa., presented at the same meeting
a most interesting paper on the same subject and also submitted many
sample castings, made by this process. Without giving definite informa-
tion as to sizes of moulds with respect to patterns, he impressed the
necessity for great mass in them. For instance, a mould for a 2-inch soil
pipe T, weighs 500 pounds; one for a 3-inch trap 1700 pounds. In a
mould for 4-inch soil pipe weighing 65 pounds, there were 6500 pounds
iron. Castings were made in this mould every seven minutes without
raising its temperatiu^e over 300° F.
He found that it is unnecessary to coat the moulds, but that their
temperature must be sufficiently high to prevent the condensation of
moisture before casting. If the castings are removed from the moulds
immediately upon setting, there is little trouble about sticking after
60 to ICO castings have been made. The moulds improve by continued
use, but how long they will last is imknown. He has now in use a mould
in which 6000 castings have been made and it shows no signs of deterio-
ration. The life of a mould depends not so much on the number of cast-
ings made in it as upon the number of times it has been allowed to
become entirely cold and then reheated. Continuous pouring, when
correctly timed so as to preserve a generally even temperature, has but
very slight tendency to crack the mould. If the castings are removed
from the mould as soon as they have set sufiiciently to handle, there is
with proper mixture no appearance of chill when cold. This was shown
by a number of samples which had been machined. The iron was soft,
and was readily filed on the parts not machined.
Cores are made of cast iron, and if straight, or curved in circular
shape, can easily be removed from the castings, if taken out quickly
while the casting is at a bright red. It is altogether probable that the
time to remove the castings is at any period after setting and prior to
the third expansion, and that the core should be removed during the
third expansion. See Keep's "Cast Iron," Chapter VIII. The iron
must be melted very hot. ]\Ir. Custer's view is that the percentage
of silicon may range between 1.75 and 3 per cent. The mixture in use
by him is as follows:
56o
("onlinuous Melting
Si ' Pho8.
. 1
s
Mn
G. C.
C. C.
2 2i I IJ
.01
^
30a
I 54
Mr. Custer summarizes as follows:
"Any casting that can be poured in a sand mould can be poured in an
iron mould. If the iron is hot enough to run in green sand mould it will
surely run in an iron mould.
Iron that is suitable for radiator fittings, or brake shoes, or any
other class of duplicate work that is made in sand, will be suitable for
the use of permanent moulds. The same e.xperience that shows the
foundryman what is best for sand moulding can be applied in |)ermanent
mould work.
It is true that a somewhat wider range of iron can be used in per-
manent moulds for the same class of work than is the case in sand mould-
ing, but any change from the general practice in selecting irons for any
particular class of work must be made with a great deal of care. It is of
course a subject that demands close and incessant study, and every
manufacturer who wishes to use permanent moulds must give the same
care and thought to this method that he has given to those previously
employed. "
Interesting information was brought out in the discussion of Mr.
Custer's paper which is summarized below.
Temperature of moulds is not allowed to exceed 300° F.; the pouring
is proportioned at intervals so as not to exceed that temperature.
It takes 25 seconds to make a 4-inch soil pipe T. No sand used in
the core. The core for this mould was shown, which had been in con-
stant use for thirteen months.
The mould for a 2-inch T weighed 500 pounds, the T itself weighs
8! J pounds.
The core with which the T was made was shown. It had been in use
seven months during which i>eriod 3500 castings were made.
A casting can be made from it e\cr)- forty-five seconds throughout
the day.
No precaution is taken against shrinkage. Chilling quicklj- to point
of set makes castings homogeneous, reducing shrinkage strains to a min-
imum. A trap weighing 42 pounds made on a sand core was shown.
One is made every seven minutes. The mould weighs 1900 pounds.
The casting is taken out within four seconds after pouring.
No special care is taken to keeji the moulds from dampness. They
are simply \snped out carefully before using. The core, upon which a
Centrifugal Castings 561
four-inch pipe, 5 feet 3 inches long was made, was shown. The pipe
was H inch thick and weighed 65 pounds. The core had Me inch taper
in the whole length.
The pouring table revolves once in yii minutes. There are on it
35 pipe moulds, and a casting is produced every fifteen seconds.
In a ten-hour run at this rate of production, the temperature of the
moulds never exceeds 250° F. The operations are automatic. With a
2-inch pipe, the casting can be taken from the mould within three seconds;
it must not be allowed to remain in mould over six seconds. With a
six-inch pipe, the time of removal is from five to sixteen seconds.
One man operates the table, pouring and removing the pipe, cleaning
out the moulds, and setting the cores. The iron is white hot as it comes
from the cupola. No attention is paid to coating the moulds; they are
wiped out from time to time with a greasy rag if any dirt is present.
The heaviest castings made are 6-inch pipes weighing no pounds each.
Gates are made larger than in green sand practice.
JMr. Custer did not consider the phosphorus content of importance.
He prefers iron 0.5 to i.o per cent phosphorus on account of fluidity.
Chilling occurs so quickly that there is no segregation. The tensile
strength of castings made in iron moulds is about 30 per cent greater than
that of same character made in sand.
Brake shoes are left in the mould seven seconds. It takes about a
minute to make a brake shoe. The castings do not warp.
Six-inch pipes can be laid on the pile within 20 seconds after casting.
The silicon content should not be lower than 1.75 per cent, sulphur
should be below 0.05 per cent, total carbon high as possible not below
2.65.
Has used 70 per cent scrap with pig carrying 3 per cent silicon.
Centrifugal Castings
In 1809, Anthony Eckhardt of Soho, England, was granted a patent
for making castings in rotating moulds, procuring in this manner either
hoUow or solid castings. Nothing favorable seems to have resulted
from the scheme.
In 1848, Mr. Lovegrove attempted to make pipes in this manner.
Subsequently a Mr. Shanks patented the same method in England.
Sir Henry Bessemer endeavored to remove the gases from steel castings
by a similar process.
About the same time a Mr. Needham endeavored to apply the method
to making car wheels. So far as can be learned nothing of practical
value resulted from these efforts. It is said that car wheels are now
made in Germany in this way using a high carbon steel for the rim and
562 Continuous Melting
soft material for the rciiler. The moulfJ is made to revolve about 120
times |)er minute while jwuring. The (irinciple is use<l by dentists success-
fully, and there seems to be no good reason why it could not be applied
to some classes of iron castings where difTiculty is encountered in running
delicate parts, or to obtain inc reased density at the iM;ri[)hery.
Castings vinder Pressure
Attempts have been made to submit the li(|uid iron to pneumatic
or hydraulic pressure in order to eliminate fxsrosity or shrinkage cavi-
ties. So far these have been entirely experimental; the successful
application of the idea would remove all doubt as to shrinkage in rims
of fly wheels or in similar castings, where undiscoverable defects may
exist.
Direct Casting
Making castings directly from the furnace has been practiced more
or less since the discovery of reducing iron from the ores. But by
reason of the presence of impurities and gases, which are to a greater
or less extent eliminated in the process of refining in the cupola, the pro-
duction of castings by the direct process has never been followed to
any extent. In fact, except for quantities of large coarse castings, or
an occasional piece required at the furnace, it may be said that the
process has been entirely disregarded. The presence of kish in large
quantity has been the greatest obstacle to contend with. The use of a
receiver with reheating provision, in connection with manganese would
seem to indicate a solution of this difTiculty, especially for pipes and
other coarse castings, where the physical characteristics are not matters
of vital importance.
In view of the advancement in modern metallurgy, it is more than
probable that commercial competition will turn manufacturers of prod-
ucts for which such iron is suitable to further efforts in this direction.
Carpenter Shop and Tool Room
In every foundry the services of a carpenter and machinist are more
or less in demand. In the larger works it is found most convenient to
devote separate space to each.
The carpenter shop should be given suflBcient room for construction
and repair of wood flasks, bottom boards, etc., and with its equipment
of benches, trestle, etc., should be provided with a cut-off saw.
The tool room should have a drill press and small lathe. Unless there
is a laboratory connected with the works, the testing machines are con-
veniently located in the tool room.
Tumblers
563
The Cleaning Roona
The cleaning room should be adjacent to the moulding room, but
separated from it by a wall or partition to exclude the dust and dirt
from the foundry.
Where the work is heavy there should be proper facilities in the way
of tracks and cranes. The necessary equipment comprises tumbling
barrels, brushes, chipping (either hand or pneumatic) and grinding
apparatus.
The sand blast is also of the greatest value.
Tumblers
The shape, size and number of tumblers depend entirely upon the
character and volume of the work. Tumblers are made to revolve
about inclined or horizontal axes. Those having inclined axes are used
for very light castings, brass, forgings, etc. They are seldom found in
the ordinary foundry. The barrel may be tilted for loading or dis-
charging. The following cut shows the general character of this type.
They vary in size as re-
quired.
Fig. 216 shows the No.
2 machine mounted with
28-inch cast-iron barrel in
partially lowered position
preparatory to dumping.
This machine is designed
along the same lines as the
No. I tumbler excepting that
it is much heavier and the
crank shaft is back geared 2
to I, making the raising and
lowering of the barrel when
heavily loaded quick and
easy. It is driven by tight and loose pulleys 16 inches in diameter by
3%-inch face, and will take barrels from 22 to 36 inches diameter, of
wood, cast iron, steel, wrought brass and cast brass. The tumbling
process may be wet or dry as desired, and the design of the machine
is such that the barrel may be located at any required angle while in
motion, to suit quantity of work being operated upon, and lowered to
empty by means of the crank, ratchet and pawl. It has a belt shifter
not shown in cut.
Fig. 216.
564 Continuous Melting
Floor space, with barrel, 42 by 60 inches.
\Vcij;ht, without barrel, fxxj pounds.
Speed of light and loose pulleys, 147 to 168 rev. per min.
Speed of barrel, 35 to 40 rev. per min.
The ordinary horizontal tumbler is from 30 to 36 inches in diameter
and from 4 to 6 feet lonj;. It may revolve on trunnions or on friction
rollers.
The barrel is made up of cast-iron slaves .securely bolte<l to the heads,
and with closely fitting joints. The peripheral speed should be about
90 feet per minute. They are used singly, in pairs, or in batteries.
The castings, large and small, are packed as closely as possible in the
barrels, together with a quantity of shot, sprues or stars. .cVny un-
occupied space is filled by pieces of wood. If any of the castings are
delicate they are tumbled by themselves, so as to avoid breakage. It is
not uncommon to tumble castings weighing 600 to 800 pounds; they
must be packed very closely, however. The length of time that castings
must be rattled to clean them depends entirely upon the intricacy of
the shapes. While ten minutes may answer for some, others may
require 30 minutes or even an hour.
The injury to castings from grinding away sharp comers or angular
projections arises from the improper packing or too long continued
tumbling. Since the dust comes from the tumblers in great volume,
as an act of humanitj', they should either be enclosed, or provided with
exhaust fans. The dust may be carried to a water seal, or discharged
outside the shop.
The cuts following show several varieties of tumblers manufactured.
Usually each shop makes its owti tumblers, so that the patterns may be
at hand for repairs.
Fig. 217.
Reliable Steel Square Tumbling Mills
56s
" The Falls " Friction-driven
Tumbling Mill
This mill was designed by an
expert foundryman. It is of the
very best workmanship through-
out, and is guaranteed to give
splendid satisfaction.
Made in six sizes as follows:
Fig. 21
No
Diameter,
Length ,
inches
inches
I
26
48
2
32
54
3
38
60
4
42
54
S
48
72
6
54
78
Reliable Steel Square Tumbling Mills
Particularly Suited for Light Castings
Fig. 219.
This is a strong mill with double heads. Each side is strengthened
by a T bar run and riveted the full length and doubly bolted to each
head. Edges are enclosed by an angle securely riveted and countersunk
from end to end. Door opening is strongly reinforced.
566 ('(lilt imioiis Melting
Friction-driven Exhaust Tumbling Milla
These mills are especially adapted to be run in gangs from one shaft
and one driving pulley. They can be stopped or started independently
or may be remo\ed with contents from the driving frame by crane and
conveyed to any part of the foundry. Mills may be equipped at small
extra cost with reversing device, permitting rotation in either direction,
mills still remaining portable and interchangeable.
They combine strength with simplicity.
Mr. Outerbridge discovered that the strength of castings was increased
by tumbling. Following up this discover)' Mr. Keep determined that
the increase of strength by tumbling ceased after two hours treatment,
that the increase in strength was due to smoothing and pressing the
surface, closing any incipient cracks and openings.
Chipping
Much of the chipping must 1)C done In- hand. The pneumatic hammer
has, however, superseded the hand chisel to a great e.\tent. There are
few foundries not equipped with this de\ice.
Grinding
To finish castings properly, the fins and gate spots should be ground.
In addition to the ordinar>' emer>' wheel, the portable wheel driven by a
flexible shaft is employed advantageously.
The Sand Blast
This appliance is of the greatest importance. More surface can be
cleaned with it in a given time than by any other means except the
rattler. The use of the other appliances above mentioned is not dis-
placed by it, however, as there are many recesses about castings wliich
are protected from the blast, and which must be cleaned by hand.
The importance of properly cleaning castings should not be over-
looked. No matter how well made or how good in respect of material,
if ihcy are sent from the cleaner in a slovenly condition, their commercial
value is greatly impaired.
Pickling 567
Pickling
Formerly pickling castings was largely employed, but of recent years,
by reason of the improved facings used, the practice is not so much
followed. Nevertheless there are places about castings from which the
sand is not properly removed by the ordinary processes, and again
some machine shops prefer pickled castings, as the cutting edges of
their tools are not injured so quickly, by reason of the entire removal
of the sand. This process is also followed where the castings are to be
galvanized or tinned, as it leaves clean metallic surfaces.
For pickling, either sulphuric or hydrofluoric acid is used, the former
more commonly. The acid solution must be weak ; one part of ordinary
vitriol to four or six parts of water attacks the iron rapidly, whereas the
undiluted acid has no effect.
In diluting the acid, care must be taken to pour the acid into the
water, and not the water into the acid. Dilute sulphuric acid dissolves
the iron in contact, thereby loosening the sand. The action is more
rapid with warm than with hot solution.
This solution, when applied to castings, will loosen the sand scale in
from one to twelve hours, depending upon the thickness of the scale.
The acid solution is kept in a lead-Uned wood vat. The vat should
be about two feet deep, the other dimensions varying with the amount
of castings to be treated. At the bottom of the vat is a wooden grating
fastened together by wood dowels. The grating is held down by lead
weights. It must be high enough above the bottom of the vat for the
sand to drop through. Upon this grating the castings rest as they are
immersed.
After remaining in the bath the requisite length of time, they are
removed and thoroughly washed with hot water. The acid must be
completely removed or they will rust. It is a good plan to dip them in
a strong solution of lye or soda before washing.
Another practice is to place a lead-hned platform so that one edge
may overhang one end of the vat; the platform incUning a couple of
inches toward the vat, and having the remaining edges raised two inches,
so that all the drainage may be into the vat. Upon this platform is
placed a wood grating, and the castings on the grating. The pickle is
then dipped from vat with an iron bucket and poured over the castings.
They are washed thoroughly with the pickle, so that there may be
no sand surface which has not been saturated. It may be necessary
to repeat the operation more than once. When the sand scale begins
to loosen, the castings are removed and washed as before. The washing
may be done with a hose while the castings are on the bed, but in such
568 Continuous Melting
case [wovision must be made to ( arr)' off the water in a trough so that
it may not enter the vat.
The strength of the solution must l>e ke|)t up Ijy addition of fresh
acid from lime to time.
Hydrofluoric Acid
Where this acid is used for pickHng, the solution should \ie one part
of 48 per cent acid to 30 parts of water. Hydrofluoric acid dissolves
the sand instead of acting on the iron. The treatment of the castings
is the same as with the \itriol, l)ut the sand must be removed from below
the grating, otherwise the acid will be rapidly neutralized.
The workmen should be cautioned in handling cither of these acids
as they cause severe bums, if they come in contact with the flesh.
Where acid is spilled on the flesh or clothing, wash the parts freely with
water and then with dilute ammonia. Raw linseed oil applied to bums
produces a soothing effect.
Hydrofluoric acid leaves the surface of the castings bright and clean,
and is, therefore, best for electroplating.
CHAPTER XXV
Method of Ascertaining the Weight of Castings from the
Weight of Patterns
Pattern weighing
one pound
Weight when cast in
Cast
iron,
pounds
Yellow
brass,
pounds
Gun
metal,
pounds
Zinc,
pounds
Alumi-
num,
pounds
Copper,
pounds
Bay wood . . .
Beech
Cedar
Cherry
Linden
Mahogany. .
Maple
Oak
Pear
Pine, white.
Pine, yellow
Whitewood . .
16.1
10.7
12.0
8.5
9.2
9-4
10.9
14.7
13. 1
16.4
9-9
9-5
18.0
12.0
13. 5
9-5
10.3
10.5
12.2
16. 5
14.7
18.4
10.3
10.0
18.9
12.6
14. 1
10.0
10.8
II. o
12.8
17-3
IS. 4
193
8.5
8.2
IS. 6
10.4
II. 6
8.2
8.9
91
10.6
14 3
12.7
IS. 9
10.5
10. 1
19.2
12.8
14.3
10 I
II. o
11. 2
13.0
17. S
15.6
19s
Allowance should be made for any metal in the pattern.
Specific Gravity and Average Weight per Cubic Foot of
Pattern Lumber
Wood
Beech
Cedar
Cherry
Linden
Mahogany . . ,
Maple
Oak, white. .
Oak, red . . . .
Pine, white.
Pine, yellow
Walnut.
Average
weight per
cubic foot,
pounds
46
39
41
37
SI
42
48
46
28
38
38
569
570
Dftcrminalion of Wci^lit of Ca.sting.s
Weight of Casti.sgs Determined from Weight of Patterns
(By F. G. Walker.)
''■■" '■'• ••■• 1 in
A p.ittem Wfighirn;
one pound made of
iron,
pounds
Zinc,
pounds
Copper,
pounds
Yellow
brass,
pounds
Gun
metal,
pounds
1
Alumi- , .
num, ^
pounds , J"^*^
1
Mahogany, Nassau. . . .
Mahogany, Honduras.
Mahogany, Spanish —
10.7
12.9
8.5
12. S
16.7
14. 1
9.0
10.4
12.7
8.2
12. 1
16.1
136
8.6
12.8
15 3
10. 1
14.9
19.8
16.7
10.4
12.2
14.6
9 7
14.2
19.0
16.0
10.4
12 S
ISO
9 9
14.6
19 S
16.S
10.9
so
32.0
Pine, yellow
Oak
Weight of a Superficial Foot of Cast Iron
Thick-
ness,
inches
Weight,
pounds
Thick-
ness,
Weight,
pounds
Thick-
ness,
inch.,.s
I'i
Weight,
pounds
46.87
51.56
56.25
60.93
Thick-
ness,
inches
Weight,
pounds
y*
9 37
14.06
18.75
23.43
I
28.12
32.81
37.50
42.18
i i"s
2
65.62
70.31
75 00
Formulas for Finding the Weight of Iron Castings
To find the weight of sfiuare
or rectangular castings, multi-
ply the length by the breadth,
"" ~ "L " — ^ by the thickness, by 0.26:
Fig. 221. W = LBTX 0.26.
To find the weight of
solid cylinders, the weight
equals the outside diameter
squared, multiplied by the
length, multiplied by 0.204:
If
D-L X 0.204.
Determination of Weight of Castings
571
W = weight of casting in pounds;
L = length of casting in inches;
T = thickness of casting in inches;
B = breadth of casting in inches;
D = outside or large diameter in inches.
To find the weight of hol-
low cylinders, multiply the
small or inside diameter plus
the thickness, by the length,
by the thickness, by 0.817:
W=[d + T)TLXo.Si7. Fig.
K- L-
FiG. 224.
W = DdL X 0.204.
W = weight of casting in pounds;
L = length of casting in inches;
T = thickness of casting in inches;
D = large diameter in inches;
d = small diameter in inches.
To find the weight of a hollow hemisphere,
multiply the thickness by the small radius
plus the thickness divided by 2, squared, by
1.652:
To find the weight
of a solid ellipse, mul-
tiply the large diam-
eter by the small di-
ameter, by the length,
by 0.204:
To find the weight of a solid sphere, mul-
tiply the diameter cubed by 0.1365 :
W = D3 X 0.1365.
Fig. 226.
W = weight of casting in pounds;
R = outside or large radius in inches;
r = insidv or small radius in inches;
T = thickness in inches;
D = outside or large diameter in inches.
S7^
Determination of WciRhl of Caslings
Formulas for Finding the Weight of a Hollow Iron Sphere
and a Body of Rammed Sand
To find the weight of a hollow sphere mul-
I \]. tiply ihc outside diameter cubed, minus the
inside diameter culled, by 10.365:
D--->
W = {D*-d') 0.1365.
Fig. 227.
W = weight of casting in pounds;
D = outside or large diameter in inches;
d = inside or small diameter in indies.
Fig. 228.
To find the weight of a body of rammed
sand, multiply the length by the breadth, by
the height in feet, by 87:
W = LBH X 87.
W = weight of body of sand in p)Ounds;
L = length of body of sand in feet;
B = breadth of body of sand in feet;
H = height of bodj' of sand in feet.
Formulas for Finding the Weight of Iron Castings
To find the weight
of a triangular casting,
multiply the length by
the breadth, by the
thickness, by 0.13:
TT' = LBT X 0.13.
Fig.
■-L-
229.
To find the weight of a flywheel, 11 feel in
diameter, having elliptical arms. The first
operation is to find the weight of the hub;
second, the rim; and third, the arms. The
sum of these gives the weight of the wheel.
To find the weight of the hub:
W = id + T)TLX 0.817.
To find the weight of the rim, the same
formula as above is used.
To find the weight of one arm:
/fO -J
Fig. 230.
W
DdL X 0.24.
Determination of Weight of Castings
573
Multiply by six to find the weight of the six arms.
W = weight of casting in pounds;
D = outside or large diameter in inches;
d = inside or small diameter in inches;
L = length in inches;
T = thickness in inches;
B = breadtli in inches.
To find the weight of a spherical segment of one base, multiply the
square of the height by the difference between the radius of the sphere
and one-third of the height, by 0.818; or, to the
radius of the base squared, multiplied by the
height by 0.409, add the height cubed multiplied
by 0.136:
W = H^-(r--\ X 0.818,
TT' = r"H X 0.409 + ^^ X 0.136.
TI' = weight of casting in poimds;
R = radius of sphere in inches;
H = height of segment in inches;
f = radius of base in inches.
Fig. 231.
To find the weight of a spherical segment of two bases, from the
radius of the sphere multipUed by the difference between the squares of
the distances from the bases to the poles by
0.818, subtract the difference between the cubes
of the distances from the bases to the pole,
multiphed by 0.273, or*
To the sum of the squares of the radii of the
bases, multiplied by the height by 0.409, add
the height cubed, multipUed bj' 0.136:
Fig. 232.
TT' = R (.42 - 52) X 0.818 - (.43 - B^) X 0.^273,
W = H{r'^ + s^) X 0.409 + ^ X 0.136.
W = weight of casting in pounds;
R = radius of sphere in inches;
T = radius of large base of segment in inches;
5 = radius of small base of segment in inches;
A = distance from large base to pole in inches;
B = distance from small ba.se to pole in inches;
E = height of segment in inches.
574
Determination of Weight of Castings
1
the
o find the wcisht of a ring made by ( uiting a cylindrical hole through
center of a sphere, muluply ihc chord cul>ed by 0.136:
W = C X 0.136.
The chord is equal to the srjuare root of the
result obtained by subtracting the square of
the diameter of the hole from the square of
the diameter of the sphere:
C = VlP-^.
Fig. 233.
W = weight of casting in pounds;
D = diameter of sphere in inches;
d = diameter of hole in inches.
To find the weight of a ring of circular cross section, multiply
the radius of the cross section ^?qua^ed by the radius of the circle
passing through the center of the cross section,
by 5.140: y^^
W = r-R X 5.140.
TF = weight of casting in pounds;
r = radius of cross section in inches;
R = radius of circle passing through cen-
ter of cross section in inches.
To find the weight of a frustrum of a hexagonal pyramid, multiply
the siun of the side of the large base squared, the side of the small base
squared and the product
of the two sides, by the
length, by 0.226, or mul-
tiply the sum of the dis-
tance across the flats of
the large base squared,
the distance across the
->l
Fig. 235.
flats of the small base squared and the product of these two distances,
by the length, by 0.075.
!26,
;F = (5^ + j2 + Ss) LXo.
To find the weight of
a straight fillet, multiply
the radius squared by the
length, by 0.0559.
w = r:^lx 0.0559.
]V=^{r-+f + Ff)Lx 0.075.
71"
Fig. 236.
Weight Required on Copes
575
W = weight of casting in pounds;
L = length of casting in inches;
S = side of large base in inches;
5 = side of small base in inches;
F = distance across the flats of large base in inches;
/ = distance across the flats of small base in inches;
R = radius of fillet in inches.
Formulas for Finding the Weight Required on a Cope to
Resist the Pressure of Molten Metal ; and the Pres-
sure Exerted on the Mould
To find the weight required on a cope to resist the pressiu'e of molten
iron, multiply the cope area of the casting in p — "j
square inches by the height of the riser top 1
above the casting in inches, by 0.21 : v.^-=r^=r
-mi^
W = AH X 0.21.
Fig. 237.
W = weight to be placed on a flask in pounds;
A = cope area of casting in square inches;
H = height of riser top above casting in inches.
To find the pressure exerted on a mold by molten iron multiply the
height in inches from the point of pressure to
the top of the riser by 0.26:
P = H X 0.26.
■:.-;^^;::;-::>:".:-.^:S.:V.:0 p _ pressure in pounds per square
Fig. 238. inch;
H = height from point of pressure to the top of the riser in
inches.
To find the weight of an inside circular fillet,
multiply the difference between the diameter of
the cyUnder made by the side of the fillet and
the product of the radius and 0.446, by the
radius squared, by 0.176, or, from the diameter
of the cyUnder made by the side of the fillet,
multipHed by the radius squared, by 0.176, sub-
tract the radius cubed multiplied by 0.0784.
W = (D- 0.446 R) /?2 X 0.176,
or W = DR' X 0.176 - R^ X o.oyS4.
Fig. 239.
576
I )il(rrniii;iti()n of Weight of Castings
To find the weight of an outside circular fillet, multiply the sum of
ihe diameter of the cylinder made by the side of the fillet and the product
of the radius and 0.446, by the radius s<|uarc<l,
by 0.176, or to the diameter of the cylinder
made by the side of the fillet multiplied by the
radius squared, by 0.176, add the radius cubed
multiplied by 0.0784:
W = {D + 0.446 i?; /P X o. 1 76,
W
DR? X 0.176 + K' X 0.0784.
^
R
.?^i
k- D--->l
Fig. 240.
II' = weight of casting in pounds;
R = radius of fillet in inches;
D = diameter of cylinder made or generated by
the side of fillet in inches.
CHAPTER XXVI
WATER SUPPLY, LIGHTING, HEATING AND
VENTILATION
Water Supply
Provision for water supply to the foundry is a matter of the first
importance. If water cannot be obtained from the pubUc mains, facil-
ities for pumping and distributing must be provided. The system
must be so arranged, either by elevated tanks or otherwise, as to fiu'nish
water under a pressure of from 25 to 30 pounds. While the supply
must be abundant, the natural tendency to its wasteful use must be
suppressed.
Fig. 241. — Water Box and Hose Connection.
Conveniently located near the cupola for ciuenching the dump, should
be a hydrant with hose attached, ready for immediate use. Pipes should
be so run about the foundry that taps may be conveniently distributed
for wetting down the floors and sprinkling the sand heaps; each floor
must have easy access to the sprinkling hose. Ample provision should
be made for drinking; basins near the drinking fountains, in which to
bathe their arms and faces, add greatly to the comfort of the workmen.
The illustrations herewith, taken from the Iron Age, show provisions
577
57S Water Supply, Light in^, Heating and \'entilation
made fi)r this purpose and for lavatories, clc, in a large Cleveland
foundry
Running water should be supplied at the closets. In many foundries
of recent construction, wash basins, shower baths and lockers arc pro-
vided, enabling the men to wash and change their clothes before leaving
the works. The free use of water implies, of course, a system of sewer-
age. Care must be taken to avoid puddles or wet six)ts about the floors.
The matter of water supply for fire protection is entirely indefjendenl
of that for foundry purposes, and should be provided for separately.
Fig. 242. — Porcelain Washbowls and Sled Lockers in Lavatory.
Lighting
Next to water supply in importance is the matter of lighting. Many
foundries are deficient in this respect and sufTer either in the character
or quantity of product from improper lighting. Daylight is invaluable,
and should he utilized to the fullest extent. In the construction of
foundry buildings, the windows should be tall and as close together as
the character of the structure will permit; they should not e.xtend
lower than four feet from the floor. A modern construction showing
the sides of the building made almost entirely of glass is showni in the
engraving below.
Windows in the moniter should be swi\-eled and arranged to op>en easily
for ventilation. Skylights are to be avoided if possible, as they cause
no end of annoyance. The weaxnng-shed roof gives excellent results,
and is frequently used in foundr>' construction. The glazing should be
of a character to prevent the direct admission of sunlight. Ground
glass, wire glas.'^ or glass wnth horizontal ribs afford a mellow light,
relieving the eyes from the glare of direct sunUght.
Heating and Ventilating
579
Artificial light for the early morning and late evening hours, during
the season of short days, is best afforded by some adaptation of the
electric lamp. Tungsten lamps in groups of four, distributed at inter-
vals of about 40 feet are largely used. Such lamps are provided with
reflectors to direct the rays downwards and diffuse them. The lamps
must be placed so as to clear the crane ways, and should be elevated
about 20 feet from the floor. The Cooper-Hewett mercury lamps,
placed about 50 feet apart and covered with reflectors, are very satis-
factory. The flaming arc lamps, similarly placed, furnish the greatest
illumination for a given expenditure of current.
Fig. 243.
A recent type of kerosene burner, the Kauffman, having a mantel
somewhat similar to the Wellsbach, is said to furnish a given candle
power at less cost than any lamp known.
With anj' system of hghting, care must be taken to keep the lamps
clean and in good order, otherwise their efficiency is soon greatly im-
paired. Where electric lights are used, the generators should be inde-
pendent of those which furnish current to the motors. Power for fans,
elevators, cranes, sand mixers, etc., is most conveniently supplied by
electricity. Each machine should have an independent motor. Elec-
tric trucks, operated by storage batteries, and magnetic hoists, for
service in the foundry and yard are almost indispensable. In fact
the introduction of electricity has so simplified foundry operations
that its use is imperative.
Heating and Ventilating
Heating and ventilating the foundry are subjects which formerly
received little attention. A few stoves or open fires in iron rings, placed
where they would be least in the way, constituted the usual equipment;
foundries fitted with steam heating or hot-air systems were exceptional.
580 Water Supply, Lighting, Heating and Ventilation
Gradually foundrymen have learned to appreciate the advantages of a
n)mfi)rl;il)le working; lcmi)cralure and good ventilation, xs shown by
increased output. A cold shop and chilled or jiarlly frozen sand heaps
may easily reduce the value of a morning's work from 20 to 25 per cent.
.\s foundry oix;rations re(juire active physical exertion, the temperature
of the shop should not e.xceed 50° to 55" F. At 7 o'clock in the morning
the building should be warm tluoughout. For this purix)se direct and
vacuum steam heating systems are used with gcKxl results. Both are
open to objections. The warm air is not evenly distributed; much of
it is sent to the u()[)cr part of the building, where it docs no good. With
either system several hours are required in extremely cold weather to
produce a comfortable temperature in the morning. Cold air enters
through the windows and doors, causing drafts and an uneven distribu-
tion of heat.
More satisfactory results are furnished by the fan and hot-blast system.
This consists of a sheet-iron chamber, in which are placed the requisite
number of coils heated cither Ijy direct or exhaust steam, if the latter
is available, an exhaust fan and the distributing pipes. The fan draws
the air over the coils and from the chamber and forces it about the build-
ing through large ducts, from which branch pipes are taken at proper
intervals; through these branches the warm air is discharged at the
desired spots within the shop. This system is largely used and possesses
advantages over those having direct radiation.
The amount of heat absorbed by air flowing over pipes increases
rapidly with the velocity of the air. When the velocity' of the air current
flowing over the pipes in the heating chamber is about 1500 feet per
minute (the usual velocity) the area of the heating surface required to
accomplish a given heating effect is only about one-fifth that for direct
radiation. With the fan and hot-blast system the building is filled
with air under slight pressure, termed a plenum, which prevents cold air
from entering; warm air flows out through all leaks. The warm air
is discharged from the pipes near the floor, and uniformly distributed
through the low,er part of the building. By reason of such distribution
and the great volume of air discharged, the shop may be quickly warmed
in the morning. If the fan is driven by an independent engine, the
exhaust steam is sent directly to the coils, thereby making tlic expendi-
ture for power nominal. Where live steam is not available for an engine
the fan may be driven by a motor. With the motor-driven fan, the
watchman can start the apparatus during exceedingly cold nights, anfl
thereby prevent the sand heaps from freezing. The ducts are usually
circular in section, made of galvanized iron and supported by the chords
of the building so as to clear the crane way.
Heating and Ventilating
S8r
The sketch below shows the usual arrangement for fans and ducts.
In shops of moderate size, where but one fan is required, the ducts, of
course, must run all around the building.
Fig. 244. — Typical Arrangement of Heating and Ventilating System for
Foundry with Unobstructed Craneway.
From the ducts, discharge pipes are dropped at intervals of from 30 to
40 feet. These usually terminate about 8 feet above the floor line, and
leave the ducts at an angle of about 45°, inclined in the direction of the
5S2 Water Supply, Lighting, Healing and N'cntilaiion
air currents. Where the discharges are dropped as alx)ve slated, ihe
open ends should incline about 20° from ihc vertical; they should
alternately face the walls and the center bay. Six square inches of <Us-
charge ojjening are ordinarily allowed for every icco cubic feet of space,
and ihe aggregate area of the openings should be 25 per cent greater
than the area of the ducts. From these data the size of the ducts may
be calculated for any building of known dimensions.
Underground ducts with vertical discharge jjijjes are desirable, as
thc3' offer no obstruction to foundry operations, but they are quite
expensive; the overhead ducts seem best to meet all requirements.
Where steam or hot air is used for heating, the matter of ventilation
requires no provision, except for that period of the day occupied in
melting, as the leakages are suflicierrt to supply an abundance of fresh
air. During the heat, vapor and gases rise in great volumes; to permit
them to escape or to permit fresh air to enter, the swiveled windows in
the monitor are opened.
WTjere steam heat is employed, discomfort is occasionally experienced
during cold or stormy weather, as the gases fall as soon as they begin
to cool, and the vapor is condensed by the incoming air. With the hot-
blast system this difficulty does not occur, since the plenum is sufficient
to drive out the gases and vapor through the open windows. Mr. W.
H. Carrier of the Buffalo Forge Company, Buffalo, N. Y., has discussed
the subject of Foundry Heating and Ventilating so fully in a paper pre-
sented at a meeting of the American Foundr>Tnen's Association, that
advantage is taken of the opportunity presented through the courtesy
of the Buffalo Forge Company to make extensive extracts therefrom:
"The proper distribution of heat in the foundry is comparatively difficult.
In general the problem is that of a large open space, affording little
opportunity for efficient placing of direct radiation. On account ol
the monitor type of building usually employed, there is relatively a
great height. The hot air rises up into the lantern and passes out through
the ventilators, if fans are not provided to deUver it near the floor. The
heated column of air in the building serves to draw cold air from with-
out at every opening. This inward leakage of cold air, not only de-
mands a great amount of heat, but makes a thorough distribution of
heat at the floor line most essential for comfort and economy of opera-
tion. A sUght plenum, or outward leakage, of air at the doors and
openings, caused by the delivery and proper distribution of sufficient
heated air into the building is the only solution of the difficulty. Ample
ventilation is at times most necessary. The lantern type of build-
ing is best adapted to quickly ventilate, since the ventilators simply
have to be opened to permit the hotter and Ughter gases and vapors
Heating and Ventilating 583
to pass out. External air must enter the building to replace that
escaping through the ventilators. Cold air entering the doors and
openings tends to cool and condense the rising vapors. It is there-
fore essential that a system be installed which will deliver warmed
fresh air during the pouring periods, when ventilation is of first im-
portance.
Rapid heating of the building in the morning means that the best
efficiency from the men will be obtained over the entire working period.
A system which is elastic, and which may be rapidly varied to suit the
requirements is to be favored. Coke or gas fired salamanders are appar-
ently the most economical means of heating, as all the heat goes directly
into the building. The atmosphere in a tightly closed building heated
by this method becomes intolerable, and if sufficient ventilation is
provided to make conditions healthful, the amount of heat required is
greater than with other systems. The grade of fuel used is also con-
siderably more expensive than that used in other systems of heating,
to say nothing of the care of a large number of separate fires scattered
about the building.
In heating with direct radiation, steam is usually employed, although
hot-water systems with forced circulation have been successfully oper-
ated. Unless there is a large amount of hot water available, it is not
an economical system to employ, on" account of the greatly increased
amount of radiating surface required at the lower temperature. In
steam heating, the high pressure, the low pressure or the vacuum system
of distribution may be used; the selection of the particular sj-stem
depends on load conditions. Where high-pressure steam is available,
and there is no exhaust steam, it should of course, be used. If, however,
there is no high pressure or exhaust steam available from the power
plant, then an independent low-pressure boiler should be installed, fur-
nishing steam at from 5 pounds to 10 pounds pressure. For low-pressure
work cast-iron boilers may be used; no boiler feed pumps are required.
The boiler should be placed at a level low enough for the condensation
to drain back by gravity. If this is impracticable, then a centrifugal
pump may be employed to return the condensed water to the boiler.
A vacuum system should always be used when exhaust steam from the
power plant is available. In a vacuum system of distribution, the
back pressure should not exceed i pound, as otherwise the losses will
outweigh the gain. The fan sj'stem is undoubtedly the best for foundry
heating and ventilating, and it is particularly adapted to the severe
requirements of foundries, and other buildings of this construction,
where there are large open spaces to be heated. The principal advantages
of the fan system over direct radiation are:
584 Water Supply, Lighting, Heating and \'enlilation
1. The thorough distribution of heat secured by discharging the air
under pressure through suitable outlets, wnth suflicicnt velocity to
ciirry the heat to the jxjints where it is most needed without causing
jicrceptiblc draughts.
2. No hc;it is wasted as in direct radiation, where a large part is sent
directly through the walls, with slight effect upon the temiK-rature of
the building. The fan system affords means of supplying heat directly
to the interior of the building.
3. No heat is wasted by heating unoccupied spaces, as along the roof
and in the monitor. Tests of the fan system installed in foundries have,
in certain instances, sho\vn lower temperatures in the monitors than at
5 feet above the floor line.
4. Fan systems heat up very much more rapidly in the morning,
when it is desirable to bring up the temperature in as short time as
IKJssible.
5. It gives a rapid warm air change, which effectually removes
smoke, steam and dust during pouring time; an effect possible only
with a fan system. During such periods, when ventilation is required,
the fresh and return air dampers should be adjusted to take all the air
from out of doors. During the remainder of the day, however, the
greater part of the air should be returned from the building to the
apparatus, so that the heat required for ventilation may be the least
possible. Precaution should always be taken to see that this feature
is provided for.
6. Fan systems cost less to install properh-, since the apparatus is
centrally located, and it is not necessary to pipe the steam to all parts
of the building as in direct radiation.
7. The cost of maintenance is less, since the radiating surface of a
direct system along the walls is frequentlj' damaged, while in the cen-
trally-located fan apparatus, it is thoroughly protected.
As in direct radiation, steam or hot water can be used in the fan
system heater coils; but as the cool air is drawn over these coiLs by
the fan, a great deal more heat is obtained from the same amount of
heating surface. This permits the square feet of radiation to be re-
duced about two-thirds. The fan is often driven by a direct -connected
steam engine, the e.xhaust from which is used in the heater coils. This
is an exceedingly economical method, as practically all of the heat of
the steam is utilized.
A new t>pe of fan heating system, which is ginng the highest degree
of satisfaction, has been developed by the Buffalo Forge Company; this
is the direct air furnace system. Instead of burning fuel under boilers,
generatmg steam, transferring steam from boilers to heater coils through
Heating and Ventilating 585
a long riin of pipe, and finally giving up heat to air from the heater
coils, this system transfers the heat of the burning fuel directly to the
air for distribution. An efficiency of 85 to 90 per cent has actually
been attained, as against the usual efficiency of 50 to 60 per cent derived
from steam service. The Buffalo Forge Company has made many
installations using gas for fuel, and recently erected one in which pow-
dered coal was used. Fuel oil can also be employed. The construc-
tion of the furnace is similar to that for a water tube boiler. The hot
gasses pass through the tubes, a fan draws the circulating air around
the tubes, by which it is heated, and then distributes it through the
building. Fig. 244 shows one of these furnaces recently installed in an
important factory in the West. The main hot air ducts from the fan
are usually made of galvanized iron, and are carried in the roof trusses.
When these ducts are placed at a height not exceeding 20 .feet, the air
may be delivered directly into the building through short outlets. The
design of these outlets is of particular importance to the success of the
sj'stem. The velocity must be properly proportioned to the height,
to the size of the outlet and to the horizontal distance which the air
is to be blown. The greater the distance and height above the floor,
and the smaller the outlets, the higher the velocity must be to obtain
the proper distribution. On the other hand, if the velocity is exces-
sive for these conditions, objectionable draughts will be produced.
In some cases the main pipe has to be placed too far above the floor
to permit good distribution of heat at the floor line with short outlets.
In such cases it is usual to provide drop pipes from the main at the
columns or along the side walls. Where the drop pipes are placed at
the columns, each pipe is usually provided with two branches; one
blowing toward the base of the windows at the side walls, the other
blowing toward the center of the building. Where the drop pipes are
extended downward at the side walls, it is usual to provide three outlets
to each pipe, two blowing sidewise along the walls, and the third out-
ward toward the center of the building.
In wide buildings it is customary to run two lines of pipes along the
columns on each side; while in narrower buildings it is possible to
obtain an entirely satisfactory distribution of heat with one line of
main pipe, having outlets so proportioned as to blow across the building
to the further side. A very neat, though more expensive system of
distribution is with underground main ducts, with galvanized iron
vertical risers, arranged along the columns or side walls; or in some
instances, as in particularly wide buildings, at both places. The system
of outlets in this case will be practically the same as where drop pipes
are used. Fans may be either motor or engine driven. When an
s86 Water Supply, Lighting, Heating and Ventilation
ul)undancc of exhaust steam is available for use in the heater coils, the
molor-<lriven fan will be fount! the more economical and satisfactory. It
is preferred liy many on account of the simi)iicity of ojieration and the
slight care and attention required. Witii small fans it is gowl practice
to clirect-conncct the motor to the fan; but with the larger apjiaratus
the speed of operation is so low as to make it advisable to Ijelt-drive the
fan, by reason of the high cost of slow speed motors. Engine-<lriven
fans are advisable when moderately high jjressurc steam is available.
The steam can be used to drive the fan and the exhaust is available for
the heater coils. This method is exceedingly economical, since prac-
tically all of the heat is utilized.
The power used to drive the fan is almost negligible, as the engine is
really little more than a pressure reducing valve. The speed of operation
with engine drive is also much more fle.vible, allowing a wider range of
speed, as may be necessitated by var}ing weather conditions. Direct
radiation and the fan system of heating cost practically the same to
install, the fan system as a rule being somewhat cheaper. Of course,
with the fan system, the power necessary to drive the fan is additional,
and it might seem that the operating expense would be somewhat more
than with direct radiation; but the more equable distribution of heat by
the fan system cuts down the losses and reduces the radiating surface
materially. The operating expenses of the two systems, however, vary
little in the long run."
-
CHAPTER XXVII
FOUNDRY ACCOUNTS
Any system of foundry accounting must be subject to variation in
details to meet the requirements of different classes of work.
A system suitable for a foundry producing pipe, car wheels or other
standard work must be modified in some of its details to adapt it to
the requirements of a jobbing foundry. The value of an accounting
system, aside from determining the cost of production, lies in reducing
the expenses and in pointing out by comparative analysis the direction
in which reductions can be made.
Cost keeping is too often neglected. Many foundrymen establishing
prices, etc., by those of competitors, have absolutely no knowledge of
actual costs. There are few branches of business in which the indirect
expenses, those apart from the cost of material and labor, exceed those
of the foundry. Only by constant comparison, by tracing increase or
decrease from one period to another, and continually following lines
indicating improved results, can the expenses be made to approach the
minimum.
An effective cost system must not only furnish accurate results, but
must furnish them promptly, so as to permit ready and periodical com-
parison.
Prompt information as to any means of increasing production or of
decreasing losses or costs greatly enhances its value. The system must
not be so elaborate as to render it impractical, but simplicity must not
be accompanied with neglect. One that is not accurately or system-
atically followed is worse than useless. Any effective system requires a
large amoimt of clerical work, but the results are profitable in the high-
est degree.
The one given below has been in satisfactory use by a large manu-
facturing establishment, making castings for its own consumption.
An order emanates from the management, going to the drawing room.
There it is given a shop order number. A form bearing this number is
fiUed out, showing the patterns required, the drawing number, pattern
number and number of castings wanted from each pattern, date of
deUvery from the foundry and any changes to be made. This form,
No. I, passes to the Requisition Clerk, who makes a requisition in quad-
587
588
Foundry Accounts
ru|)le, form Xo. 2, on the foundry. This form is about six by nine inches;
and as many sets of blanks, all Ixiaring the same shop order number, are
used as arc rccjuircd. These fonns are in shape for inde.xing willi
guide cards, 'i'hree of each set of these forms after completion are
sent to the founcky, and the fourth is hied in the office.
Of the three sets sent to the foundry, one is marked " Foundry Rcquisi-
lion," one "Pattern Shop" and the third "Core Room."
The foundry clerk fills in date of receipt, date for deliver)' of patterns
;ind cores and the casting date; then, having marked on them the
deliveries required, he transmits to the Pattern Shop and Core Room
their respective requisitions. The Pattern Shop and Core Room fore-
men each stamp them with dale of receipt.
Form 2.
FOUNDRY REQUISITION
Williams & Jo.nes
Shop Order, 5486. Date, 3/9/10. Castings wanted, 4/4/10.
For 25 9X12 C. Crank. S. Valve Throttling Engines.
Name of part
Drawing
number
Pattern
number
No. of
pieces
wanted
Alterations
7984
8092
8093
8140
8098
8099
7642
7990
7991
46.854
46,855
46.856
46,857
46,859
46.860
46.861
46.862
46.86.5
25
25
25
25
25
25
100
flange at exhaust out-
let }% inch.
St'f'ng box gland
Steam chest cover
Steam chest glands
Cylinder lagging
Piston
Add Me inch to each end
of cover.
Reduce diameter H inch.
Requisition received in foundrj', 3/10/10.
Requisition received in pattern shop.
Requisition received in core room.
Order to be completed, 3/31/ 10.
Floor date, 3/22/10.
Patterns wanted, 3/21/10.
Cores wanted, four sets, 3/22/10.
Four sets each day thereafter.
Record of Caslings Made
Date
Good
Bad
Date
Good
Bad
Date
Good
Bad
Date
Good
Bad
3/22
3
I
3/29
2
3/23
4
3/24
4
3/25
4
3/26
4
3/28
4
Pattern Card
589
In filling out the floor or casting date, the date of delivery, etc., the
foundry clerk knows that only four cylinders can be made at each heat.
He therefore fixes the date for completion at 3/31/ 10; this allows four
days to provide for any contingencies. The Foundry Requisition is
then filed under its floor date.
At the end of each week the index cards up to that date are with-
drawn from the front and passed to rear of card box. There are enough
cards in the box to cover six months or a year as desired.
Any unfilled orders at the end of the week are advanced to the first
date of the coming week, so that the current orders are all at the front
of the box. Each day the foreman and clerk spend time to select
orders and make out a program for the next heat.
As the orders are completed, each requisition with its supplementary
orders is filed away for reference.
The Foundry Pattern Loft is divided into two parts, one for uncom-
pleted orders (Live End), and the other for completed orders (Dead
End).
The patterns are deUvered by Pattern shop at the Live End.
A man from Pattern Storage has a book in which he takes receipts
for patterns delivered. He also receipts for patterns which he removes
from Dead End.
Precisely the same system is pursued with core boxes. The Pattern
Shop delivers and removes the boxes, taking and giving receipts.
Attached to each pattern is a tag, on which all the data above the
heavy line is made out in Pattern Shop: all below is filled out in Foundry.
PATTERN CARD
o
Moulder's Tag.
Foundry Tag.
Date issued, 3/21/10.
Date issued, 3/21/10
Shop order, 5486.
Shop order, 5486.
Name of piece, 9x12 cylinder.
Name of piece, 9X12 cylinder.
Pattern No. 46,854.
Pattern No. 46,854.
No. wanted 25. Date 3/31.
No. wanted 25, date, 3/31.
Name of moulder, John Hayes.
Name of moulder, John Hayes.
Date in sand, 3/22/10.
Date in sand, 3/22/10.
Tally //// //// //// //// ////
Moulder's time.
Moulder must return this tag
John Hayes — ¥ ¥ ¥ ¥ ¥
with pattern.
John Hayes — ¥ ¥ ¥
Wm. Moran — ¥ ¥ ¥ ¥ ¥
Wm. Moran - %'■ ¥ ¥
The tag is perforated across the middle. When the pattern is issued
to the moulder, the clerk tears off and retains the foundry tag on which
5QO
Foundry Accounts
llic lime is entered and then Tiled away. The moulder's tag is de-
stroyed when |)allern is removed to storage.
The foreman ol core room enters time of core makers on core room
requisition. It will be noticed that the clerk has not only entered on
the Foutidry tag the time of John Hayes, but also that of Wm. Moran,
iiel|jcr.
There must be a case in which arc kc|jl cards showing records of pig
iron, scrap, coke, sand, sea coal, fire clay and any other material re-
ceived in car lots.
PIG IRON CARD
Pig Iron
From Jones. Smith & Company
Car. N. P. R.R., 438.827. Brand Xo. 2. S.
Wt., G. T.. 24.23.
Analysis ,
Received. 2/10/10.
Price, J16.S0 Did.
1
Silicon Sulphur
2.38 1 .032
Phosphorus
.43
Manganese
.54
Net weight. 54.282.
Expended. 54.660.
Overrun, 378.
CO O O f^ *^ O* C30
&:?:
10 t* 0> N ^^ V
M « 1-1 Ci N « >
« « « M M « O
On back of this card the withdrawals and corresponding dates are
entered and balance cast up on face.
The cards for sand, fire clay, etc., are the same as for coke, without
the analysis. It is advisable, howe\er, to have these supplies analyzed
ocaibionally.
Pig Iron
COKE CARD
591
Coke
Form 5.
Car No. 7482, N. Y. C.
Received, 2/7/10.
Ovens, Hamilton by-product.
Weight, 32,600.
S4.8S Deld.
A nalysis
Per cent
85
8
Ash
II
I
As a matter of convenience to the foreman in making up the mixture,
it is desirable to enter the pig iron in a special book, as per diagram
below as well as to keep the cards.
PIG IRON
Form 6.
Sample Page of Pig Iron Book.
Date
re-
ceived
Car
No.
Brand
Net
weight
Ex-
pended
Analysis
12/9/09
12/9/09
12/15/09
1/7/10
2/10/10
132,568
35,689
46,351
25,135
439.827
No. 2S
No. 2S
No. 2 N
No. 3 N
No. 2 S
78,594
76.432
69,496
58,439
54.282
12/20
12/27
1/14/10
2/8/10
3/2/10
I* Si 3.2s S .03 P .89 Mn .82
2* Si 3.09 S .032 P .85 Mn .75
1 Si 2.84 S .038 P .76 Mn .68
2 Si 2.80 S .040 P .74 Mn .66
1 Si 2.19 S .027 P .29 Mn .75
2 Si 2.10 S .026 P .27 Mn .74
1 Si 1.67 S .024 P .26 Mn .69
2 Si 1. 65 S .023 P .24 Mn .67
1 Si 2.38 S .032 P .43 Mn .54
2 Si 2.25 S .036 P .48 Mn .52
I
2
I
2
* No. I is the furnace analysis; No. 2, that of the foundry chemist.
The Heat Book is given on page 592. In this book the foreman enters
for the coming heat the irons which are to be used and the mixture.
The remainder of the account may be filled out later by the clerk after
returns are made. This book is of the greatest importance as it enables
592
Foundry Accounts
the foreman to repeal at once any mixture lused at any time, or for any
particular purjiosc.
The sheet shown is for the Iicat of 2/22/ from which 4 cylinders arc
to be poured and a special charge (the first) containing 10 per cent steel
scrap is made. The cylinders weigh al>out 500 pounds each, and as
there arc crank disc and other castings requiring strong iron, the entire
first charge will contain steel.
The charges arc 4000 pounds each, and the mi.vturc is uniform through-
out the heat, except for first and last charges. Turning to the Pig Iron
Book, the foreman selects such iron as will furnish the desired mi.xture
for cylinders, also those for the remaining charges and enters them on
the heat book. A memorandum is given the boss of the yard gang,
showing the car numbers and the amount of iron from each car for each
charge.
The number of charges for the ordinarj- mixture is left blank until
later in the day, when the total amount to be melted is ascertained.
The weighman has a pad of forms upon which he prepares a slip for
each charge giving the car number, weight of iron from each car, weight
of coke and lime.
Each charge of iron is piled by itself on cupola platform in regular
order. The coke with limestone is sent up in cars as the charging of
cupola proceeds.
SAMPLE SHEET FROM HEAT BOOK
WiLLi.wis & Jones Fouxdry
Form 7.
Heat of 3/m/io.
Pig iron
C-ar
No.
Weight
per
charge,
pounds
No. of
charges
Analysis
Remarks
Silvery
No. 2 Sou .
No. 2 Sou. .
No. 2 Nor. .
No. 2 Nor..
Scrap
Steel scrap .
No. 2 Sou. .
No. 2 Nor. .
No. 2 Nor..
Scrap
Clean-up...
8,296
439.827
46,351
328,503
27.935
328,503
45,541
200
400
400
800 •
1800
400
800 -)
6col
200 1
2400 )
1050
I
20
I
Si 4.20 S .03 P .72 Mn .68
Si 2.25 S .036 P .48 Mn .52
Si 2.10 S .026 P .27 Mn .74
Si 2.29 S .023 P .24 Mn .67
Si 2.10 S .084 P .63 Mn .63
Si 3.75 S .017 P .86 Mn .36
Si 2.29 S .023 P .24 Mn .67
Si 1.92 S .024 P 28 Mn .63
Si 2.10 S .084 P .68 Mn .63
First
charge
! »
1 charges
Last
charge
Sample Sheet From Heat Book
593
Amount Charged
Pig iron.
33,8oo
Scrap.
49.800
Steel scrap.
400
Clean-up.
1,050
Total.
85,050
Coke.
10,950.
Returned 320.
10,630
Flux.
1,600
Production
Good castings.
Bad castings.
Gates and sprues.
Over iron.
Shot.
Clean-up.
Total accounted for.
Lost in melt.
Per cent melt in good castings.
Per cent castings good.
Per cent castings bad.
Per cent melt in returns.
Per cent loss in melt.
Iron melted per pound coke.
66.466
2,708
6,106
5,143
650
1,670
82,743
2,307
78.2
96.1
3.9
(19.0
' 2.7
8 lbs. to I
Mixtures
1st charge special.
Regular charges.
5% car 8296.
20% car 328,503.
20% car 27,935.
60% scrap.
10% car 439.827.
10% steel.
15% car 328,503.
10% car 46,351.
45% scrap.
5% car 45,541.
Analysis
Computed.
1st charge.
Si
1.66
S
.075
p
.42
Mn
.46
Have
analyses
Computed.
Regular.
Si
2.21
s
.088
p
.63
Mn
47
made
as re-
Actual.
1st charge.
Si
1.64
s
.080
p
.43
Mn
45
quired
Actual.
Regular.
Si
2.23
s
.092
p
.6s
Mn
.44
594
Foundry Accounts
Prtxluctivc
Non-
productive
Total*
Av. ,
per
hour
32.60
Hours
1133-6
113. 6
Cost
Hours
Cost
Hours
c:ost
$383.38
Foundry
GDre room
Cleaning room
$274.90
34.08
180
36
234
$28.80
S.76
39 84
$74.20
1697-2
Total
1247-2
$308.98
4SO
Helper* arc
included in
foundry as
productive.
Blast on. 1:50 p.m.
First tap, 2:13 P.M.
Test bar special.
Test bar regiUar.
Pressure, 9 ounces.
Bottom dropped, 4:45 P..M.
Transverse, 2800.
Transverse, 2200.
First iron, 2 p.m.
The meller and boss of the yard gang are each furnished with a copy
of charging schedule. '.Vfter the charges are all up, the wcighman turns
in to foundry ollice, slips for the bottom coke, and one for each charge
gixnng complete weights of everything entering the cupola.
Form 9.
Charging Schedule
Date, 3/22/10.
Charges
1st charge .
20 charges .
Last charge.
Materials
Bottom coke
Steel scrap
Car 8296
Car 439.827
Car 46,351
Car 328,503
Scrap (selected)
Coke
Car 27.935
Car 328,503
Car 45.541
Scrap
Returned coke
Clean-up
Use 80 pounds limestone from third to
nineteenth charge inclusive.
WeighU
3850
400
300
400
400
800
1800
400
800
6co
200
2400
100
loso
Weigh Slips 595
Weigh Ticket
Form 10.
Charge No. i. Date, 3/22/10.
Coke bottom 2850
Steel scrap 400
Car 8296 200
Car 439.827 400
Car 46,351 400
Car 328,503 800
Scrap 1800
Limestone.
Weigh Ticket
Form 10.
Charge No. 2. Date, 3/23/10.
Coke 400
Car 27,935 800
Car 328.503 600
Car 45,541 200
Scrap 2400
Limestone.
On the day following the heat, after recovering the iron from the
gangways, cinders, etc., the yard foreman turns the weight into the
ofSce.
Returns from Foundry
Form II.
3/23/10. Heat of 3/22/10.
Bad castings 650
Over iron S143
Shot 650
Clean-up 1670
Returned coke 320
The bad castings on above slip are those thrown out in the foundry,
to which are subsequently added those rejected in the cleaning room.
590 Foundry Accounts
I'rom the moulder's tags, turned in on the zand, and from information
oblaini'd from the floor concerning work on lag-, which luivc uot lux-n
turned in, the clerk |>rci)ares in part, du|,>licate cleaning rcxim reix)rts.
He enters the shop order nimilR-rs, pattern numl)ers, names of parLs
and numljer of |)arts made. Tliis re|>ort then goes to forcm;in of clean-
in>^ room, who com|>letes it, sending one copy to the foundry oflicc and
tlie other to the work's olTice.
The form is given on page 597. As many sheets as are necessary are
used for each heat.
The Time Book, Weigh Tickets, Foundry Returns and Cleaning Room
Report furnish all the data, except analysis and test, for completion
of entrj' in heat book for 3 22 10. Information as to the last two items
is obtained from time to time iis required. The heat report is made out
in duplicate; original sent to Works Ofl'ice and du[)licate filed in Foundrj'.
This is followed by a weekly summary. At the end of each month an
inventory is taken of all supplies; and their cost, jjer hunflred pounds
good castings, is determined for the month passed. This cost is used in
making out foundry reports for the succeeding month.
All supplies except the bulky materials, such as sand, fire clay, etc.
are kept in store room and are issued upon requisition from foremen
or clerk, upon blanks as per sketch.
Requisition on Dale, 3/21/10.
Store Keeper, Issue to
Jno. SULLrV'AN,
5 Pounds Silver Lead.
W.M. Wilson. Foreman.
These requisitions, together with tallies of sand, fire clay, etc., are
turned into office by store keeper at end of month.
Careful scrutiny and comparison of these monthly statements and
expenditures result in marked savings. They promote among the
departments a strife for the lowest record. The reduction in the amount
of core supplies, nails, rods and sand is especially noticeable.
As regards iron flasks and other castings made for the foundrj-, if
they are for permanent equipment, ihcy are so charged. If on the
other hand they are for temporary service, they are charged to foundr>-
at cost of labor, plus the difference between the cost of good castings
and scrap.
Monthly comparisons, or more frequent if desired, are made with
statements from the works office. Comparisons arc likewise made at
the end of the fiscal year.
Cleaning Room Report
597
5 "O
H B
fOC^ TtfON tM*© M
0»OoO O OO-^OO"^
"S s
rON-^roo»TfN(0
f^W '^fO'N '^(N'O
S ^c
M -^ t^ -^ O r^ i/i
N a> w M w o o
M ►"! o) f^ w w w
§"3
w
6^
fi
^e^
^
lO li^ l/l in
1 S I § S gg : -g
■ x: bo cj 00 cij f^ j^
i W c/5 c/i 02 U E S
m to t^ a^ O tH
5 -O "O to ^o
■^ '«3- -^ -^ ■^
tOtOvOtOtOtOtOtOvO
OOOOOOCOQOOOOOOOOO
ioioio»o»oioioioio
598
Foundry .\ccouiiis
Form 14.
FOUNDRY
AlU.IAMS 6i
Heat ol
Grade
No. I
No. 2
Car No.
Sou.
439.827
46.351
27.93S
No. 3
No. 4
Weight...
Cost
Car No.
Silvery
8296
Weight
200
200
$1.49
Weight
No. 2 N.
400
400
16,000
16.800
I123.73
Car No.
328.S03
45.541
Weight
12,800
4.000
16,800
$127.51
Car No.
Weight
^
"?;c_. a
&
«^ a
e
B&
Cost
Iron i
good
castin
"S-S
CO "S
"3
Returns
includ
bad
castin
S'3
1^
<
m
oca
V
8.5 "S
04 0
Weight...
85,050
66.466
2708
13.569
2307
82.743
78.2
96.1
Cost
$634.66
J520.73
Costs
«>&
^ <» ^
m «
a
2
"3
BO
si
J2 8
1
BtJ
►S3
•a
•0 c
lie
ill
0 C-.S
C-3 2
founc
St per
pound
castin
S
S"
1
§1
a 0T3
380
"8s
5 8 81
M
ilO
H <«
Hours
1133.6
H3-6
450
1697.2
2.55
Cost
$274.98
$34.08
$74-40
$383.38
$0.5765
$00396
$0,783
$1,399
Foundry Reports
599
REPORTS
Jones Co.
3/22/IO.
a a
t.'O
wa 0
*^ 0.
0 ^
IS
DM
0
0
3
Iron pe
100 poun
coke
Cost pe
100 poun
melted ir
a
400
49,800
1050
85.050
10,630
1600
8-1
$300
$348.60
$4.20
$608.53
$25.53
$0.60
$0,746
gg
U. 4J O ^j
Total cost of melt . .
Cr.
Returns 16,275 pounds (
.70
Cost of iron in good
casting
$634.66
113.93
520.73
S«.S
0 O-tS
I0.783
I
6oo
Foundry Arcounts
WEEKLY FOUNDRY REPORT
Williams & iosvs Pounuky
Form IS.
HeaU o( 3/23-a5 and a6/io.
Date
of
Consumplion
Product
heat
February
S.8oo
0.
2
0
•3
0
H
0)
M
0
u
1 250
Is
4
IP
14
ii
"a
(2
23
36,500
32,98o| s.ooo
80,360
11,250
57.8592703
16.172
3626
80.360
25
27.720
3,6oo
23.880 s.ooo
60,200
9.540
900
43..M4 1340
1J.244 2272
60.200
28
27.S20
7.800
26.800 ....
62,200
9.930
9SO
45.406 1900
12.4062488 62.200
Totals. .
91.740
17,280
83,740 10,000
202,760
30,730
3100
146,6095943
41,822 8386202,760
Summary
Total iron melted
Total coke used
Total flu.x used
Total cost melt
Credit
Returns (including bad castings) 70^ per 100 pounds
Total loss
Total good castings
Total bad castings
Total productive labor
Total non-productive labor
Total labor
Total cost of supplies
Total foundry cost of good castings.
Per cent of melt in good castings
Per cent of melt in bad castings
Per cent of melt in bad return (including bad cast-
ings)
Per cent of melt in loss
Per cent of castings good
Per cent of castings bad
Average cost of labor per hour
Cost of iron per loo pounds
Cost of iron melted per 100 pounds
Cost of iron in good castings ix.-r 100 pounds
Cost of labor, good castings per 100 pounds
Cost of supplies, good castings per 100 pounds '
Total foundry cost, good castings per 100 pounds.. .
Iron melted per pound of coke 6.6 lbs.
Pounds
20,7260
30,720
3,100
47,76s
8,386
146,609
5,943
Hours
2,482
1,490
3,97a
$1476.09
74 so
1. 17
1551.76
334.60
615.72
246.29
Per cent
72.3
2.93
23. S
4.1
96.1
3.9
Cents
21.7
0.728
o 76s
1217.16
826.01
58.05
2137.32
0.830
0.S88
0.0396
I.4S76
Monthly Expenditure of Supplies
6oi
Form i6.
MONTHLY EXPENDITURE OF SUPPLIES
Williams & Jones Foundry
February, 1910.
Materials
Quantity
o 9
o a
Si
3 p
Anchors
Belting
Belt lacing
Bellows
Beeswax. .■
Bolts
Brick, red
Brick, fire
Brick, block
Brooms
Barrows, wheel
Barrows, pig iron
Brushes, soft
Brushes, hard
Brushes, core
Brushes, casting
Brushes, camel's hair. .
Brushes, paint
Brushes, white wash. .
Brushes, wheel
Blocks, chain
Candles
Cable wire
Carbons
Castings
Cans, blow
Chisels, cold
Chaplets
Charcoal
Chain
Chain links
Chalk
Chalk, line
Clay
Clay, fire
Clamps
Clamps, spike
Clamps, screw
Core, compound dry. .
Core, compound liquid
Core vent, metallic
Coke forks
Coke baskets
6oa Founflry Arrounts
Monthly Expenditure of Supplies Continued)
Materials
Coke scoops
Crow bars
Crucibles
Cloth wire
Cups, tin
Cutter's emery
Facing mineral . . .
Flour
Fuel
Gauges, wind ....
Gauges, air
Globes, electric. ..
Globes, lantern...
Glue
Glutrin
Grease
Hammers
Handles, hammer
Handles, sledge...
Hose, air
Hose, water
Hose, couplings . .
Hose, nozzles
Iron bar
Iron, sheet
Irons, draw
Irons, flasks
Jackscrew
Jack-bolts
Levels, spirit
Lead, bar
Lead, sheet
Lead, pipe
Lead, red
Lead, white
Lead, silver
Lime
Lumber
Litharge
Lycopodium
Mallets
Mauls
Quantity
u
u
I
Monthly Expenditure of Supplies 603
Monthly Expenditure of Supplies (Continued)
Materials
Quantity
Manganese, ferro
Mercury
Molasses
Nails
Nuts
Oil, core
Oil, coal
Oil. belt
Oil, lard
Oil, linseed
Oil, hard
OU, black
Oil, machine. ...
Oil, rosin
Oil, cans
Pails, iron
Pails, wood
Pencils, lead
Pipe, iron
Pipe, fittings
Picks, cupola
Pliers
Pliers, cutting
Pots, sprinkling . .
Paper, sand
Paper, toilet
Paper, emery
Paper, wrapping . .
Rammers
Rammers, bench.
Riddles
Riddles, brass . . . .
Rivets, copper.. . .
Rivets, iron
Rosin
Rope
Saws, hand
Saws, hack
Screws
Screws, drivers. . .
Stationary
Scrapers
Silicon, ferro
Straps, lifting. . . .
Stars, tumbler. . .
Sand, moulding .
26
° 9
02
S .0
0O4
Foiimlrv Aiiounts
MontlUy Expenditure of Supplies Continued)
Materials
Sand, lake
Sand, bank
Sand, fire
Shovels, moulders' .
Shovels, laborers' . .
Sprayers, blacking.
Sponges
Smooth-on. . .'
Swabs
Sledges
Stone, emery
Salt
Sulphur
Sea coal
Talc
Tacks
Torches, blow
Twine
Straw
Vitriol
Wire, iron
Wire, copper
Wire, wax vent
Wire, cable
Washers
Wheels, emery
Wheels, sheave
Wheels, barrow
Wrenches, open
Wrenches, monkey.
Wrenches, pipe
QuAntity
2 ! KE
& o o
■■vB
Total $284.56
Good castings for month 718.37;
Cost of supplies for 100 good castings for February, 1910 So. 0396
Use this price for the month of March, 1910.
Monthly Comparisons of Foundry Accounts
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Transmission of Orders
6ii
Chart Showing Direction of Transmission of Shop and
Foundry Orders, Together With That of Return
Reports
1 jSupcrlntendeni-
Drawing Room (
Cleanino) Yard Cupola
Room
Mouldina
Floor "^
Core
Room
Fig. 245.
The chart above shows the direction of transmission of orders from
the superintendent to the foundry office, and thence, with supplementary
orders, to the delivery of the completed product at the cleaning room;
as also that of return reports to foundry office, works office, and superin-
tendent. Full lines indicate the course of orders outward; dotted lines
that of the return reports.
From Superintendent (i) to
From Drawing Room .... (2) to
From Foundry (4) to
From Foundry Office .
(4) to
Works Office (3)
I Drawing Room (2)
Foundry (4)
Works Office (3)
Pattern Shop (5)
Pattern Shop (5)
Core Room (6)
Floor (7)
Cupola (8)
Yard (9)
Cleaning Room. . . . (10)
6i2 Foundry Accounts
From Pattern Shop (5) lo \ ;"r"''^> ^^""'^'^ J^)
' -" I Core Room (6)
From Core Room (6) lo Moulding Floor. .. . (7)
From Cupola (8) to Moulding Floor. ... (7)
From Moulding Floor. ... (7) to Cleaning Room. . . .(10)
RETUitN Reports
From Moulding Floor. ... (7)1
From Core Room (6 ) . r- j /-vn- / »
From Cupola (sj f ^° ^^^""^'■y O^"^'^- ^^^
From Cleaning Room. . . .(io)j
,, „ T^ 1 r^tr I \ ^ /Superintendent (i)
I-roml-oundryOmce (4) to { ^irks Onice (3)
From Works OflSce (3) to Su|)erintendent (i)
The system of accounting as above described has been followed for
some years by one of the western foundries, with excellent results. It
involves considerable clerical work, but one clerk can handle it.
Some modifications are required to adapt it to a jobbing foundry.
These arc indicated at once and are readily made.
As showing different methods of foundry accounting, each having its
advantages and disadvantages, papers presented on the subject to the
.American Foundrymen's .Association by Mr. B. A. Franklin and Mr. J.
P. Golden are given. . . One can be developed from the lot which will
meet any requirement.
AMERICAN FOUNDRYMEN'S ASSOCIATION
Foundry Costs
By B. a. Franklin, Boston, Mass.
"... Form I illustrates the first method of foundry cost showing:
The operations are divided into the elements of
Melting.
Moulding
Section A
I. Metal. 2. Fuel.
3. Melting E.xpense.
Section B
4. Moulding Labor.
5. Moulding Expense — Floor and Bench separately
Section C
6. Cleaning Labor. 10. Pickling.
7. Cleaning Expense. 11. Picklinp Expense.
8. Tumbling Labor. 12. Sand Blasting Labor.
9. Tumbling Expense. 13. Sand Blasting Expense.
Foundry Costs 613
Section D
14. Core Labor. 15. Core Expense.
Section E
16. General Expense.
"In discussing this system no attempt is made to discuss the method
of getting the information because such methods are simple and easily
worked out."
"The Basic Costs are illustrated in Form i, which shows the weekly
operation of the foundry as a whole, and Form 2 represents the cost of
an actual casting. Form 3 represents the monthly foundry showing
of profit and loss, offering means of proof of the foundry cost and show-
ing the net result. "
". . .As nearly as possible foundry shop economy demands, and
foundry work permits a daily clean-up, though, of course, some oper-
ations happen one day after the beginning. "
"A foundry cost might then be a daily record sheet. Weekly records,
however, are sufficient generally, and the one presented is on this
basis. "
Form i
"Section A. Deals with metal."
"Here is shown, separately for each different mixture, of which one
foundry might generally employ two or three, the weights and value
of iron charged. These weights may readily be proved by checking
as each car or lot of scrap is used up. In the case of scrap made in the
foundry or 'own scrap' no value is put on this since it is put into the
heat in an iron foundry, on the basis that scrap made on each heat will
be approximately the same per cent, and what is made one day is gathered
up and used the next day. The exception to this is in the case of 'bad
castings,' charged at scrap value, and, as seen later, accounted for in
casting cost."
"In a Steel Foundry it would be necessary to change all scrap at
scrap value and credit same to particular castings. "
"The 'metal-used' value is shown and the pounds melted, but the
'metal cost' is obtained by dividing, not by poimds melted, but by
pounds of 'castings made'^ — i.e., good and bad castings. The bad
castings are to be charged to the particular order as will be seen later.
We thus arrive at a weekly metal cost for each mixture. "
"Likewise for purposes of general guidance, there is shown weekly
the 'per cent, of good castings to melt,' the 'per cent of bad castings
6i4 Foundry Accounts
to castings made,' and the per cent of metal disappearance or 'per cent
of loss.' "
"Now for management guidance toward general shop economy,
these figures present standards and bases for striving for lower costs —
viz., to make the percentage of good castings to the melt as high as
possible, to make the |)ercenlagc of bad castings to castings made as
low as i>ossible, and the record will cjuickly show that the cost fluctuates
with these conditions. "
"And it will be found that melting and handling of metal and fuel
can be done on piece work to bring best economy in metal-cost."
"A definite and valuable i)oint to note is that in addition to the
weekly figure of cost per pound, there is carried along the average or
'period cost per j)ound. ' This is the figure to be used in cost work.
"... The weekly figures are constantly compared with the i)eriod
figures showing whether the weekly result is belter or worse than the
average, and an observation of the detail shows why. ..."
"In each section it will be noted that the costs are brought down to a
few \-ital imits or percentages, and when these vary, they are significant
of a gain or loss in economy of production, the reason for which can be
readily observed by casting the eye up the details and observing the
comparison of them."
"... Section B. Moulding. — Here are two elements to be con-
sidered — productive labor and expense. The expense is shown in
relation to productive labor. It may be sho\\Ti in relation to hours if
desired, but in each class of moulding labor there is generally no great
fluctuation of rate per hour. ..."
"The productive labor and expense should be kept separately as to
class of moulding, as floor, bench, machine, etc., since the expense varies
considerably with the class. "
" . . .A little thought and experiment would seem to show that on
the whole the expenses approximately vary according to time spent in
productive labor rather than by the pound."
"In the matter of productive labor it is to be understood that
money paid for moulding each job, whether day work or piece work,
is to be known and used in figuring definite casting, as shown in
Form 2."
"It is in this productive labor cost that the first element of variation
in casting costs is to be found, the expense percentage being the same or
taken as the same, except in the matter of certain direct charges or
expenses to be discussed later. "
Foundry Costs 615
"Section C. Cleaning Castings. — In the matter of cleaning castings
there must be some division. Tumbling, pickling, and sand blasting
are taken separately as shown below. This leaves for consideration
here the cleaning of castings by other than these three methods and
applies mainly to large castings. ..."
". . . In Timibling the labor can best be put on piece work and will
generally be done by the pound, and expenses will be shown by the
pound. ..."
"In Sand Blasting and Pickling the expenses are shown in relation to
productive labor, and the work can be put on piece work. ..."
"Section D. Core Room. — Here the labor can in the main be put
on f)iece work and the expenses shown in detail. ..."
"Section E. . . . General Expenses. — This is shown in relation to
productive labor, the items of productive labor being those of Moulding,
Core Making and Cleaning operations.
"... Thus we arrive at certain weekly and period basic figures of
cost in the main elements in the foundry of
Metal. Core Making.
Moulding. General Expenses.
Cleaning.
"The items of metal and expense are easily provable with the books
monthly, and the labor with the pay roll weekly, so that we get a proved
weekly picture of the foundry situation as compared with average or
period, and we get it in such detail as will show the reasons of all varia-
tions of operation. ..."
"Consideration of Casting Cost. The first element to consider is
that of direct charges. In many jobs, but by no means all of them,
are certain charges which it seems desirable should be charged directly
to the particular order. They need in most foundry work be very small
in number. These charges must essentially be gathered and held until
the job is shipped and cost ready to work out. "
Form 2
"Form 2 illustrates this final casting cost."
"In all castings finished in a given period, the varying elements of
unit cost would be purely the productive labor items of moulding and
cleaning and direct charges, the metal, fuel, melting, moulding, cleaning
and general expense charges being taken from the period figures on the
weekly cost sheet."
"Therefore, in working out the cost of a finished casting, it is essential
to know of it as a particular job; the weight — and the shipping slip
(h6 Foundry Arcniinls
Rives that ; the moiikiinR and core making lalwr and the cleaning labor,
where average rates |)er ]M)und are not ased. "
"... Direct charges are added and also loss on bad castings. A
record of bad ca.stings is necessary and sim|)le."
"On bad castings the loss would dei)cnd on how far the work had
[)rogrcsscd when discovered as bad, and what work on them had been
paid for. The metal, of course, would be credited at scrap value."
" By this method then it will be obser\'ed that with very small clerical
labor, the practical foundryman or manager gets a weekly, or daily,
if he so designs, view of his foundry costs and their fluctuations which
form a definite and correct basis for accurate estimate, and he can very
quickly get a particular job or casting cost by having the money sjxjnt
on moulding and cleaning, etc., gathered."
"The Cost System settled, the bookkeeping should l)c made to parallel
the cost system, in which case the monthly showing would be made to
show as per Form 3."
"Thus is obtained a complete monthly analj'sis. In most foundries
one clerk and almost invariably two, can operate the system as far as
costs are concerned."
Cost of Metal
617
Metal — Section A. No. i. Form i
Mixture No. i
Pig Grade i '.
Pig Grade 2
Pig Grade 3
Pig Grade 4
Pig Grade 5
Bought scrap
Own scrap chillers
Own scrap floor scrap
Own scrap bad castings
Own scrap gates
Weekly totals metal used. . .
Period totals metal used
Weekly total pounds castings
made
Period total pounds castings
made
Good castings made
Period castings made
Per cent good castings to melt
Period per cent castings made
Bad castings
Per cent bad castings to
castings made
Shop scrap
Per cent shop scrap.
Total pounds (weekly)
Total pounds (period) .
Pounds lost
Period pounds lost
Per cent lost.
Perio'^ per cent lost
Weekly metal cost per 100
pounds
Period metal cost per 100
pounds
Oct. 9
Pounds
34.240
32,270
S,68o
36.310
31.500
15,900
1.275
7.300
10.000
36,100
210,575
149,280
140,125
66. s
9.155
6.1
51.800
210,080
9.495
4-5
Amount
252.22
234-10
38.67
259 -35
249 . 61
106.47
Oct. 16
Pounds
33,950
33.290
14,270
32,070
32,720
17,000
1.420
9.000
9.000
34.800
217,520
428,095
150,441
299,721
139.867
279.992
64.3
10,574
7
54.400
204,841
12,679
22,174
S.8
Amount
253.87
249.68
97. IS
232.65
259.28
113.84
63.00
o
1269.47
2479.89
Oct. 23
Pounds
25,620
25,440
6,010
30.150
25,080
11,900
1,13
7.700
10,000
26,500
169,535
597.630
n6,45i
416,172
109,069
389,061
643
65.1
7,382
6.3
43,700
160,151
9.384
31.558
5-5
5.3
.85
.83
Amount
191 58
187-39
40.92
218,72
198.74
79-68
987.03
3466.92
6i8
Foundry Accounts
Mi.TAi, — Si ( rioN A — No. 2. Form i
Fuel and melting expense
Labor (cupola men)
Labor (handling coke and
coal)
Labor (miscellaneous)
Labor (handling iron)
Coke
Coal
Wood.
Fire brick.
Fire clay
Oyster shells
Mica sand
Chg. from other depts.
Analysis of iron
Rclining cupola and repairs..
Tumbling cupola bottom. . . .
Crane labor
Elevator labor
Blower labor
Handling oyster shells.
Bituminous facing.
Interest on investment
Heat, light and power
Taxes, insurance and depre-
ciation
Weekly expense
Period expense
Weekly pounds castings made
Period pounds castings made.
Weekly cost per loo pounds. .
Period cost per loo pounds. . .
Weekly pounds melted to
pounds fuel
Period pounds melted to
pounds fuel
'•■9
Oct. 16
Oc,
Pounds
Amount
Pounds
Amount
Pounds
AS-Os
44 70
1.80
573
S3 50
1.82
18.51
SS. 97
3-20
1.64
2.63
■ 90
2.00
2.63
30.00
2.00
2.90
10 95
8.66
.53
30.00
10. 7S
8.52
.80
10.20
6. IS
10.20
6.IS
149,280
12.42
199.78
.134
8.7
150,441
299,721
12.42
203. SS
403.33
.135
.135
8.4
8.5
1 16.451
416.172
9 M
44 08
82s
I S3
2.63
9 30
6.93
-44
10.20
6.IS
12.42
174. 8S
578.18
IS
.139
8.3
8.S
Moulding Expense
619
Moulding — Section B. Form i
Oct. 9
Oct. 16
Oct. 23
Pounds
Amount
Pounds
Amount
Pounds
Amount
Bench Moulding
884.80
10.00
6-58
2.42
7-50
2.60
23.16
46.37
6.30
.47
2.30
30.58
41-94
192.22
21.8
858.80
1743.60
10.00
6.88
2.80
10.48
23-54
SO. 83
6.88
.40
1.65
30.58
41.94
185.98
387.20
21.7
21. 1
Period productive labor
Moulding Expense on
Productive Labor
Non-productive labor
Flasks, snap boards and
2459 -00
5-00
I- 15
Miscellaneous supplies
1.09
Shovels and screens
Rammers.
Charges from other depts —
Making bottom boards for
moulding machines
1.60
8.19
Sand
37-77
6.10
Handling weights and bands.
.62
Parting sand.
Interest on investment
Heat, light and power.
Taxes, insurance and depre-
30.58
41.94
134 04
512.24
Per cent moulding expense to
18.7
Period per cent moidding
expense to prod, labor
20.8
630
Foundry Accounts
C"l i; ANINC, ANU TUMUUNU — SECTION C. FORM I
Productive labor
Number of pounds cleaned
and tumbled
Period pounds cleaned and
tumbled
Cost per 100 pounds (if day
work)
Period cost per loo pounds
(if day work)
Cleaning and Tumbling
Expense
Supplies.
Overseeing
Non-productive labor
Charges from other depts. . . .
Tumblers
Stars for tumbling
Interest on investment
Heat, light and power
Taxes, insurance and depre-
ciation
Weekly gross expense
Stars used in Xo. 3.
Weekly expense
Period expense
Weekly expense cost per 100 lbs
Period expense cost per 100
pounds
Weekly total cleaning and
tumbling cost
Period total cleaning and
tumbling cost
Oct. 9
Pounds
154,462
Amount
74.62
.056
544
55. 44
8.40
71.73
71.73
.053
.109
Oct. 16
Pounds
139.089
273.S5I
Amount
70.92
.053
.054
.40
• 40
.6s
4.00
S.44
55.44
8.40
74.73
74.73
146.46
• 053
.053
.106
Oct. as
Pounds
105.203
.T78.7S4
Amount
ST. 14
.054
0S3
I 93
• 75
2.03
10.00
S-44
55-44
8.40
73.98
73.98
220.44
.07
.058
.124
III
Pickling Expense
621
Pickling — Section C — No. 2. Form i
Oct. 9
Oct. 16
Oct. 23
Pounds
Amount
Pounds
Amount
Pounds
Amount
Weekly prod, labor
Period prod, labor
Weekly pounds pickled
Period pounds pickled
Weekly cost per loo pounds
62,818
20.70
.033
1.75
2.06
23.92
3.40
3.08
2.53
36.74
177. S
65,600
128,418
19.82
40.52
.030
.032
.75
15.28
1.88
3.40
3.08
2.53
26.92
63.66
135.8 ,
155. 8
36,220
164,638
13-10
53.62
.036
.034
1. 10
Period cost per lOO pounds
Pickling Expense
Non-productive labor
Oil of vitriol
Acid spigots.
Charges from other depts. . . .
Interest on investment
Heat, light and power
Taxes, insurance and depre-
ciation
Total weekly expense
Total period expense
Per cent dept. expense to
1.48
3.40
3.08
2.53
22.10
85.76
168.7
Period per cent dept. expense
160
622
l''(jiiii<lrs Accounts
Sand BLASTiNCi — Skction C — No. 3. Form 1
I Uci. y i Oct. 16
founds
Weekly prod, labor
IVriod prod, labor
Weekly pounds san<l blasted.
Period pounds sand blasted .
Weekly cost per 100 pounds
(if day work)
Period cost per icxj pounds
(if day work)
Sand Blashng Expense
Non-productive labor
Supplies
Sand
Charges from other depts —
Interest on investment
Heat, light and power
Taxes, insurance and depre-
ciation
Total weekly expense
Total period expense
Per cent dept. expense to
prod, labor
Period per cent dept. expense
to prod, labor
Prod, labor
Amount
Pounds
• 75
l.IO
6.80
IS. 40
1.38
25.43
581.9
11.800
22,000
Amount
6.06
10.43
.051
.048
.61
1. 10
6.80
IS. 40
1.38
25-29
50.72
417.4
486.3
486.3
Oct. 23
Pounds
8,100
30.100
Amount
4 61
IS 04
.057
05
.41
1. 10
6.80
IS 40
I 38
25.09
75.81
544 2
504.2
504.2
Core-Making Expense
623
Core Department — Section D. Form i
Productive labor
Period productive labor. . . .
Core Making Expense
Foreman
Tending ovens
Inspecting cores
Storing cores
General labor
Sand
Coke
Coal
Rosin.
Miscellaneous supplies
Flour.
Interest on investment
Heat, light and power
Taxes, insurance and depre-
ciation
Weekly core making e.xpense
Period core making e.xpense.
Weekly per cent expense to
prod, labor
Period per cent expense to
prod, labor
Labor
Oct. 9
Pounds
Amount
24
00
12
65
19
14
12
10
17
II
21
80
2
92
6
44
5.54
13
67
I
43
21
61
158
41
67.8
Oct. 16
Pounds
Amount
220
6S
454
20
24
00
12
63
18
08
II
78
15
16
18
32
2
45
5.58
3
00
13
67
I
43
21
61
147
71
306
12
66
9
67
4
67
4
Oct. 23
Pounds
Amount
165.65
619.85
24.00
7.87
13.89
9.62
13-37
25.89
l.S6
1-73
1.55
13.67
1.43
21.61
136.19
442 31
82.2
71-3
71.3
624
Foundry Accounts
General Exi'
Executive
Foreman
9396— 2— D.
Non-productive labor
Clerical
Supplies
Charged from other Dcpts.
Scrap
Gas
Inspecting
Injured employee
Tending pattern safe
Brooms
Interest on investment
Heat, light and power
Taxes, insurance and depre-
ciation
Weekly general expense
Period general expense
Weekly prod, labor
Period prod, labor
Per cent expense to prod,
labor
Period per cent expense to
prod, labor
Oct. 9
Pounds Amount
27-00
48.00
12.74
49 00
.87
I.S 55
45. 38
1. 00
63.20
11.47
1 1., 56
22 59
310.45
618.81
984 49
62.9
Oct. 16
Pounds Amount
27.00
48.00
25.08
49 00
1 43
26.00
357
1.00
64.59
9.60
11.56
22.59
310.45
599 87
1218 68
955 60
1940.09
62.8
62.8
Oct. 33
Pounds Amount
27 00
48.00
16.67
4900
1,85
27 75
13 98
1. 00
42 65
5 00
7.20
75
11.56
22.59
310.4s
585.4s
1804.13
790.25
2730. i4
73 9
65.8
Individual Job of Casting Cost. Form 2
Date, Oct. 12
ISO Blocks — J. & S. Co. — 850 pounds
Amount
Unit cost
Va
.83 per 100
7.0s
. 139 per 100
1.18
3.00
20.8%
.62
.50
71.3%
.36
.053 per 100
pounds
■ AS
.058 per 100
pounds
■49
.034
29
t6o^c.
.46
65.8%
2.13
.42 .
16.95
.0199
Metal
MeltinR expense
Moulding
Moulding expense
Cores
Cores, expense
Cleaning and tumbling.
850
Cleaning and tumbling expense.
Sand blasting.
Sand blasting expense.
Pickling
Pickling expense
(ieneral expense
Spoiled work
Total
Cost per pound
3 spoiled
Note. — In this case no selling expense is added, as it might be in many cases.
A Successful Foundry Cost System 625
Monthly Showing. Form 3
Quick Assets.
Cash.
Accounts Receivable.
Permanent Assets.
Real Estate.
Building.
Machinery.
Raw Material on Hand.
Pig Iron. (Credit amount used each week as per costs and charge
to Mfg. Acct.)
Scrap.
Manufacturing Acct. (See analysis below.)
Expenses undivided (meaning expense supplies not used).
Quick Liabilities.
Accounts Payable.
Permanent Liabilities.
Capital.
Depreciation.
Surplus.
Details of Mfg. Acct.
Dr.
Inventory at start of castings in process.
Metal )
Labor ^ each month.
Expense )
Cr.
Sales.
Inventory of castings in process ist of each
month.
Balance Profit or Loss monthly.
A SUCCESSFUL FOUNDRY COST SYSTEM
By J. P. Golden, Columbus, Ga.
"... The system consists of, first: a Daily Cupola Report, the
printed form ha\-ing column for charge, number of pounds coke and
brand, pounds pig iron and brand, and per cent silicon and sulphur,
scrap, foreign and returns, and total charge also Unes for weekly totals
for use in weekly report. Ratio of coke to iron. Time blast started.
Time bottom dropped. Average blast pressure. Per cent sulphur in
heat. Per cent silicon in heat. Remarks. With each sheet signed by
foreman.
626 I'oundry Accounts
"Second: The Daily Foundry Rc(X)rt, which is made up by the
RumhlinK Room foreman. This rc|>ort consists of a sheet, with columns
for name of moulder, hour or piece rate, number of moulds, numl)er of
castings, time of helper, pattern description with columns for weights
of the various classes of work, as pulleys, sheaves, hangers, hanger
boxes, pillow blocks, couplings, cane mills, factories, miscellaneous,
etc. Also column for number of pieces lost, total weight of each kind
of piece lost, and a cause column for same, showing if it did not run, if
it was crushed, blowed, or whatever cause of defect. There is a line
at bottom of sheet for weekly totals to be used in weekly report. The
daily foundry report furnishes a ready means of comparison of each
moulder's record, with his own, or with other moulders as to quantitj* of
good castings, castings lost, weight and cost of same. This reix)rt also
shows the amount of good and bad castings for each day, in each class,
with the weekly total for each.
"Third: There is a book for defective and other castings returned
from shop and customers, in which is the following rule:
'All castings returned by machine shop and cxistomers, before
being made over, must be entered in this book, gi\nng cause for
making over. Castings returned to foundry' from shop or cus-
tomers, through no fault of foimdry, must not be deducted from
net foundry castings, and should be considered as foreign scrap.
If fault of foundry, they are charged back to foundry and are con-
sidered as foundry return scrap.'
This book has columns for showing date returned, by whom, descrif>-
tion, cause and weight. Without this book, there could be returned
defective castings, which were the foundry's fault and made over with-
out the superintendent's knowledge. With the "to be made over"
casting book, all castings returned are specified therein. If the fault
of the machine shop, it is so stated. If returned from customers, this
is noted with date, description, cause and weight. No casting is made
over without being recorded in this book. This book, being always open
to superintendent and foreman, saves inquiries and explanations. . . .
"Fourth: The Weekly Foundr>' Report Sheet. This sheet is made
up from the daily foundr>' report, and cupola sheets and the book (to
be made over castings). On this sheet, provision is made for record
of bad castings returned from foundry, shop or customer, by classes,
as well as the good castings made. The total of good castings minus
defective castings gives net good castings for week. The average per
cent of all castings lost is given, with the per cent loss in each class, with
the total pounds pig and foreign scrap charged in cupola, and the net
A Successful Foundry Cost System 627
good castings deducted therefrom, we find the per cent lost in remelt,
cupola droppings, gangways, etc. The weekly foundry report also has
a record of total melt taken from daily cupola sheet, which with net
good castings deducted gives per cent, bad castings, gates, etc., of total
melt, including foreign scrap, returns and pig. In a division headed
cupola charge is given the number of pounds pig iron, foreign scrap and
coke, with current price of each and total cost per week. To these
amoimts are added the total wages, giving a total of material and wages
for week, which divided by the net good castings gives the cost per
100 pounds, net castings, including pig iron, scrap, coke, wages.
"The weekly report also has separate divisions for non-producers,
rumbling department, moulding department, core shop, day and night
cleaning gangs, in which the wages of each class of men in each division
are given separately, by total, and the wage cost per hundred pounds.
. . . The weekly report also embodies the grand total wages cost per
100 poimds, and this is the most important item, for both foreman and
superintendent, for this item is one which the foreman can control to
the greatest extent, and which speaks the loudest in favor of the system. "
"... In connection with the weekly report is a detailed report of
the pounds of good castings, to whom sold or charged, and price for each
lot, and from this sheet is prepared, on the back of the weekly report,
a statement giving the estimated profit or loss for week."
"And lastly, there is a ready reference sheet (headed Comparison of
Per cents, Wages Cost per 100 Pounds in Different Departments of
Foundry from Weekly Foundry Report) giving the comparison by
weeks and the average comparison at the end of each year of the fol-
lo\ving items after date. Net good castings for week, castings killed,
in machine shop with columns for the per cent loss of each of the several
classes of castings, each class in a separate column, gives a ready means
of comparison in that class for all of its weeks.
"There are also columns for the cost per week per 100 pounds, net
castings including pig iron, scrap, coke and wages, the wage cost per
100 pounds, in the non-producers, rumbling and moulding departments,
also the core shop, day and night cleaning gangs with a colimin for
grand total wage cost per 100 pounds.
"Both the superintendent and foreman have access to the several
reports giving each the means of knowdng the actual conditions in all
departments of the foundry at all times.
"This system gives the foreman the means of remedying a small or
defective output by the knowledge of the cause producing it, and to
place each moulder upon the class of work to which he is best fitted to
increase the general output."
6a8
I'ouiidrv Aciouiils
O
Hi
Q
2
Q
O
O
'1«!3A\
ISOJ S330UI
sncouB]
^lO^DBJ
sniuuxni
SIlllU 3UB3
s3uiidno3
s^tooiq
saxoq
i33UEJJ
sjaSuBjj
soAsaqg
sXaiinj
a
a
•o
1
dpH
}o jaqiunfi
spinoui
|0 J3quint»i
a}t3J oDaid
JO Jnojj
Name
Castings To Be Made Over
629
"... The system furnishes a basis for closer estimates than formerly
upon work a little out of the usual run, bj'' knowing exactly what prices
can be accepted for the regular work. The foundry foreman in this
case is allowed nominal control of the foundry, hiring and discharging
his men, fixing their wages, and increases in pay for his men are by his
recommendations subject to approval of superintendent. ..."
SAMPLE SHEET FROM "CASTINGS RETURNED FROM
SHOP AND CUSTOMERS, TO BE MADE OVER."
Note: All castings returned by machine shop and customers, before
being made over, must be entered in this book, stating cause for being
made over.
Castings returned to foundry from shop or customers, through no
fault of foundry, must not be deducted from net foundry castings, but
should be considered as foreign scrap; but if fault of foundry, they
should be charged back to foundry, and considered as foundry return
scrap.
All castings returned by shop or customers, in excess of number
ordered, will be charged to foundry the same as defective castings, and
placed in foundry return scrap, unless otherwise ordered by superin-
tendent.
Sample of Entry
Date
returned
By whom
returned
Description
Cause
Whose fault
Weight,
pounds
April 26, 1909
Our Mach. shop
I S. B. pulley
aexS-aJie
in. bore
Bored too
large
Mach. shop
240
April 29, 1909
Our Mach. shop
I split pulley
24X6 — 2?i6
in. bore
Broke lug
in split-
ting
Mach. shop
120
May 3, 1909
Customer
12 gear castings
P. 2
Cored too
large
Foundry
14
May 5, 1909
Foundry
I D. B. pulley
36X8-21^6
in. bore
Blow hole
in face
Foundry
260
630
Foundry Accounts
WEEKLY FOUNDRY
GoLDENS' Foundry and Machine Co., Columbus, Ga.
For Week Ending Friday, 19
Bad castings returned from foundry.
Total pounds good castings made.
Defective castings returned from shop and customers
Net good castings for week. Total amount ( )
Total pounds pig and foreign scrap charged in cupola.
Net good castings for week.
Per cent lost in renielt, cupola droppings, gangways, etc.
Per cent bad castings, gates, etc., of total melt.
Including foreign scrap, returns and pig.
Average per cent of ca*t-
ings lost.
Remainder.
Total melt.
Net good castings.
Proportionate Wage
Cost Per Hundred
No. Non-producers Wages
Foundry foreman. $
Foundry assistant.
Pulley man.
Crane man.
Wages cost per 1
f hundred pounds | S
Clerk.
net c£istings. )
Cupola tender.
Cupola helpers.
Carpenters.
Watchman.
Total $ J
No. Rumbling Department Wages
Foreman. $ 1
Wages cost per
Assistant.
hundred pounds
Men. J
net castings,
$
Total $
chipped, cleaned,
and ready to ship.
Grand Total Kage Cost
Note. — Castings returned to foundry from our shop and customers, through no
fault of loundo'. must not be deducted from net foundry castings, and should be
Weekly Foundry Report
631
REPORT
■3
C
ca
t-l
1^
p. ai
0 BO
c3;S
c31
3
S
1
h
3-1
CUPOL
A Charge
Pounds pig iron @ per hundred $ i
Cost per hundred ■»
Pounds foreign scrap @ per hundred 1
pounds net castings 1 .
Pounds coke @ per hundred |
including pig iron, |
Total wages $ >
scrap, coke, wages. J
Total
$
Material cost per hundred pounds net castings made as per sheet. $
Total cost per hundred pounds net castings made
as per sheet. $
Poiinds in Different Departments
No. Moulding Department Wages
Moulders (white).
Helpers (white).
Helpers (black).
$
Total $
Wages cost per
hundred pounds
net castings.
'
No. Core Shop
Wages
Foreman.
Core makers.
Help.
S
Total $
Wages cost per
hundred pounds
net castings.
•
No. Night Cleaning Gang Wages
Headman.
Men.
$
Total $
Wages cost per
hundred pounds
net castings.
$
No. Day Cleaning
Gang
Wages
Headman.
Men.
*
$
Total $
Wages cost per'
hundred pounds ,
net castings.
S
per Hundred Pounds $
put in foreign scrap pile. Weekly foundry report, made up from daily foundry re-
port and cupola sheet.
Pounds castings " killed " in machine shop.
u
M
^
P^
Q
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A
Oj
O
8
PU
p
o
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1
sou
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1
i^av/A Joljl. OJOJ
SaUI)St23 13U
Bpunod ooiJad ^sod sd8bm
luaiuvicdop iluipino|^
diqs oj Xpcoj
puc p'oucap 'poddiijD
's8ui5SB3 5.5U spunod ooi j:xl
^so3 aScM luouivicdap auiiqiun-^
saupsBs
53U spunod OOI jad isoa
saSBM sjoonpojd-uox , v
S.iacM pUB 3^103 'dBJOS 'UOJI
8id Suipnput "auiisca
}3U spunod OOI J3d ^so;^
•Di3 "uxniaj -g -J Suipnpui |
•%pm pjo; JO ' ■ 3}3 • S3}t33 ■ 1
•sSuiisBO pcq ;h30 j3J
•Djo "sAbm
-SubS 'sSuiddojp B]OdnD
Ijauiaj ut '-jsoi ^uao aaj
5S0[ s3ui;sB0
snoau-Biiaosiui luao jaj ,
?soi s3ui;sED 1
^so( sSuijstra 1
}SOl S3Ul}SB3 1
snuiuini 1U3D jaj |
linu 3UBD :;U30 ja^j |
gUlldnOO 1U3D J3J 1
Jisoiq -J aU3D JSJ 1
;so] SHUIISBD 1
xoq aaSuttii luaD J3,j |
^soj SSUllSBO 1
ISOl SSUIJSBD 1
3AB3qS ;U33 J3^ 1
jsoi sSuiisea 1
Xajind 1U33 J3j |
^soi s3ui;sB3
1U03 J3d 33rjbAE l^aOX
doqs ourqDTJUi ,
ut panil s8ut'iSE3
jjaoM JO}
S8UI}SB0 p008 53NJ
19 .
Goldens"
Foundry &
Machine Co.
Week
ending
CHAPTER XXVIII
PIG IRON DIRECTORY
The Classification and Directory of Pig Iron Brands given herewith
are taken from Professor Porter's Report.
"Pig Iron is classified as:
First. — Cold, Warm or Hot Blast.
Second. — Coke, Anthracite or Charcoal.
Third. — Sand or Machine.
Fourth. — Basic, Bessemer, Malleable, Foundry or Forge.
"It is only necessary to define the fourth classification as the others
are self-explanatory. "
" Basic iron means primarily one with low silicon. The standard for
this grade having silicon under i per cent and sulphur under 0.05 per
cent."
"Bessemer iron means primarily phosphorus under i per cent. Stand-
ard Bessemer contains from i to 1.25 per cent silicon with sulphur
under 0.05, but the grade is essentially based on low phosphorus. Irons
with extra low phosphorus and variable silicon are sometimes designated
as low phosphorus irons."
" Foundry and Forge Irons embrace practically everything in the way
of ordinary iron, these grades being subdivided on the basis of silicon
and sulphur content."
"The following subclassification of Foundry and Forge iron has been
agreed upon by the blast furnace interests of the districts indicated:
Classification and Grades of Foundry Iron
Southern Points
No. I foundry
No. 2 foundry
No. 3 foundry
No. 4 foundry
Gray forge
No. I soft
No. 2 soft
633
Silicon, per cent Sulphur, per cent
2.75-3.25
.05
and under
2. 25-2. 75
• 05
•* **
1-75-2.25
.06
" "
1.25-2.00
.07
'* '*
I. 25-1. 75
.08
II 1*
3. 00 and over
.05
II .1
2.50-3.25
.05
II 1.
634 I'ig Iron Directory
Classification and Grades of Foundry Iron (Continued)
Eastern Points
No.iX
No. 2X
No. 2 plain
No. 3 foundry
No. 2 mill
Gray forge
Mottled and White by Fracture, Cen
TRAL West and Lake Points
No. I foundry
No. 2 foundry
No. 3 foundry
Gray forge
Buffalo Grading
Scotch
No. I foundry
No. 2 foundry
No. 2 plain
No. 3 foundry
Gray forge
Silicon, per cent
2.7s and up
2 25-2-75
I. 75-2. 25
I 2S-I.7S
1 . 25 and under
1.50 ■•
2-25-2.75
I -75-2.25
1.7s and under
3-00 and over
2.50-3.00
2.0O-2-S0
1.50-2.00
1.50 (under)
Sulphtu", per cent
.0^0 and under
-045 "
.050 "
06s •• ••
06s '• ••
065 and up
-05 and under
OS "
.05 "
. OS and over
-05 and under
.05 "
-OS "
.05 "
.05 "
.05 and (over)
Note. — If sulphur is in excess of maximum, it is graded as lower
grade, regardless of silicon.
"Charcoal is not as a rule graded according to the above table but is
sold by fracture, by analysis, by chill tests, or by some special s\-stem
of grading according to the custom of the maker and demand of the
purchaser. "
" It will be noted that so far as Foundry iron is concerned the grading
system is based exclusively on silicon and sulphur. One reason for
this is that the phosphorus and manganese are fixed by the composition
of the ores used, whereas the silicon and sulphur can be varied at will
by slight changes in the method of operating the furnace. Since in
many, perhaps, the majority of, cases a blast furnace will be limited
to a very few ores as a source of supply, it follows that it will be limited
also in the range of phosphorus and manganese in the iron it produces.
For this reason, a given l^rand of iron will usuall}' run fairly constant
as regards phosphorus and manganese, although its silicon and sulphur
can be varied at the wish of the management. However, this condition,
while common, is not universal, for some concerns possess a variet>' of
ores and can by mi.xing them produce iron of any composition desired.
Coke and Anthracite Irons 635
"In using this directory please bear in mind that it is not infallible.
Much of the data has been difficult to get, a few concerns refusing abso-
lutely to furnish information. Again, in some cases time brings changes
in ownership and character of ore supply, etc., and of course, these
things will affect the character of the product. In spite of these defic-
iencies, however, it is believed that the following tables represent the
most accurate information along these lines available at the present
time and that they will be found of considerable value."
"Finally, it must be emphasized that the use of the data is not to tell
the foundryman the exact analysis of any carload of any brand, but
rather to help him locate those brands which have, or can be made to
have a composition suitable for his work. "
"In these' tables the percentage of sulphur is not usually given. It
should be understood that all furnaces strive for, and usually obtain,
low sulphur in their iron. Practically all foundry grades are sold on the
understanding that the sulphur is under 0.05 per cent and hence no
useful purpose is served in giving the sulphur range except in a very
few cases where it normally runs unusually low."
Coke and Anthracite Irons
Adrian. — Adrian fee., DuBois, Pa. (Adrian fee. Co.)
Hot blast coke, sand cast, foundry iron, from Lake Superior ores.
Sil. 1.0-4.0% Mang. 0.4-1.2% Phos. 0.4-0.9%
Alice. — Alice fee., Birmingham, Ala. (Tenn. Coal, Iron & Ry. Co.)
Hot blast, coke, sand or chill cast iron, from Ala. red and brown ores.
Fdry. Sil. 1.0-4.0% Mang. 0.1-0.4% * Phos. 0.71-0%
Basic Under 1% 0.1-0.4 Under 1%
Alice. — Alice fee., Sharpsville, Pa. (The Youngstown Sheet & Tube
Co.)
Hot blast, coke iron, from Lake Superior ores.
Usually make Bessemer only for use in their own steel works.
Alleghany. — Alleghany fee., Iron Gate, Va. (Oriskany Ore & Iron Co.)
Hot blast, coke, sand cast, foundry iron, from local brown ores.
Sil. 1.0-4.0% Mang. 0.7-1.5% Phos. 0.2-0.6%
Allegheny. — McKeefrey fee., Leetonia, O. (McKeefrey & Co.)
Hot blast, coke, sand cast, foundry iron, from Lake Superior ores.
Sil. 0.7-2.0% Mang. 0.4-0.8% Phos. 0.4-0.7%
* Sometimes higher.
6j6 rig Iron Directory
InJover. — Andovcr fee, Phillipsburg, N. J. (Andover Iron Co.)
Hot blast, coke, sand cast, foundry iron, frum local magnetic ore.
Lake Superior ore, iron nodules and roll scale.
Sil. 1.5-4.0% Mang. 0.6-1.5% Phos. 0.6-0.9%
.4 . R. .\fills. — (2 stacks), Allcntown, Pa. (.\llcntown Rollins Mills Co.)
Hot blast, anthracite and coke iron, from local hematites and N. J.
and N. Y. magnetites.
Ashland. — Ashland fees. (2 stacks), .Ashland, Ky. (..Vshland Iron &
Min. Co.)
Hot blast, raw coal and coke, sand cast iron, from local brown and
Lake Superior ores.
High Sil. Fdry. Sil. 5.0-12.0% Mang. 0.5-0.8% Phos. 0.5-0.9%
Bess. Ferro Sil. 9.0-14.0% 0.5-0.8% under 1.0%
Aurora. — Aurora fee., Columbia, Pa. (Susquehanna Iron Co.)
Hot blast, anthracite and coke, forge and foundry- iron, from native
and Lake Superior ores.
Not in operation, March, 1910.
5a//c//c. — Battelle fee., Battelle, Ala. (Lookout Mt. Iron Co.)
Hot blast, coke, sand cast, foundry' iron, from local red hematite.
Not in operation March, 1910.
Bay View. — Bay\iew fees. (2 stacks), Milwaukee, Wise. (Illinois
Steel Co.)
Hot blast, coke, sand east iron, from Lake Superior ores.
Mall. Bes. Sil. 1.0-3.0% Phos. under 0.20% Mang. 0.50-1.0%
Fdry. 1.0-3.0% over 0.50% 0.50-1.0
Beijonl. — Belfont fee.. Ironton, O. (Belfont Iron Works Co.)
Hot blast, coke, fdry iron, sand east, from Lake Superior and native
ores.
Sil. 1.50-2.50% Phos. 0.40-0.70% Mang. 0.50-0.90%
Bellefonte. — Bellefonte fee., Bellcfonte, Pa. (.BcUefonte Furnace Co.)
Hot blast, coke, sand cast, foundr\' iron, from native and Lake
Superior ores.
Sil. 1.75-4.0% Phos. 0.5-0.7% Mang. 0.5-0.7%
Belmont. — Belmont fee.. Wheeling', W. Va. (\Vhceling Iron & Steel
Co.)
Hot blast, coke, sand east, from Lake Superior ores.
Make only iron for their own steel plant.
Btssenicr. — Bessemer fees. (5 stacks), Bessemer, Ala. (Term. C. I.
& Ry. Co.")
Same as De Bardeleben, which see.
Coke and Anthracite Irons 637
Bessie. — Bessie fee., New Straitsville, O. (Bessie Ferro Silicon Co.)
Hot blast, coke and raw coal, sand cast, ferro silicon, from Lake
Superior low phos. ore.
Sil. 8.0-14.0% Phos. under 0.10% Mang. under 1.0%
Big Stone Gap. — Union fee. No. i. Big Stone Gap, Va. (Union Iron
and Steel Co.)
Hot blast, coke, sand cast, fdry iron, from local fossil brown ores.
Sil. usually high Phos. 0.40-0.80% Mang. 0.40-1.0%
Bird. — Bird fee., Culbertson, O. (The Bird Iron Co.)
Hot blast, coke, sand cast, fdry iron, from Lake Superior and native
ores.
Not in operation March, 1910.
Boyd. — Ashland fees. (2 stacks), Ashland, Ky. (Ashland 1. & Miu.
Co., Inc.)
Hot blast, raw coal and coke, sand cast, fdry iron, from Bath Co.
& Lake Superior ores.
Sil. 1.50-3.0% Phos. 0.40-0.90% Mang. 0.50-0.80%
Brier Hill. — Grace fee., No. 2, Youngstown, O. (The Brier Hill I. &
C. Co.)
Hot blast, coke basic and Bessemer iron, from Lake Superior ores.
Bristol. — Bristol fee., Bristol, Tenn. (Va. Iron, Coal & Coke Co.)
Hot blast, coke, from local brown ores.
Fdry. Sil. 2.0-2.75% Phos. abt. 0.50%
Basic (chill cast) low abt. 0.60%
Mang. abt. 0.75%
1.0-1.50%
Brooke. — Brooke fees. (2 stacks), Birdsboro, Pa. (E. & G. Brooke Co.)
Hot blast, anthracite and coke, from Lake Superior, Newfoundland
and magnetic ores.
Buckeye. — Columbus fees. (2 stacks), Columbus, O. (The Columbus
I. & S. Co.)
Hot blast, coke, chill mold iron, from Lake Superior ores.
Fdry Sil. 1.0-3.0% Phos. 0.40-0.60% Mang. 0.60-0.80%*
Mai. Bes. 0.50-2.50 under 0.20 0.60-1.0. f
Basic under i.o under 0.20 0.80-1.0
Stand. Bes. 1.0-2.0 under o.io
• Sometimes higher. t Higher or lower if desired.
6^}S I'ig Iron Directory
Burttii Vkla. — Bucna Vista ftc, Hiuna Vista, \'a. (Oriskany Ore &
Iron Co.)
Hot hlast, coke, (hill, and sand rait iron, from Oriikany hrown
hematite.
Fdry. Sil. i.o-4.o',c/ I'hos. 0.2-1.0% Mang. 0.6-1.5%
Basic under 1.0 0.2-0.5 0.6-1.5%
Spec, car wheel 1.0-1.50 0.2-0.5 0.6-1.5
/Jh/j/o. — Buffalo Union fee. (3 sUcks), Buffalo, N. V. (The Buffalo
U. F. Co.)
Hot blast, coke, sand cast iron, from Lake Superior ores.
Fdry. Sil. 1.50-3.25% Phos. 0.40-0.70% Mang. 0.50-1.0%
Mai. 0.75-2.0 0.10-0.20 0.40-1.0
Burden. — Burden fee., Troy, N. Y. (The Burden Iron Co.)
Hot blast, mixed anthracite coal and coke, occasionally coke alone.
Magnetic concentrates from northern New York.
Out of operation March, 19 10.
Carbon. — Carbon fee., Perryville, Pa. (Carbon Iron & Steel Co.)
Hot blast, anthracite coal and coke foundry iron, magnetic from
N. J. & Lake Champlain, Lake Superior, and foreign ores.
Sil. 1.50-3.00% Phos. 0.40-0.90% Mang. 0.40-0.90%
Carondelel. — Missouri fee.. So. St. Louis, Mo. (St. Louis Blast Fee.
Co.)
Hot blast, coke, Missouri red and brown hematite.
Analysis refused.
Chaleaiigay. — Standish fee., Standish, N. Y. (Northern Iron Co.)
Hot blast, coke, sand cast, foundry iron, from local magnetic ores.
Sil. 1.0-3.0% Phos. 0.02-0.035% Mang. 0.15-0.50*^0
Chattanooga. — Chattanooga fee., Chattanooga, Tenn. (The Southern
I. & S. Co.)
Hot blast, coke, sand cast, foundry iron, from .Mabama red and
Georgia brown hematite.
Sil. 1.50-3.50% Phos. 1.0-1.5% Mang. 0.6-1.0%*
Cherry Valley. — Cherrj' Vallej' fee., Leetonia, O. (United I. & S. Co.)
Hot blast, coke, sand cast, foundry' iron, from Lake Superior ores.
Sil. as desired Phos. o.20-o.6o'^'o Mang. 0.60-0.80%
Chkkies. — Chickies fees. (2 stacks), Chickies, Pa. (Standard Iron
Min. & Furnace Co.)
Hot blast, anthracite and coke, sand cast, foundr>' iron, from mag-
netites.
* Sometimes higher.
Coke and Anlhracile Irons 639
Citico. — Citico fee., Chattanooga, Tenn. (Citico Furnace Co.)
Plot blast, coke, sand cast, soft foundry, from red and brown hema-
tites from Tennessee and Georgia.
SiL 2.0-3.0% Phos. abt. 1.25% Mang. abt. 0.60%
Claire. — Claire fee., Sharpsville, Pa. (Claire Furnace Co.)
Hot blast, coke, Bessemer iron only, from Lake Superior ores.
Cleveland. — Cleveland fees. (2 stacks), Cleveland, O. (Cleveland Fur-
nace Co.)
Hot blast, coke, from Lake Superior ores.
Analysis refused.
Clifton. — Clifton fees. (2 stacks), Ironton, Alabama. (Alabama Con-
sol. C. & I. Co.)
Hot blast, coke, sand cast, foundry iron, from local brown hematite.
Sil. 1.0-6.0% Phos. c.35-0.70% Mang. 1.0-2.0%
Clima.K. — Hubbard fees. (2 stacks), Hubbard, O. (The Andrews &
Hitchcock I. Co.)
Hot blast, coke, sand cast, strong foundry iron, from Lake Superior
ores.
Sil. 1.35-1-75% Phos. 0.30-0.40% Mang. 0.50-0.80%
Clinton. — Chnton fees., Pittsburgh, Pa. (Clinton I. & S. Co.)
Hot blast, coke, sand cast, foundry iron, from Lake Superior
ores.
Sil. up to 3.0% Phos. 0.20-0.75% Mang. 0.50-1.0%
Colonial. — Colonial fees. (2 alt. stacks), Riddlesburg, Fa. (Colonial
Iron Co.)
Hot blast, coke, sand cast, foundry iron, from Lake Superior and
native ores.
Sil. up to 4.0% Phos. 0.40-0.60% Mang. 0.50-0.80%
Covington. — Covington fee., Covington, Va. (Low Moor Iron Co. of
Va.)
Hot blast, coke, sand cast iron, from native brown hematite.
Fdry. Sil. 1.5-3.0% Phos. 0.90-1.2% Mang. 0.70-1.0%
High Sil. silvery 4.0-8.0 0.90-1.2 0.70-1.0
Cranberry. — Cranberry fee., Johnson City, Tenn. (The Cranberry
Fee. Co )
Hot blast, coke, sand cast, low phos. iron, from local magnetic
ore.
Sil. 1.0-3.5% Phos. under 0.035% Mang. 0.4-0.6%
640 Pig Iron Directory
Crane. — Crane fees. (3 slacks), Catasauqua, Pa. (Emi)irc S. & I. Co.)
Hot l)liisl, anthraritc and coke, sand cast iron, from N. J. m;iKneti< ,
I'a. hematite, Lake .Su|Krior and foreiKn ores.
Fdry. Sil. 0.75-3.50% Phos. o.6o-o.yo% Mang. 0.50-2.0%
Basic under i.o under i.o 0.50-0.80
Low phos. 1.0-3.0 under 0.03 0.50-3.0
Crozer. — Crozer fees. (2 sUcks), Roanoke, Va. (Va. Iron, Coal &
Coke Co.)
Hot blast, coke, sand cast iron, from Va. limonite, mountain and
specular ores.
Fdry. Sil. 2.10-2.75% Phos. 0.60-0.80% Mang. 0.60-0.90%
Basic abt 0.70 abt. 0.70 abt. 1.25
Cumberland. — Cumberland fee., Cumberland Fee. P. O., Tenn. (War-
ner Iron Co.)
Hot blast, coke, sand cast foundry, from local brown and red hema-
tites.
Sil. 2.0-4.5% Phos. abt. 2.0% Mang. abt. 0.30%
Dayton. — Dayton fees. (2 stacks), Dayton, Tenn. (The Dayton C. &
I. Co. Ltd.)
Hot blast, coke, sand cast, foundry- iron, from Tenn. fossil and
Georgia hematite.
De Bardeleben. — Bessemer fees. (.5 stacks), Bessemer, Tenn. (Tenn.
C. L & Ry. Co.)
Hot blast, coke, sand and chill cast iron, from local red and brown
hem.
Fdry. & Mill Sil. up to 3.25% Phos. 0.70-1.0% Mang. 0.10-0.40
Basic up to 1.0 up to 1.0 0.10-0.40
Detroit. — Detroit fee., Detroit, Mich. (Detroit Furnace Co.)
Hot blast, coke, sand cast, foundr>- iron, from Lake Superior ores.
Dora. — Dora fee., Pulaski City, Va. (Va. Iron, Coal & Coke Co.)
Hot blast, coke, sand cast foundrj' iron, from native limonite and
mountain ores.
Sil. 1.50-3.00% Phos. 0.40-0.80% Mang. 0.50-0.90%
Dover. — Dover fee.. Canal Dover, O. (The Pa. Iron & Steel Co.)
Hot blast, coke, sand cast, foundry iron, from Lake Superior ores.
Dunbar. — Dunbar fees. (2 stacks), Dunbar, Pa. (Dunbar Furnace Co.)
Hot blast, coke, sand or machine cast iron, from Lake Superior
specular and soft ores.
Fdry. Sil. 1.5-3.0% Phos. 0.30-0.60% Mang. 0.30-0.60%
Malleable 1.0-2.0 under 0.20 0.30 0.80
Coke and Anthracite Irons 641
Durham. — Durham fee., Riegelsville, Pa. (Durham Iron Co.)
Hot blast, anthracite and coke, sand cast iron, from Lake Superior,
local hematite and New Jersey magnetite.
Eliza. — Pittsburgh fees. (5 stacks), Pittsburgh, Pa. (Jones & Laughlin
St. Co.)
Hot blast, coke, Bessemer and basic, machine cast iron, from Lake
Superior ores.
Ella. — Ella fee., West Middlesex, Pa. (Pickands, Mather & Co.)
Hot blast, coke, foundry and malleable iron, from Lake Superior
ores.
On account of the large assortment of ores available, this furnace
can make practically any desired composition.
EmbreeviUe. — Embreeville fee., Embreeville, Tenn. (Embree Iron Co.)
Hot blast, coke, foundry iron, from local brown hematite.
Empire. — Reading, Pa. (Empire Steel & Iron Co.)
Hot blast, anthracite and coke, foundry iron, from Lake Superior,
Porman and magnetic ores.
Sil. 2.0-3.0% Phos. 1.25-2.50% Mang. 0.50-1.0%
Emporium. — Emporium fee.. Emporium, Pa. (Emporium Iron Co.)
Hot blast, coke, foundry iron, from brown hematite.
Sil. as desired Phos. abt. 0.80% Mang. abt. 0.60%
Ensley. — Ensley fees. (6 stacks), Ensley, Alabama. (Tenn. C. I. &
Ry. Co.)
Hot blast, coke, machine cast iron, from red and brown hematite.
Basic Sil. up to 1.0% Phos. 0.70-1.0% Mang. 0.10-0.40%*
Fdry. & Mill up to 2.50 0.70-1.0 0.10-0.40*
Essex. — Northern fee., Port Henry, N. Y. (Northern Iron Co.)
Hot blast, coke, foundry iron, from local magnetic ores.
Sil. 1.0-2.50% Phos. 0.40-0.90% Mang. 0.10-0.40%
Etowah. — Etowah fees. (2 stacks), Gadsden, Ala. (Ala. Consol.)
Hot blast, coke, foundry iron, from local red and brown hematite.
Sil. i.o-.o6% Phos. 0.70-1.20% Mang. 0.40-0.80%
Eureka. — Same as Oxmoor, which see.
Everett. — Earlston fee., Earleston, Pa. (Jos. E. Thropp.)
Hot blast, coke, foundry iron, from Lake Superior and local brown
ores.
Sil. 1.50-3.50% Phos. 0.40-0.70% Mang. 0.50-0.90%
* Sometimes higher.
642 I'ig Iron Directory
/'iiiniic. — Fannie fee, West Middlcsi-x, Pa. (United Iron & Steel
Co.)
Hot blast, coke, foundry iron, from Lake Sui>crior ores.
Sil. as desired Phos. 0.20-0.60% Mang. 0.60-0.80%
I'cdcral. — Federal fees. (2 stacks), S. Chicago, III. (.Federal Furnace
Co.)
Hot blast, coke, mal. and foundry iron, from Lake Superior ore.
Sil. as desired. Phos. as desired. Mang. as desired.
i'loreiue. — Philadelphia fee., Florence, Ala. (Sloss-Shefl'ield S. & I.
Co.)
Hot blast, coke, sand cast, foundry iron, from .\la. brown hematite.
Sil. as desired. Phos. 0.80-1.25% Mang. 0.40-0.80%
Fort Pill. — Cherry Valley fee., Leetonia, O. (United I. & S. Co.)
Hot blast, coke, spec, car wheel iron, from Lake Superior ore.
Sil. as desired. Phos. 0.20-0.80% Mang. 0.60-0.80%
Franklin. — Franklin fee., Franklin Sprinc;s, N. Y. (I'ranklin Iron
Mfg. Co.)
Hot blast, coke, foundry iron, from fossil, red hematite from Clin-
ton, N. Y.
Not in operation March, 19 10.
511.2.25-3.0% Phos. 1.25-1.50% Mang. 0.25-0.40%
Gem. — Same as Shenandoah, which see.
Genesee. — Genesee fee., Charlotte, N. Y. (Genesee Furnace Co.)
Hot blast, coke, from Lake Superior ore.
Not in operation March, 1910.
Girard. — Mattie fee., Girard, O. (Girard Iron Co.)
Hot blast, coke, foundry iron, from Lake Superior ore.
Sil. 1.50-3.0% Phos. 0.40-0.70% Mang. 0.50-0.80%
Globe. — Globe fee., Jackson, O. (Globe Iron Co.)
Hot blast, raw coal and coke, sand cast, high silicon silvery iron,
from native ores.
Sil. 4.0%-! 2.0% Phos. 0.40-0.80% Mang. 0.40-0.80%
Grafton. — McKeefrey fee., Leetonia, O. (McKeefrey & Co.)
Hot blast, coke, foundry iron, from Lake Superior ores.
Sil. 2.0-2.50% Phos. 0.40-0.70% Mang. 0.40-0.80%
Graham. — Graham fee.,' Graham, Va. (Va. Iron, Coal & Coke Co.)
Hot blast, coke, foundry and basic iron, from Lake Superior and
native brown hematite.
Coke and Anthracite Irons 643
fl^a»w7/ow. — Hamilton fee., Hanging Rock, O. (The Hanging Rock
Iron Co.)
Hot blast, coke, sand cast iron, from native block and limestone
and Lake Superior ores.
Fdry. Sil. as desired. Phos. 0.3-0.4% Mang. 0.5-0.7%
Mall. as desired. under 0.20
Hector. — Clinton fee., Pittsburgh, Pa. (Clinton Iron & St. Co.)
Hot blast, coke, foundry iron, from Lake Superior ores.
Sil. up to 3.50% Phos. 0.50-0.75% Mang. up to 1.0%
Helen. —Helen fee., Clarksville, Tenn. (Red River Furnace Co.)
Hot blast, coke, sand cast soft, fluid foundry iron, from local brown
hematite.
Sil. 2.0-3.0% Phos. abt. 1.25% Mang. 0.40-0.60%
Henry Clay. — Henry Clay fees. (2 stacks), Reading, Pa. (Empire
Steel & Iron Co.)
Hot blast, anthracite coal and coke, foundry and forge iron, from
local hematite and magnetite.
Fdry. Sil. 1.50-4.50% Phos. 2.50-3.50%
Hillman. — Grand River fees. (2 stacks), Grand Rivers, Ky. (Hillman
Land & Iron Co.)
Hot blast, coke, foundry and forge sand cast iron, from local brown
hematite.
Not in operation March, 1910.
Hubbard. — Hubbard fees. (2 stacks), Hubbard, O. (The Andrews &
Hitchcock Iron Co.)
Hot blast, coke, malleable iron, from Lake Superior ore.
Sil. 1.0-2.0% Phos. under 0.20% Mang. under 0.80%
Hubbard Scotch. — Hubbard fees. (2 stacks), Hubbard, O. (The
Andrews & Hitchcock Iron Co.)
Hot blast, coke, soft foundry iron, from Lake Superior ores.
Sil. up to 3.00% Phos. 0.50-0.65% Mang. about 0.60%
Hudson. — Secausus fee., Secausus, N. J. (Hudson Iron Co.)
Hot blast, anthracite coal and coke, foundry iron, from N. Y. mag-
netite, N. J. limonite and Lake Superior ores.
Sil. up to 3-4% Phos. 0.60-0.95% Mang. up to 0.50%
Imperial. — Shelby fee., No. i, Shelby, Ala. (Shelby Iron Co.)
Hot blast, coke, iron from local brown hematite.
Not in operation March, 1910.
Inland. — Inland fee., Indiana Harbor, Ind. (Inland Steel Co.)
Hot blast, coke, basic iron, from Lake Superior ores.
644 I'i^' Iron Directory
Ironalon. — Clifton fees. (2 slacks), Ironaloii, Ala. (Alabama Consol.
C. &. I. Co.;
Hot blast, coke, foundry iron, sand cast, from local brown ore.
Sil. 1.0-6.0% Phos. 0.70-0.90% Mang. 0.70-1.0%
Iroquois. — Iroquois fees. (2 stacks), S. Chicago, III. (Irofjuois Iron
Co.)
Hot blast, coke, foundry iron, from Lake Su[)crior ores.
Sil. 1.35-2.50% Phos. 0.3-0.4%* Mang. 0.40.-0.70%
Ivanhoc. — Ivanhoc fee., Ivanhoe, Va. (Carter Iron Co.)
Hot blast, coke, sand cast, foundry iron, from local and Lake
Superior ores.
Sil. % as desired. Phos. abt. 0.40% Mang. abt. 0.70%
Jenifer. — Jenifer fee., Jenifer, Ala. (Jenifer Iron & Coal Co.)
Hot blast, coke, sand cast, foundry iron from local brown hematite.
Not in operation March, 19 10.
Jisco. — Jisco fee., Jackson, O. Qackson Iron & Steel Co.)
Hot blast, coke and raw coal, high silicon iron, from native and Lake
Superior ores.
Sil. 4.0-14.0% Phos. up to 0.9% Mang. up to 09%
Josephine. — Josephine fee., Josephine, Pa. (Josephine Furnace &
Coke Co.)
Hot blast, coke, sand cast iron, from Lake Superior ores.
Fdry. Sil. up to 4.0% Phos. 0.50-0.80% Alang. under 0.90%
Bessemer 1.25-2.0 0.085-0.10 under 0.90
Juniata. — Marshall fee., Newport, Pa. (Juniata Fee. & Fdry. Co.)
Hot blast, anthracite coal and coke, sand cast, foundry iron, from
local hematite and Lake Superior ores.
Sil. up to 2.0% Phos. under 1.0% Mang. under 1.0%
Lackawanna. — (12 stacks). (Lackawanna Steel Co.)
Lackawanna fees. (7 stacks), Lackawanna, N. Y.
Bird Coleman fees. (2 stacks), Cornwall, Pa.
Colebrook fees. (2 stacks), Lebanon, Pa.
N. Cornwall fee., Cornwall, Pa.
Hot blast, coke, Bes. and basic iron, from Lake Superior and Corn-
wall ores.
Lady Ensley. — Lady Ensley fee., Sheflield, Ala. (Sloss-Sheflield S. &
I. Co.)
Hot blast, coke, sand cast, foundry iron, from local brown hematite.
Sil. as desired. Phos. 1.0-1.50% Mang. 0.50-0.80%
• Sometimes higher.
Coke axid Anthracite Irons 645
La Follette. — La Follette fee., La Follette, Tenn. (La Follette C, I.
& Ry. Co.)
Hot blast, coke, sand cast, foundry iron, from local fossil, red and
brown hematite.
Sil. up to 4.0% Phos. 1.0-1.25% Mang. 0.50-0.75%
L. C. R. — Lebanon, 0. (Lebanon Reduction Co.)
Coke and charcoal, low phos. pig.
Operated for experimental purposes only.
Lebanon Valley. — Lebanon fee., Lebanon, Pa. (Lebanon Valley Fee.
Co.)
Hot blast, anthracite coal and coke, sand cast, foundry iron, prin-
cipally Cornwall ore.
Sil. as desired. Phos. 0.3-0.4% Mang. 0.3-0.4%
Leesport. — Leesport fee., Leesport, Pa. (Leesport Furnace Co.)
Hot blast, anthracite coal and coke, sand east, foundry iron, from
local hematite and magnetite.
Sil. as desired. Phos. 0.2-0.3% Mang. abt. 1.00%
Lehigh. — Lehigh fee., Allentown, Pa. (Lehigh Iron & Steel Co.)
Hot blast, anthracite and coke, sand cast, foundry and mill iron,
from Lake Superior, local hematite and New Jersey magnetite.
Not in operation March, 1910.
Lone Star. — Sam Lanham fee.. Rusk, Texas. (State of Texas.)
Hot blast, coke, from local brown hematite.
Not in operation March, 19 10.
Longdale. — Longdale fee., Longdale, Va. (The Longdale Iron Co.)
Hot blast, coke, chill east iron, from local browTi hematite.
"Basic" Sil. under 1.0% Phos. [0.90-1.0% Mang. 1.0-1.5%
" Off Basic Sil. " 1.0-1.75 0.90-1.0 1.0-1.50
"Off Basic Sul." * 0.25-0.75 0.90-1.0 1.0-1.50
Lowmoor. — Lowmoor fees. (2 alt. stacks), Lowmoor, Va. (Lowmoor
I. Co. of Va.)
Hot blast, coke, sand cast iron, from local brown hematite.
Fdry. Sil. 1.50-3.0% Phos. 0.80-1.0% Mang. 0.90-1.2%
High Sil. silvery 4.0-8.0 0.80-1.0 0.90-1.2
Macungie. — Macungie fee., Maeungie, Pa. (Empire Steel & Iron Co.)
Hot blast, anthracite and coke, sand east, foundry iron, from local
hematites. Lake Superior and foreign ores.
Sil. 0.75-3.50% Phos. 0.60-0.90% Mang. 0.50-2.0%
* Sulphur over .05 per cent.
646 Pig Iron Directory
Mallealilc. — Iroquois fees. (2 stacks), S. Chicago, III. (Iro(juois Iron Co.)
Hot blast, coke, sand cast, foundry iron, from I^kc Suijcrior ores.
Sil. 1.25-2.50% Phos. under 0.2% Mang. 0.40-0.70%
Mannic. — Aliens Creek fees. (2 stacks), Mannic, Tenn. (Bon Air C.
& I. Co.)
Hot blast, coke, sand cast, foundry iron, from local bnjwn hematite.
Sil. uj) to 8.0% Phos. abt. 2.0% Mang. 0.40-0.65%
Marshall. — Marshall fee., New-port, Pa. (Juniata I'ce. & I-dry Co.)
Hot blast, anthracite and coke, sand cast, foundry iron, from local
hematite and Lake Superior ores.
Sil. up to 3.0% Phos. under 1.0% Mang. under 1.0%
Marlins Ferry. — Martin's Ferry fee., Martin's Ferry, \V. Va. (Wheel-
ing Iron & Steel Co.j
Hot blast, coke, Bessemer only, from Lake Superior ores.
Max Meadows. — Max Meadows fee., Ma.x Meadows, Va. (Va. Iron,
Coal & Coke Co.)
Hot blast, coke, sand cast iron, from Va. limonitc and mountain ores.
Fdry. Sil. 1.75-2.75% Phos. 0.40-0.70% Mang. 1.0-2.0%
Basic under 1.0 under i.o Mang. abt. 1.50
Miami. — Hamilton, O. (Hamilton Iron & Steel Co.)
Hot blast, coke, iron, from Lake Superior ores.
Fdry. Sil. 1.0-3.50% Phos. 0.40-0.70% Mang. 0.50-0.80%
Mall. 0.75-2.0 under 0.20 0.60-1.0
Basic under i.o under 0.20 as desired
Missouri. — Missouri fee., S. St. Louis, Mo. (St. Louis Blast Furnace
Co.)
Hot blast, coke, basic iron, from Mo. red and brown hematites.
Analysis refused.
Musconetcong. — Musconetcong fee.. Stanhope, N. J. (Musconetcong
Iron Works.)
Hot blast, anthracite and coke, foundrj" iron, from New Jersey
magnetic, Lake Superior, Cuban and other foreign ores.
Sil. 2.50-3.50% Phos. 0.60-0.70% Mang. 0.60-0.70%
Napier. — Napier fee., Napier, Tenn. (Napier Iron Works.)
Hot blast, coke, foundry iron, from local brown hematite.
Sil. 2.0-2.75% Phos. 0.75-1.50% Mang. 0.40-0.80%
Nellie. — Ironton, O. (The Ironton Iron Co.)
Hot blast, coke, from Lake Superior ores.
Fdry. Sil. 1.25-3.0% Phos. 0.40-0.60%- Mang. 0.50-0.80%
Mall. Bes. 1.0-2.0 under 0.20 0.50-0.90
Coke and Anthracite Irons 647
Nellie. — Alice & Blanche fees. (alt. stacks), Ironton, O. (The Mar-
ting I. & S. Co.)
Hot blast, coke, sand cast iron, from Lake Superior and Kentucky
ores.
Fdry. Sil. 1.0-3.0% Phos. 0.40-0.60% Mang. 0.50-1.0%
Mall. 0.50-3.0 under 0.20 0.50-1.0
Niagara. — Niagara fee., N. Tonawanda, N. Y. (Tonawanda Iron &
Steel Co.)
Hot blast, coke, foundry iron, from Lake Superior hematite.
Analysis refused.
Nittany. — - Same as Bellefonle, which see.
Norton. — Ashland, Ky. (Norton Iron Works.)
Hot blast, coke, mall, and Bess, iron, from Lake Superior ores.
Norway. — Colonial fees. (2 alt. stacks), Riddlesburg, Pa. (Colonial
Iron Co.)
Hot blast, coke, foimdry iron, from Lake Superior and native ores.
Sil. up to 4.0% Phos. 0.60-0.90% Mang. 0.70-1.0%
Oxford. — Oxford fee., Oxford, N. J. (Empire Steel & Iron Co.)
Hot blast, anthracite and coke, basic iron, from local magnetic and
special ores.
Sil. under 1.0% Phos. under 1.0% Mang. 0.75-1.25%
Oxtnoor. — Oxmoor fees. (2 stacks), Oxmoor, Ala. (Term. Coal, I. &
Ry. Co.)
Hot blast, coke, foundry and forge, sand cast, from red and brown
hematite.
Sil. up to 3.50% Phos. 0.70-1.0% Mang. 0.10-0.40%*
Perry. — Carbon fee., Perryville, Pa. (Carbon Iron & Steel Co.)
Hot blast, anthracite and coke, Bess, iron, from Lake Superior,
foreign, Lake Champlain and New Jersey ores.
Paxton. — Paxton fees. (2 stacks), Harrisburg, Pa. (Central I. & S.
Co.)
Hot blast, anthracite and coke, various ores.
Peerless. — Iroquois fees. (2 stacks), S. Chicago, 111. (Iroquois Iron
Co.)
Hot blast, coke, foundry iron, from Lake Superior ores.
Sil. 3.0-3.5% Phos. 0.30-0.40% Mang. 0.40-0.70%
Pencost. — Bessie fee., New Straitsville, O. (Bessie Ferro-Silicon Co.)
Hot blast, coke, ferro-silicon, from Lake Superior ores.
Sil. 5.0-12.0% Phos. 0.30-0.70% Mang. under 1.0%
* Sometimes higher.
648 I'i^ Iron directory
I'lqiiest. — Pequcst fee, Hultzville, N. J. (I'f(|ucst Co.)
IIol blast, anthracite and coke, foundr>' injii, from N. J. magnclic
and manganiferous ores.
Out of blast March, 1910.
Perry. — Perry fee., Krie, Pa. (Perry Iron Co.)
Hot blast, coke, sand cast iron, from Lake Sujwrior ores.
Fdr>-. Sil. 1.75-30% Phos. 0.40-0.70% Mang. 0.40-0.80%
Fdry. 1.00-2.00 1. 15-0.30 0.40-0.80
Special 2.00-3.50 1.00-1.50 0.40-0.80
Pioneer. — Pioneer fees. (3 stacks), Thomas, Ala. (Republic Iron &St. Co.)
Hot blast, coke, foundry iron, from red and brown hematite.
Sil. up to 3-5°%* I'bos. 0.75-0.95% Mang. 0.40-0.80%
Poughkeepsie. — Poughkeepsie fees. (2 stacks), Poughkeepsie, N. Y.
(Poughkeepsie Iron Co.)
Hot blast, anthracite and coke, from Lake Superior, local brown
hematite and Port Henry magnetite ores.
Not in operation March, 1910.
Poughkeepsie. — Poughkeepsie fees. (2 stacks), Poughkeepsie, N. Y.
(Poughkeepsie Iron Co.)
Not in operation March, 1910. (See Poughkeepsie.)
Princess. — Princess fee., Glen Wilton, Va. (Princess Furnace Co.)
Hot blast, coke, foundry iron, from local limonite.
Sil. up to 3.0 or 4.0% Phos. 0.60-0.80^^ Mang. up to 1.0%
Pulaski. — Pulaski fee., Pulaski, City, Va. (Pulaski Iron Co.)
Hot blast, coke, foundry iron, from local brown ores.
Sil. 2.0-3.50% Phos. 0.50-0.80% Mang. 0.40-0.70%
Punxy. — Punxy fee., Punxsutawney, Pa. (Punxsutawney Iron Co.)
Hot blast, coke, foundry iron, from Lake Superior hematite.
Sil. 1.0-4.0% Phos. 0.40-0.60% Mang. 0.45-1.60%
Radford. — Radford Crane fee.. Radford, \'a. (\'a. Iron, Coal & Coke Co.)
Hot blast, coke, foundr>' iron, from \'a. limonite and mounUiin ores.
Sil. 1.5-2.75% Phos. abt. 1.00%. Mang. abt. 1.25%
Rebecca. — Rebecca fees. (2 stacks), Kittanning, Pa. (Kittanning L
& S. Mfg. Co.)
Hot blast, coke, chill cast iron, from Lake Superior ores.
Fdry. Sil. up to 3.0% Phos. 0.40-0.80% Mang. under 1.0%
Basic under i.o under 0.50 under i.o
Mall. 1. 0-1.50 under 0.20 under 1.0
• Sometimes up to 8.00 per cent.
Coke and Athracite Irons 649
Red River. — Helen fee., Clarksville, Tenn. (Red River Furnace Co.)
Hot blast, coke, from local brown hematite.
Fdry. Sil. 2.0- 3.0% Phos. abt. 0.80% Mang. abt. 0.65%
Scotch 3.5- 5.5 abt. 0.80 abt. 0.60
High Silicon 8.0-12.0 abt. 0.80 abt. 0.40
Rising Fawn. — Rising Fawn fee., Rising Fawn, Ga. (Southern I.
& S. Co.)
Hot blast, coke, iron from red and brown hematites.
Not in operation March, 19 10.
Roanoke. — West End fee., Roanoke, Va. (West End Furnace Co.)
Hot blast, coke, foundry iron, from Va. brown hematite.
Sil. as desired. Phos. 0.75-1.0% Mang. 0.50-1.0%
Robesonia. — Robesonia fee., Robesonia, Pa. (Robesonia Iron Co.
Ltd.)
Hot blast, anthracite and coke, foundry iron, from Cornwall ore.
Sil. 2.0-3.50% Phos. under 0.04% Mang. abt. 0.10%
Rockdale. — Rockdale fee., Rockdale, Tenn. (Rockdale Iron Co.)
Hot blast, coke, iron from Tenn. brown hematite.
Fdry. Sil. 2.0 -2.75% Phos. abt. 1.40% Mang. abt. 0.25%
Ferro Phos. 0.07-0.75 17.0-22.0 0.15-0.25
Rockhill. — Rockhill fees., (2 alt. stacks), Rockhill P. O., Pa. (Rockhill
Fee. Co.)
Hot blast, coke, iron from fossil and Lake Superior ores.
Not in operatipn March, 1910.
Rockwood. — Rock wood fees. (2 stacks). Rock wood, Tenn. (Roane
Iron Co.)
Hot blast, coke, foundry iron, from red fossil ore.
Sil. 1.75-2.75% Phos. abt. 1.40% Mang. abt. 0.50%
Sampson Strong. — Upson fee., Cleveland, O. (Upson Net Co.)
Hot blast, coke, foundry iron, from Lake Superior ore.
Sil. 1.5-1.8% Phos. 0.40-0.60% Mang. 0.60-1.0%
Sarah. — Sarah fee., Ironton, O. (The Kelley Nail & Iron Co.)
Hot blast, coke, Bessemer iron, from Lake Superior ore.
Saxton. — Saxton fees. (2 stacks), Saxton, Pa. (Jos. E. Thropp.)
Hot blast, coke, foundry iron, from Lake Superior and local brown
ores.
Sil. 1.5-3.5% Phos. 0.40-0.90% Mang. 0.50-0.90%
Scottdale. — Scottdale fee., Scottdale, Pa. (.Scottdale Furnace Co.)
Hot blast, coke, foundry iron, from Lake Superior ore.
650 Pig Iron Directory
Senega. — McKcefrcy fee., Lcclonia, O. (McKeefrcy & Co.)
Hoi blast, coke, foundry iron, from Lake Suijcrior oroj.
Sil. 1.0-2.0% Phos. under 0.20% Mang. 0.40-0.80%
Sluirpsvilte. — Sharpsvillc fee., Sharpsvillc, Pa. (Shari>sville, Fee. Co.)
Hot blast, coke, mostly Bess, iron, from Lake Superior and New
York magn. ores.
ShtJUld.—Shefheld fees. (3 sUeks), Sheffield, .Via. (Sheffield C. &
L Co.)
Hot blast eoke, foundry iron, from .MabanHi and Tennessee brown
hematites.
Sil. as desired. Phos. abt. 1.0/ (, Mang. abt. 0.50%
Sheffield. — Hattie Ensley fee., Sheffield, .\la. (Sloss-Sheffield S. & L
Co.)
Hot blast, eoke, foundry iron, from loeal brow-n hematite.
Sil. as desired. I^hos. abt. 1.20% Mang. abt. 0.50%
Shetiaiidoah. — Gem fee., Shenandoah, Va. (Oriskany Ore & Iron Co.)
Hot blast, eoke, foundry iron, from loeal brown hem. and Lake
Superior ores.
Sil. as desired. Phos. 0.40-0.80% Mang. 0.60-1.0%
Shenango. — Shenango fees. (5 stacks), Sharpsville, Pa. (Shenango
Fee. Co.)
Hot blast, eoke, basic, chill cast iron, from Lake Superior ores.
Sil. under 1.0% Phos. under 0.05% Mang. 0.70-1.30%
Sheridan. — Sheridan fee., Sheridan, Pa. (Berkshire Iron Works.)
Hot blast, anthracite and coke, foundry iron, sand cast, from Corn-
wall local hematite.
Sil. 1.0-4.0% Phos. 0.40-0.90% Mang. up to 0.75%
Silver Creek. — Rome fee., Rome, Ga. (Silver Creek Furnace Co.)
Hot blast, eoke, sand east, foundry iron, from red and bro\vh hema-
tite, loeal.
Sil. up to 5.0% Phos. under 1.0% Mang. up to 2.0%
Silver Spring. — Paxton fees. (2 stacks), Harrisburg, Pa. (Central
L&S. Co.)
Hot blast, anthracite and coke, foundry iron, from \arious ores.
5/055. — Sloss fees. (4 stacks), Birmingham, .Via. (Sloss-Shellield S.
& L Co.)
Hot blast, coke, foundry iron, from red fossil, hard and soft and
brown hematites.
Sil. as desired. Phos. abt. 0.75% Mang. abt. 0.40%
Coke and Anthracite Irons 651
Soko. — Soho fee., Pittsburg, Pa. (Jones & Laughlin Steel Co.)
Hot blast, coke, basic and Bes. iron, from Lake Superior ores.
South Pittsburgh. — So. Pittsburgh fees. (3 stacks). So. Pittsburgh, Tenn.
(Tenn. Coal, Iron & R.R. Co.)
Hot blast, coke, mill and foundry, sand cast iron, from local hard
red hematite, and brown hematite from Georgia.
Sil. up to 3.50%* Phos. 1.00-1.50% Mang. 0.50-1.50%
Spring Valley. — Spring Valley fee., Spring Valley, Wise. (Spring
Valley Iron & Ore Co.)
Hot blast, coke or sometimes charcoal, sand east iron, from brown
hematite ore.
Mall. Sil. 0.80-1.50% Phos. under 0.20% Mang. 1.0-1.5%
Fdry. 1.5-3.00 under 0.20 1.0-1.50
Standard. — Standard fee., Goodrich, Tenn. (Standard Iron Co.)
Hot blast, coke, foundry iron, from local brown hematite.
Sil. i.75-4-5o% Phos. abt. 0.95% Mang. abt. 0.40%
Star. — Star fee., Jackson, O. (Star Furnace Co.)
Hot blast, raw coal and coke, sand cast, Jackson Co. softener, from
native limonite and block ores.
Sil. 5.00-12.00% Phos. 0.43-0.80% Mang. abt. 0.70%
Star &" Crescent. — Rusk fee., Cherokee Co., Pa. (Frank A. Daniels.)
Hot blast, coke, foundry iron, from local brown hematite and black
ores.
Not in operation March, 1910.
Sterling Scotch. — Iroquois fees. (2 stacks). So. Chicago, 111. (Iroquois
I. Co.)
Hot blast, coke, foundry iron, from Lake Superior ores.
Sil. 2.50-3.0% Phos. 0.30-0.40% Mang. 0.40-0.70%
Stewart. — Stewart fee., Sharon, Pa. (Stewart Iron Co., Ltd.)
Hot blast, coke, sand cast iron, from Lake Superior ores.
Bess. Sil. 1.0-2.50% Phos. 0.09-0.10% Mang. 0.60-0.80%
Low Phos. 1.0-2.50 under 0.04 0.20-0.40
StrutJiers. — Aurora fee., Struthers, O. (The Struthers Fee. Co.)
Hot blast, coke, sand cast iron, from Lake Superior ores.
Ba'sic Sil. under 1.00% Phos. under 0.25% Mang. 0.60-1.2%
Mall. 1.00-1.50 under 0.20 abt. i.o
Susquehanna. — (2 stacks) , Buffalo, N.Y. (Buffalo & Susquehanna I. Co.)
Hot blast, coke, from Lake Superior ores.
Analysis refused.
* Sometimes higher.
6s2 Pig Iron Directory
Swede. — Swede fees. {2 slacks), Swe<lcland, Pa. (Richard Hcckscher
& Sons Co.)
Hot Ijlast, coke, sand cast iron, from Lake Sii|Krior and hi^h grade
foreign ores.
Fdry. Sil. up to 3.25% I'hos. up to 0.80% Mang. up to 0.80%
Basic up to 1.00 up to i.o up to 1.25
Bess. 1.0-2.0 up to 0.10 uj) to 2.0
Low Phos. 1.0-2.50 up to 0.035 up to 4.50
Sj)cc. High Mang. 1.0-1.50 up to 0.80 over 1.50
Sydney. — Mayville fees. (2 stacks], Mayville, Wise. (Northwestern
Iron Co.)
Hot blast, coke, foundry iron, from Lake Superior and local
ores.
Sil. 1.40-2.50% Phos. 0.60-0.80% Mang. 0.50-1.0%
ra//<wfega. — Talladega fee., Talladega, Ala. (Northern .\la. C, L. &:
R.R. Co.)
Hot blast, coke, foundry iron, from native brown ore.
Not in operation March, 1910.
Temple. — Temple fee., Reading, Pa. (Temple Iron Co.)
Hot blast, anthracite and coke, foundry iron, from Lake Superior,
local hematite, N. J. magnetic and foreign ores.
Sil. 1.75-3.50% Phos. 0.60-0.80% Mang. 0.40-0.80%
The .Mary. — Mary fee., Lowellviiie, O. (The Ohio Iron & Steel Co.)
Hot blast, coke, Bessemer only, from Lake Superior ores.
Thomas. — Thomas fee., Milwaukee, Wise. (Thomas Furnace Co.)
Hot blast, coke, sand cast iron, from Lake Superior ores.
Mai. Bess. Sil. 1.00-2.00% Phos. 0.10-0.20% Mang. 0.40-1.75%
Fdry. as desired. 0.15-0.60 0.50-1.25
Thomas. — (9 stacks.) (The Thomas Iron Co.)
Hokendauqua fees. (4 stacks), Hokendauqua, Pa.
Keystone fee. (i stack). Island Park, Pa.
Lock Ridge fees. (2 stacks), Alburtis, Pa.
Saucon fees. (2 stacks), Hellertown. Pa.
Hot blast, anthracite and coke, sand and chill cast iron, from local
brown hematite, N. J. magnetic and foreign ores.
Fdry. Sil. as desired. Phos. 0.60-0.90% Mang. abt. 0.50%
Basic under i.o% under i.o variable
Coke and Anthracite Irons 653
Toledo. — Toledo fees. (2 stacks), Toledo, O. (Toledo Furnace Co.)
Hot blast, coke, sand cast iron, from Lake Superior ores.
Mai. Sil. 1.00-2.00% Phos. under o. 20% Mang. 0.60-1.25%
Basic under I. o under 0.20 0.60-1.25
Fdry. 1.25-2.25 0.50-0.60 0.60-1.25
Scotch 2.25-3.00 0.50-0.60 0.60-1.25
Tonawanda Scotch. — Niagara fees. (2 stacks), N. Tonawanda, N. Y.
(Tonawanda Iron & Steel Co.)
Hot blast, coke, foundry iron, from Lake Superior hematite.
Analysis refused.
Top Mill. — Top fee.. Wheeling, W. Va. (Wheeling Iron & Steel Co.)
Hot blast, coke, Bess, iron, from Lake Superior ores.
Topton. — Topton fee., Topton, Pa. (Empire Steel & Iron Co.)
Hot blast, anthracite and coke, foundry iron, from Lake Superior,
native hematite and magnetite ores.
Sil. 0.75-3.50% Phos. 0.60-0.90% Mang. 0.50-2.00%
Trussville. — Trussville fee., Trussville, Ala. (Southern I. & S. Co.)
Hot blast, coke, sand cast, foundry iron from Alabama red and
Georgia brown hematites.
Sil. up to 3.50% Phos. 0.90-1.20% Mang. 0.50-1.50%
Tuscaloosa. — Central fee.. Holt, Ala. (Central Iron & Coal Co.)
Hot blast, coke, sand east, foundry iron from red and brown hema-
tites.
Sil. 1.25-2.75% Phos. 0.80-1.0% Mang. 0.50-0.90%
Tuscarawas. — Dover fee., Canal Dover, O. (The Penn. I & C. Co.)
Hot blast, coke, foundry iron, from Lake Superior ores.
Union. — Buffalo Union fees. (3 stacks), Buffalo, N. Y. (Buffalo
Union Furnace Co.)
Hot blast, coke, foundry scotch iron, from Lake Superior ores.
Sil. 1.75-2.50% Phos. 1.20-1.50% Mang. 0.50-1.0%
Upson Scotch. — Upson fee., Cleveland, O. (Upson Nut Co.)
Hot blast, coke, foundry iron, from Lake Superior ores.
Sil. 2.0-3.0% Phos. 0.40-0.60% Mang. 0.60-0.90%
Vanderbilt. — Vanderbilt fees. (2 stacks), Birmingham, Ala. (Birm-
ingham C. & I. Co.)
Hot blast, coke, foundry iron, from local hematites.
Sil. up to 4.00% Phos. under 1.00% Mang. 0.40-1.00%
654 l''>i If"" l^ircclory
Vesta. — Vesta fee, Watts, I'a. (Susquehanna Iron Co.)
Hot blast, anthracite and coke, foundry iron, from local hematites
and magnetites.
Not in operation March, lyio.
Victoria. — Victoria fee., CJoshen, Va. (The Goshen Iron Co.)
Hot blast, coke, foundry and forge iron, from brown hematite from
Rich Patch mines.
Sil. as desired. Phos. 0.40-0.80% Mang. 1.0-1.50%
Viking. — Same as Carbon, which sec.
Warner. — Cumberland fee., I)i(kson Co., Tenn. (Warner Iron Co.)
Hot blast, coke, foundry iron, from local red and brown hematite.
Sil. j.0-2.75% Phos. abt. 1.60% Mang. abt. 0.40%
Wardiick. — Warwick fees. (3 stacks), Pottstown, Pa. (Warwick I. &
S. Co.)
Hot blast, coke, machine cast foundry iron, from Lake Superior,
N. Y., New Jersey, and foreign ores.
Sil. i.a-3.0% Phos. 0.40-0.80% Mang. 0.40-0.80%
Walls. — Watts fees. (2 stacks), Middlesborough, Ky. (Va. Coal &
Coke Co.)
Hot blast, coke, foundry iron, from native ores.
Sil. 1.50-2.75% Phos. abt. 0.45% Mang. abt. 0.20%
W elision. — W'eWston fees. (2 stacks), Wellston, O. (Wellston S. &
I. Co.)
Hot blast, coke, sand cast iron, from Lake Superior ores.
Str. fdry. Sil. 1.50-1.75% Phos. 0.18-0.20% Mang. 0.60-0.90%
Mall. 0.60-2.00 under 0.20 0.40-1.00
T^/wr/oH. — Wharton fees. (3 stacks), Wharton, N. J. (Joseph Whar-
ton.)
Hot blast, coke, occasionally some anthracite, from N. J. mag., N. Y.
and Lake Superior hematites.
Wickwirc. — Wickwire fee., Buffalo, N. Y. (Wickwire Steel Co.)
Hot blast, coke, basic iron, from Lake Superior ores.
Williamson. — Williamson fee., Birmingham, .\la. (Williamson Iron
Co.)
Hot blast, coke, iron from red fossil, and brown hematite.
Woodstock. — Woodstock fees. (2 stacks), Anniston, Ala. (Woodstock
I. Wks., Inc.)
Hot blast, coke, foundry iron, from local brown hematite.
Sil. 1.50-5.00%, Phos. abt. 1.15% Mang. 0.80-1.25%
Charcoal Irons 655
Woodward. — Woodward fee., Woodward, Ala. (Woodward Iron Co.)
Hot blast, coke, foundry iron, from local red fossil ores.
Sil. 1.0-3.0% Phos. abt. 0.80% Mang. abt. 0.30%
Zenith. — Zenith fee., W. Duluth, Minn. (Zenith Furnace Co.)
Hot blast, coke, iron, from Lake Superior ores.
Bess. Sil. 1.00-2.00% Phos. 0.08-0.10% Mang. under 1.0%
Mall. 1.00-2.00 under 0.2 0.80-1.20
Fdry. 1.50-5.00 under 0.20 over 0.60
Zug. — Detroit, Mich. (Detroit Iron & Steel Co.)
Hot blast, coke, foundry iron, from Lake Superior ores.
Charcoal Irons
Aetna. — Aetna, Ala. (J. J. Gray.)
Hot or cold blast, charcoal, car wheel iron, from local brown hema-
tite.
Not in operation March, 1910.
Alamo. — Quinn fee., Gadsden, Ala. (Quinn Furnace Co.)
Hot blast, charcoal, foundry iron, from local red and brown hema-
tite.
Not in operation March, 19 10.
Anchor. — Oak Hill, O. (Jefferson Iron Co.)
Warm blast, charcoal, strong foundry iron, from native limestone
and block ores.
Sil. abt. 2.26% Phos. abt. 0.87% Mang. abt. 0.51%
Antrim. — Antrim fee., Mancelona, Mich. (Superior Charcoal Iron Co.)
Hot blast, charcoal, foundry iron, from Lake Superior ores.
Sil. up to 2.62% Phos. 0.15-0.22% Mang. 0.30-0.70%
Berkshire. — Cheshire fee., Cheshire, Mass. (Berkshire Iron Works.)
Warm blast, charcoal, foundry iron, from local red and brown hema-
tite.
Berlin. — Glen Iron fee., Glen Iron, Pa. (John T. Church.)
Cold blast, charcoal, iron from local fossil, and hematite.
Sil. 1.0-1.5% Phos. 0.50-0.65% Mang. 0.40-0.60%
Bloom. — Bloom Switch, 0. (The Clare Iron Co.)
Hot blast, charcoal, foundry iron, from local hematite.
Not in operation March, 1910.
656 rig Iron Directory
Blue Ridge. — Tallapoosji fee, T.illai>fK)sa, Tcnn. (Southern Car Wheel
Iron Co.)
Cold and warm blast, charcoal, iron from brown hematite.
Phos. 0.18-1.50% Mang. up to 2.0%
Biickhorn. — Olive fee., Lawrence Co., O. (McGugin Iron & Coal
Co.)
Hot or cold blast, charcoal iron, from native limestone ore.
Not in operation March, 1910.
Cadillac. — Cadillac fee., Cadillac, Mich. (Milchcll-Diggins Iron Co.)
Hot blast, charcoal iron, from Lake Superior ores.
Sil. up to 2.50% Phos. 0.16-0.20% Mang. up to 1.0%
Center. — Superior P. O., O. (The Superior Portland Cement Co.)
Charcoal iron, from native limestone.
Not in operation March, 1910.
Champion. — Manistique, Mich. (Superior Charcoal Iron Co.)
Warm blast, charcoal, foundry iron from Lake Superior ores.
Sil. up to 2.62% Phos. 0.15-0.22% Mang. 0.30-0.70%
Clierokcc. — Cherokee fee., Cedartown, Ga. (Alabama & Georgia Iron
Co.)
Hot blast, charcoal, sand cast, strong foundry iron, from brown
hematite.
Sil. up to 2.50% Phos. 0.35-0.70% Mang. 0.30-1.60%
CItocolay. — Chocolay fee., Chocolay, Mich. (Lake Superior Iron &
Chemical Co.)
Warm blast, charcoal iron, from Lake Superior ores.
Fdry. Sil. up to 2.0% and over Phos. 0.17-0.22%
Car Wheel 0.05-2.0 and over 0.17-0.22
Mall. 0.17-0.22
Mang. up to 0.65% and over
0.30-0.65 and over
0.30-0.65 and over
Copacke. — Copacke Iron Works, N. Y. (Copacke Iron Works.)
Cold and warm blast, charcoal iron, from N. Y. ores.
Not in operation March, 19 10.
Dover. — Bear Spring fee., Stewart Co., Tcnn. (Dover Iron Co.)
Cold blast, charcoal, foundry iron, from local brown hematite.
Sil. 0.40-2.0% Phos. abt. 0.40% Mang. abt. 0.25%
Charcoal Irons 657
Elk Rapids. — Elk Rapids, Mich. (Superior Charcoal Iron Co.)
Hot blast, charcoal, pig for car wheels and mall., from Lake Superior
ores.
Sil. up to 2.62% Phos. 0.15-0.22% Mang. 0.36-0.70%
Excelsior. — Carp fee., Marquette, Mich. (Superior Charcoal Iron Co.)
Warm blast, charcoal iron, from Lake Superior ores.
Sil. up to 2.62% Phos. 0.15-0.22% Mang. 0.20-0.70%
Gertrude. — Maysville fees. (2 stacks), Maysville, Wise. (Northwest
Iron Co.)
Hot blast, charcoal, foundry iron, from Lake Superior and local
ores.
Sil. 2.50% and over Phos. 0.60-0.80% Mang. 0.50-1.00%
Glen Iron. — Glen Iron fee.. Glen Iron, Pa. (John T. Church.)
Cold blast, charcoal iron, from local fossil and hematite.
Sil. up to 1.00% Phos. 0.70-1.25% Mang. 0.60-1.50%
Hecla. — Heela fee., Milesburg, Pa. (The McCoy-Linn Iron Co.)
Cold blast, charcoal, foundry iron, from Nittany Valley hematite.
Sil. 0.65-1.25% Phos. abt. 0.30% Mang. 0.15-0.25%
Hecla. — Hecla fee., Ironton, O. (Hecla Iron & Mining Co.)
Cold or warm blast, charcoal, foundry iron, from local ore.
Hematite. — Center fee., Center, Ky. (White, Dixon & Co.)
Cold blast, charcoal, foundry iron, from local hematite.
Sil. 0.50-1.40% Phos. 0.25-0.39% Mang. 0.20-0.25%
Hinkle. — Ashland fee., Ashland, Wise. (Lake Superior Iron & Chem-
ical Co.)
Warm blast, charcoal iron, from Lake Superior ores.
Sil. up to 3.00% Phos. 0.10-0.18% Mang. to 0.70% and over
Jefferson. — Jefferson fee., Jefferson, Tex. (Jefferson Iron Co.)
Hot blast, charcoal iron, from local brown hematite.
Not in operation March, 1910.
Liberty 1812. — Liberty fee., Shenandoah Va. (Shenandoah I. & C.
Co., Va.)
Warm blast, charcoal iron, from brown hematite.
Marquette. — Pioneer fee., Marquette, Mich. (Superior Charcoal Iron
Co.)
Hot blast, charcoal, foundry iron, from Lake Superior ore.
Sil. up to 2.62% Phos. 0.15-0.22% Mang. 0.30-0.70%
65S TMk Iron Directory
M'uhigan. — Newberry fee., Newberry, Mi(h. (Superior Char(<jal Iron
Co.)
Warm blast, charcoal iron, from Lake Superior ores.
Sil. u|) to 2.62% Phos. 0.15-0.22% Mang. 0.30-0.70
Muirkirk. — Muirkirk fee., Muirkirk, Md. (Charles E. Coffin.)
Warm blast, charcoal iron, from local carbonate ores.
Sil. 0.70-2.50% Phos. 0.25-0.30% Mang. 0.80-2.50%
Olive. — Olive fee., Lawrence Co., O. (The McGugin I. & C. Co.)
Hot or cold blast, charcoal iron from native limestone ores.
Pine Lake. — Boyne City fee., Boync City, Mich. (Superior Charcoal
Iron Co.)
Hot blast, charcoal iron, from Lake Superior ores.
Sil. up to 2.62% Phos. 0.15-0.22% Mang. 0.30-0.70%
Pioneer. — Pioneer fee., Gladstone, Mich. (Superior Charcoal Iron Co.)
Warm blast, charcoal iron, from Lake Superior ores.
Sil. up to 2.62% Phos. 0.15-0.22% Mang. 0.30-0.70%
Reed Island. — Reed Island fee., Reed Island, Va. (Va. Iron. C. & C. Co.)
Cold blast, charcoal iron, from local limonite.
Richmond. — Richmond fee., Berkshire Co., Mass. (Richmond Iron
Works.)
Warm blast, charcoal iron, from local brown hematite.
Sil. up to 2.00% Phos. 0.28-0.35% Mang. up to 0.44%
Rock Run. — Rock Run fee., Rock Run, Ala. (The Bass Foundry &
Machine Co.)
Warm blast, charcoal iron for chill rolls, car wheels, strong castings,
from local brown hematite.
Sil. 0.30-2.25% Phos. 0.30-0.50% Mang. 0.40-1.00%
Rome. — Rome fee., Rome, Ga. (Silver Creek Furnace Co.)
Warm blast, charcoal iron, from local red and brown hemati£es.
Sil. 1.75-2.25% Phos. 0.35-0.60% ^lang. 0.50-0.80%
Round Mountain. — Round Mt. fee.. Round Mt., .\la. (Round Moun-
tain Iron & Wood .\lc. Co.)
Cold l)last, charcoal iron, from local red hematite.
Not in operation March, 1910.
Salisbury. — Canaan fees.. East Canaan, Conn. (2 slacks). (Bamum
Richardson Co.)
Warm blast, charcoal iron, from Salisbury brown hematite, sand
cast.
Sil. 1.32-1.92% Phos. abt. 0.30% Mang. 0.50-1.0%
Charcoal Irons 659
Salisbury Chatham. — Chatham fee., Chatham, N. Y. (Union Iron &
St. Co.)
Charcoal iron.
Shelby. — Shelby fee., Shelby, Ala. (^Shelby Iron Co.)
Warm blast, charcoal iron, from local brown hematite.
Sil. 0.15-2.25% Phos. 0.30-0.50% Mang. 0.50-0.80%
Sligo. — SHgo fee., Sligo, Mo. (Sligo Furnace Co.)
Hot blast, charcoal iron, from local blue specular and red ore.
Spring Lake. — Fruitport fee., Fruitport, Mich. (Spring Lake Iron
Co.)
Hot blast, sand cast, charcoal iron, from Lake Superior ores.
Sil. up to 2.50% Phos. 0.16-0.20% Mang. up to 1.0%
Spring Valley. — See under Coke Irons.
Tassie Be//. — Tassie Bell fee.. Rusk, Tex. (New Birm. Devel. Co.)
Hot blast, charcoal iron, from local brown hematites.
Not in operation March, 1910.
White Rock. — Smyth Co., Va. (Lobdell Car Wheel Co.)
Warm and cold blast, charcoal iron, from local brown hematite.
All used by the Company.
Wyebrooke. — Isabella fee., Wyebrooke, Pa. (W. M. Potts.)
Cold blast, charcoal iron, from local magnetic and hematites and
foreign and Lake Superior ores.
Not in operation March, 1910.
AUTHORITIES
BOLAND, S.
Buchanan, J. S.
Buchanan, Robert.
Byron, T. H.
"Castings."
Carpenter, H. A.
Carr, W. N.
Christopher, J. E.
Chrystie, J.
Cheney, F. R.
Colby, A. L.
Cook & Hailstone.
Cook, E. S.
Crobaugh, F. L.
Custer, E. A.
Cunningham, R. P.
De Clercy, Jut.es.
Dickinson, W. E.
Diller, H. E.
Fay, A. E.
Field, H. E.
FiRMSTONE, F.
Franklin, B. A.
"The Foundry."
CiLMORE, E. B.
Colden, E. B.
Hall, J. L.
Hatfield, W.
Hawkins, D. S.
HiONEs, A. H.
Holmes, J. A.
Hooper, G. K.
Howe, Prof. H. M.
Hynuman, N. p.
"Iron Age."
"Iron Trade Review."
Jewett, L. C.
Johnson, F.
Johnson, J. E., Jr.
Kane, \V. H.
Keep, W. J.
Kent, Wm.
Kirk, E.
Knoppell, C. E.
Lane, H. M.
Ledebur, Prof. A.
Long, A. T.
Longmuir, p.
Loudon, A. M.
Marshall, S. P.
May, W. J.
McWiLLIAMS & LONGITUIK.
McGahey, C. R.
"Mechanics."
MOLDENKE, Dr. R.
MUMFORD, E. H.
Murphy, Jos. A.
Nagle, a. F.
Outerbridge, a. E.
660
Authorities
66i
Palmer, R. H.
Pierce, E. H.
Porter, Prof. J. J.
Probert, R. H.
Putnam, E. H.
Rankine, Prof. W. J. M.
Ries, Prof. H.
Raup, p. R.
Recketts, Prof. P. C.
Robertson, J. S.
Rogers, S. M.
Rott, Prof. Carl
Rossi, A. G.
Sadlier, J. G.
Saunders, W. M.
Sameur, Prof. A.
Scott, W. G.
Shed, N. W.
SiSSONS, C. W.
Stahlund, Eissen.
Stickle, F. W.
Stupakoff, S. H.
Stead, J. E.
Sleeth, S. D.
Stoughton, Prof. B.
Trautwine, J. C.
Turner, Prof. T.
Taylor, E. M.
West, Thos. D.
Whitehouse, J. S.
Whitney, A. W.
Williams, A. D.
Wangler, J.
WuEST, Prof. F.
Wylie, C.
INDEX
Abbreviations and signs, v.
Acceleration of falling bodies, 191-93.
Accounts, See Foundry accounts.
Acid open hearth, 417, 419, 422.
Acid-resisting-castings, mixture for,
276.
Addition in algebra, 8.
Agricultural castings, average of five
meltings, 459.
Agricultural machinery, mixtures for,
276.
Air, weight of, for combustion, 204;
properties of , 215-18; required for
combustion of one pound each
of coke and coal, 444; loss in
pressure and horse power from
friction in pipes, 447.
.^ir, compressed, horse power required
for, 217-18.
Air cylinders, mixture for, 276
Air furnace, American, 391.
Algebra, 7-15.
Alligation, 5.
Alloys, 222-27.
Aluminum, properties of, 266; in-
fluence of, in cast iron, 266-67.
Aluminum bronze, 226.
American Foundrymen's Association,
See Foundrymen's Association.
American Steel & Wire Co., gauge of
sizes, 146.
Ammonia cylinders, mixture for, 276.
Analysis, mixing iron by, 274-89.
Anchors, gaggers and soldiers, 523-24.
Angle, problems of the, 17-18.
Angles, approximate measurement of,
1 15-16.
Annealing boxes, mixtures for, 277.
Annealing-oven equipped for gas, 392.
Annealing steel castings with micro-
graphs, 400-1.
Anthracite coal, 425.
Antimony, alloys containing, 227.
Apothecaries' or wine measure, 38.
Apothecaries' weight, table of, 36.
Appliances about cupola, 462-67.
Arithmetic, 1-7.
Arnold, Prof. J. O., on carbon in steels,
241, 347; mechanical properties
of normal steels, 396.
Atmosphere, pressure of, at various
readings of barometer, 216.
Authorities, 660-61.
Automobile castings, mixtures for, 277.
Avoirdupois weight, table of, 36.
B.t.u. = British thermal unit, 207.
Babbitt metal, 227.
Baby (Robert) converter, the, 397.
Balls for ball mills, mixture for, 277.
Band and hoop iron weights, 121-
22.
Barometric readings, pressure of at-
mosphere at various, 216; corre-
sponding with different altitudes,
217.
Bars of wrought iron, weight and
areas of square and round, 136-
39.
Basic open hearth, 418, 419, 423.
Bauxite, fire bricks of, 436.
Beams, transverse strength of, for-
mulas for, 188-90.
Bearing-metal alloys, 226.
Bed-plates, mixture for, 277.
Belt velocity, tables of, 229-30.
Belting, formulas for, 227-28.
Benjamin, Charles H., strength of
materials, 213—14.
Bessemer process, the, 396.
Binder bars, 505.
Binders, See Agricultural machinery.
Birmingham gauge for sheet metals
except steel and iron, 120.
Black heart malleable cast iron, 382-
85.
663
664
Index
Ulasi, I ho, in (ho nipola, .i.j'>-.|7; loss
of air pressure from frirtion in
piix's. .J47.
Blast pijR's for pressure blowers,
tables of, 450.
Blow-holes, trouble with, 316; in
steel, 398.
Blowers, pressure, for cupolas, tables
of, 4 •» 8^-4 9-
Board and timber measure, 44.
Board measure, table of, 91—92.
Bod stick, the, 463-64.
Boiler castings, nii.xture for, 277.
Boiling points at sea level, 204; at at-
mospheric pressure, 210.
Bolt ends and lag screws, 158.
Bolt heads and nuts, weights of, 159.
Bolts and nuts, U. S. standard, 150-51.
Bolts, machine, weight of, per 100,
155-56; list prices, 157.
Borings and turnings, melting, 293;
per cent of, 322.
Box strapping, 236.
Brake shoes, mixture for, 287.
Brass, fillets of, areas and weights of,
145-
Brass foundries, alloys in use in, 223.
Brass, moulding sand for, 472.
Brass, sheet and bar, weight of, 144.
Brass tubes, seamless drawn, 167-69.
Brass wire and plates, weight of, 143.
Breaking loads, formula for, 301;
ratio of tensile strength to, 10 to i,
302.
Breast of cupola, 440-41.
Buffalo steel pressure Blowers, 449.
Cables, See Chains and cables.
Cables, transmission or standing,
179-
Calorie, French thermal unit, 207.
Cap screws, 161.
Car castings, mixtures for, 278.
Car wheel iron test bars, moduli of
rupture of, 300.
Car wheels, qualities of iron for, 275;
mixtures for, 278; specifications
for, 350-55.
Carbon and iron, forms of combi-
nation of, 313.
Carbon, combined. See Cementite.
Carbon content in steel, 395.
Carbon, properties of, 252-53; in-
fluence of, as constituent of cast
iron, 253-54; loss or gain of, in
remelting, 254-56.
Carbon, total, jx-'r cent, 308, 310; in
micrographs, 311; ways of re-
ducing, 315-16; for elasticity,
323; reduced for hardness, 328;
high to decrease shrinkage, 332;
high aids fluidity, 335; for re-
sistance to heat, 337-38; for
high permeability. 340; for re-
sistance to corrosion, 341; de-
termination of, 379-So.
Carpenter shop and tool room, 562.
Carr, W. M., open-hearth methods
for steel castings, 411-16.
Carrier, W. H., on foundry heating
and ventilating, 582—86.
Cast iron, constituents of, standard
methods for determining, 377-80:
Silicon, 377-78; sulphur, 378;
phosphorus, 37S; manganese,
379; total carbon, 379-80; graph-
ite, 381.
Cast iron, effect of structure of, upon
its physioil properties, 306-14;
microscopic evidence, 308-12;
Prof. Porter on, 312—14.
Cast iron, fillets of, areas and weights
of, 145-
Cast iron, influence of chemical con-
stituents of, 252-72: Carbon, 252—
56; silicon, 256-60; sulphur,
260-63; phosphorus, 263-64;
manganese, 265-66; aluminum,
266-67, nickel, 267; titanium,
267-68; vanadium, 268-70; ther-
mit, 270; oxygen, 270-71; ni-
trogen. 271-72.
Cast iron, mechanical analysis of,
see Mechanical analysis.
Cast iron, weight of a superficial foot
of, 570.
Casting, direct, 562.
Casting properties of iron, 343-45.
Castings, mixtures for various classes
of. 273-74; (alphabetical) 276-87;
amounts of different irons to be
used found l)y percentage, 2S7-89.
Castings, qualities of iron necessary
for different grades of, 275.
Index
665
Castings, shrinkage of, per foot, 234.
Castings under pressure, 562.
Castings, weight of, determined from
weight of patterns, 569-70; for-
mulas for finding, 570-76.
Cement mortar, tensile strength of,
215-
Cementite (combined carbon), 241;
in micrographs, 308^11; physical
characteristics of, 313; per cent
combined carbon, 315, 319-20,
323; causes hardness, 324-29;
for fusibility, 332-34; low for
fluidity, 335 ; for resistance to
heat low, 337-38; low for per-
meability, 340; in micrographs,
346-49.
Center of gravity, 195-97.
Centigrade to Fahrenheit, equiva-
lent temperatures, 211-12.
Centismal years, 43.
Centrifugal castings, 561-62.
Centrifugal force, 215.
Chain end link and narrow shackle,
174.
Chain hooks, proportions for, 172.
Chains and cables, U. S. Navy stand-
ard, 173.
Chaplets, 528-36; peerless perforated,
530; double head, 531-32;
wrought-iron, 533-35-
Charcoal iron, 250.
Charcoal pig irons, directory of, 655-59.
Charging cupolas, 452-54.
Charging floor, the, 453-54-
Charpy & Grenet's experiments on
irons, 383.
Chemical analyses of cast iron, 3 1 5-49 :
Strength, 315-22; elastic prop-
erties, 322-29; shrinkage, 329—
32; fusibility, 332-34; fluidity,
334-35; resistance to heat, 335-
38; electrical properties, 338-40;
resistance to corrosion, 340-42;
resistance to wear, 342; coeffi-
cient of friction, 342-43; casting
properties, 343-45; micro-struc-
ture, 345-49-
Chemical analyses of test bars, 308—
12; micrographs, 308-11; forms
of combination of iron and car-
bon, 313.
Chemical constituents of cast iron,
influence of the (W. G. Scott),
252.
Chemical reactions in the cupola, 443-
Chilled castings, mixtures for, 274,
275, 278.
Chilled iron defined, 326-28.
Chilled roll (furnace) iron test bars,
moduli of rupture of, 299.
Chills, mixture for, 278.
Chipping and grinding, 566.
Chords for spacing circle, 89-90.
Chords of arcs from one to ninety de-
grees, 88.
Circle, length of chord for spacing,
89-90.
Circle, problems of the, 15, 18-20;
ratio of circumference to di-
ameter, 28; area of, 28.
Circles, areas and circumferences of,
for diameters from 3^^ to 100, by
tenths, 70-79; rules to compute
larger, 79.
Circles, areas and circumferences of,
for diameters in units and eighths,
64-69.
Circular arcs, table of, 80-82.
Circular arcs, table of lengths of, to
radius i, 82-84.
Circular measure, 43.
Circular segments, table of areas of,
84-87.
Cisterns and tanks, number of bar-
rels in, loo-i.
Clamps, 506.
Clarke, D. K., formula for extreme
fibre stress, 304; volume, den-
sity and pressure of air at vari-
ous temperatures, 216.
Cleaning room, the, 563-68; tumblers,
563-66; chipping, grinding, the
sand blast, 566; pickUng, 567;
hydrofluoric acid, 568.
Clout nails, tinned, 536.
Coach screws, gimlet points, 159.
Coke and anthracite pig iron.s, direc-
tory of, 635-55.
Coke, 425-29: Analyses of various
kinds of, 425-26; by-product
coke, 426-27; effect of atmos-
pheric moisture upon, 427;
666
Index
specifications for, by R. Mol-
dcnkc, 428'-29; number of pouiid:<
of iron melted by one pound of,
444-45-
Colby, A L., influence of the mould
upon piR iron, 2.J9.
Coleman, J. J., heat conducting power
of covering materials, 210.
Collars and couplings, mixture for, 27S.
Combining equivalents, 204.
Conductivity of metals, 206, 209.
Cone, the, 32-?3-
Contraction or shrinkage, 329-32.
Converter linings, 404-5; practice,
405-9-
Converter steel, cost of, 420, 421.
Converters, the Baby (Robert) and
Tropenas, 397.
Cook, E. S , on different results from
two irons of same chemical com-
position, 330-32.
Cook, F. J., and G. Hailstone, micro-
scopic evidence why similar irons
have difTerent relative strengths,
306-12, 317-19-
Cooling, influence of rate of, 318.
Cope, formula to find weight re-
quired on a, to resist pressure of
molten metal, 575.
Copper and tin, alloys of, 222.
Copper and zinc, alloys of, 223.
Copper-nickel alloys, 224.
Copper, round bolt, weight of, per
foot, 144.
Copper, tin and zinc, useful alloys of,
22s-
Copper tubes, seamless drawn, 167-69.
Copper wire and plates, weight of, 143.
Core machines, 499.
Core mi.xtures, 480-86.
Core ovens, 492-95.
Core plates and driers, 498-99.
Core room and appurtenances, 492-
500: The oven, 492—96; core
oven carriages, 496; mixing ma-
chines, sand conveyors, rod
straighteners, wire cutter, 497;
sand driers, 498; core plates and
driers, 498-99; core machines,
mould-machines, cranes and
hoists, 499-500.
Core sand with analysis, 479-80.
Corrosion, resistance to, 340-42.
Corrugated iron roofing, weight of,
141.
Cosine, 107.
Cotters, steel spring, 164.
Cotton machinery, mixture for, 278.
Covering materials, heat-conducting
power of, 210.
Cranes and hoists for core room, 499-
500.
Cranes for cupola service, 466.
Cranes for moulding nwm, 502.
Crucible castings, 423.
Crusher jaws, mixture for, 278.
Cube of a whole number ending with
ciphers, to find, 56.
Cube root, 4-5.
Cube root of large number not in
table, to find, 62-63.
Cube roots of numbers from 1000 to
10,000, 57-61.
Cubes and cube roots of numbers
from .01 to 1000, tables of, 46-56.
Cupola, construction of the, 437-52:
Five zones, 437, 442-43; the
lining, 437-39; tuyeres, 439-40;
the breast, 440-4 1 ; sand bottom,
441; chemical reactions in ordi-
nary, 443-45; wind box, 445;
builders' rating, 446; blowers for
the blast, 446-49; diameter of
blast pipes, 450-51; dimensions,
etc., of, 451-52.
Cupola appliances, 462-67: Ladles,
462-65; tapping bar, 463; bod
stick, 464-65; cranes, 466; spill
bed, 466; gagger mould, 467;
rake. 467.
Cupwia charging and melting, 452—61:
The charging floor, 453-54;
tables of meltings and losses, 455-
61; melting ratio, 461.
Cupola makers, best known, 446.
Custer, Edgar A., on permanent
moulds. 559-61.
Cutting tools, mixture for, 278.
Cylinder, the, 32.
Cylinder iron test bars, moduli of
rupture of. 300.
Cylinders or pipes, contents of, 102—3.
Cylinders, locomotive, mixtures for,
273, 282; specifications for, 355.
Index
667
Cylinders, marine and stationary,
mixtures for, 273; see also Cylin-
ders, 279.
Cylinders, solid and hollow iron, for-
mulas for finding weight of, 570-
71-
Decimal equivalents of parts of one
inch, 6.
Deflections, table of, 183-85.
Delta metal, 225.
Diamond polishing wheels, mixture
for, 279.
Dies for drop hammers, mixture for,
279.
Diller, H. E., tests of use of steel scrap
in mixtures of cast iron, 290-91;
on malleable cast iron, 390-91.
Division in algebra, 10.
Dry measure, British Imperial, see
Liquid and dry measures, British
Imperial, 39—40.
Dry measure, table of U. S., 39;
weights of, 39.
Dynamo and motor frames, mixtures
for, 279.
Dynamo frame iron test bars, moduli
of rupture of, 299.
Earth, measurements of, and on the,
238-39-
Eccentric straps, 279.
Elastic properties, 322-23.
Elasticity, modulus of, 181; table of
moduli, 182-83.
Electric furnace steel, cost of, 424.
Electrical and mechanical units, equiv-
alent values of, 220-21.
Electrical castings, mixture for, 279.
Electrical properties, 338-40.
Elimination, 12-13.
Ellipse, construction of an, 21-22;
circumference and area of an,
29.
Ellipse, solid iron, formula to find
weight of a, 571.
Engine castings, mixtures for, 279.
Equations, quadratic, 14-15.
Equations, simple, 11-14; solution
of, 12.
Expansion, lineal, for solids, 205.
Eye bolts, table for, 175.
Facings, 486-87; graphite facing and
analyses, 488-91.
Factors, useful, 44—45.
Fahrenheit to Centigrade, equivalent
temperatures, 211-12.
Falling bodies, acceleration of, for-
mulas and table, 191—92.
Fans and blowers, 280.
Farm implements, mixture for, 280.
Fe-C-Si, influence of, on cast iron,
315, 320.
Ferrite, pure iron, 241, 347.
Field, H. E., on carbon and silicon in
pig iron, 253.
Fillet, cast iron straight, formula to
find weight of a, 574; of a cir-
cular, 575-76.
Fillets of steel, cast iron and brass,
areas and weights of, by E. J.
Lees, 145.
Fire brick, 236.
Fire brick and fire clay, 434-36;
analyses, 434-35; ganister, 435;
fine sand, 435; magnesite, 436;
bauxite, 436.
Fire clays, analysis of, 237.
Fire pots, mixture for, 280.
Flanged fittings, cast iron, 232.
Flasks, 506-18: Wooden cope and
drag, 506-9; iron, 510-14; ster-
ling steel, 515-17; snap, 517-18;
slip boxes, 519; in machine
moulding, 547-So.
Flat rolled iron, see Iron, flat rolled.
Flat rolled steel, see Steel, flat rolled.
Floor plates, grate bars, etc., average
of two meltings, 460.
Fluidity, factors governing, 334-35-
Fluxes, 429-34: Limestone and fluor
spar, 430-31; analyses of slags,
432-33-
Flywheel, cast iron, formulas to find
weight of a, 572-73.
Foot, inches to decimals of a, 6.
Foot pound, the unit of work, 45.
Forces, parallelogram and parallelopi-
pedon of, 192.
Foundry accounts, 587-632: Foundry
requisition, 588-89; pattern card,
589-90; pig iron card, and book,
590, 591; coke card, 591; heat
book, 592-96; cleaning room re-
66S
Tmlex
porti S97I foundry reports, 598-
600; monthly expenditure of
supplies, 601-4; montlily com-
parison of accounts, 605-7; -i"-
nual comparison, 60H-10; chart
of transmission of orders, 611-12;
foundry costs (B. A. Franklin),
612—25; successful foundry cost
system (J. I'. Golden), 625-32.
Foundry cost system, a successful
a. p. Golden), 625-32.
Foundry costs (B. .\. Franklin), 612-
25; outline of scheme, 612-13.
Foundry pig iron, vr Pig iron.
Foundrymen's Association, American,
standard specifications for found-
ry pig iron, 246-48; table of
mixtures for various castings,
275-76; report of committee on
test bars, 294-306.
Fractions, products of, expressed in
decimals, 7.
I-'racture, of pig iron, index of com-
position, 273.
Franklin, B. \., foundry costs, 612-
25; outline of scheme, 612-13.
Frick, Louis H., dimensions of stand-
ard wrot pipe, 167.
Friction clutches, mixture for, 280.
Friction, coefficient of, 215, 342-43.
Frustrum of a cone, 23; center of
gravity of a, 196.
Frustrum of a hexagonal pyramid of
cast iron, formula to 5nd weight
of, 574-
Frustrum of a pyramid, 30-31.
Fuels, foundry, 425-29: .'\nthracite
coal, 425; coke, 425—29.
Furnace castings, mixture for, 2S0.
Furnace temperatures, 206.
Fusibility, or melting point, 332-34.
Gagger mould, 467.
Gaggers, 524.
Galvanized sheet iron, weight of, 141.
Ganister, composition of, 435.
Gas engine cylinders, mixture for, 280.
Gases, specific gravity of, 197.
Gates, tables of areas of, 524-25; top
pouring, 526; whirl, 527; "cross"
skim, 527; horn, 527.
Gears, mixtures for, 280-81.
Geometry, plane, problems in, 15-24.
German silver, 224.
(iolden, J. P., a successful foundry
cost system, 625-32.
Grain structure of cast iron, 329.
Graphite, shown in micrographs, 308-
II, 346-48; physical character-
istics of, 313; per cent of, 315-17.
330-31; size of flakes in relation
to strength, 317-19; per cent of,
for fusibility, 333-34; for resist-
ance to heat, 337-38; low, for
friction, 342.
Graphite facing, with analyses, 488-91.
Grate bars, mixture for, 281.
Gray iron castings, speciBcations for,
296-97.
Grinding machinery, mixture for, 281.
Grinding wheel speeds, table of, 231.
Guldin's theorems, 34.
Gun carriages, mixture for, 281.
Gun iron, mixture for, 281.
Gun iron test bars, moduli of rupture
of, 300.
Gyration, radius of, 197.
Hailstone, G., sec Cook, F. J.
Hangers for shafting, mixture for,
281.
Hardness, control of, 324-28.
Hardware, light, mixture for, 281.
Hatfield, W. H., experiment on de-
flection with six bars, 384; in
breaking bars, 387-8S.
Heat, measurement of, 206-10; radi-
ation of, 208; resistance to, 335-
38.
Heat unit defined, 45.
Heat-resisting iron, mixture for. 281.
Heating and ventilating, 579-86.
Height corresponding to acquired
velocity, 193.
Hemisphere, hollow iron, formula for
finding weight of a, 571.
Hexagon, relations of inscribed, to
circle. 20.
Hoisting rope, pliable wire, 179.
Hollow ware, qualities of iron for,
275: mixture for, 282.
Hooks, slings and chains, 502-3.
Hooper, G. K., on continuous melt-
ing, 554-55-
Index
669
. Horse power defined, 45; required to
compress air, 217—18.
Housings for rolling mills, mixture
for, 282.
Hydraulic cylinders, mixtures for,
282.
Hydraulic pressures, formulas for
dimensions of cast iron pipe to
withstand, 232-33.
Hydrofluoric acid used for pickling,
568.
H5rperbola, the, 23-24.
Inch, one, decimal equivalents of
parts of, 6.
Inches to decimals of a foot, 6.
Inclined plane, 194.
Information, useful, 234-39.
Ingot mould iron test bars, moduli of
rupture of, 299.
Ingot moulds and stools, mixture for,
282.
Iron and carbon, forms of combi-
nation of, 313.
Iron, band and hoop, weights per
lineal foot, 121—22.
Iron, burnt, of no use except for sash
weights, 293.
Iron castings, formulas for finding
weight of, 570-75.
Iron, flat, weight of, per foot, 45.
Iron, flat plates, weight of, per square
foot, 45.
Iron, flat rolled, weights of, per lineal
foot, 123—28; areas of, 129.
Iron, mixing, by fracture, 273-74; by
analysis, 274-89; mixtures for
various classes of castings (al-
phabetical), 276-87.
Iron ores, varieties of, 240.
Iron, physical properties of, 241.
Iron, pig, see Pig iron.
Iron roofing, corrugated, weight of,
141.
Iron, round, weight of, per foot, 45.
Iron, sheet, gauges used by U. S.
mills in rolling, 120; weight per
foot, 141.
Iron, temperatures of, corresponding
to various colors, 239.
Iron wire, gauges and weights of, 146;
list prices of, 147.
Iron, wrought, weight and areas of
square and round bars, 136-39.
Jigs, by S. H. Stupakoff, 540-46.
Jobbing castings, general, average of
five meltings, 455.
Jobbing castings, light, average of four
meltings, 455.
Joule's equivalent, 207.
Keep, W. J., on pig iron cast in iron
moulds and in sand, 249-50; in-
fluence of silicon on cast iron,
259-60; injurious influence of
sulphur, 263; effect of manga-
nese, 266; on recovery of shot
iron, 292; shrinkage of test bars,
371-72; shrinkage chart, 372-74;
strength table, 375; process of
making coke, 426.
Kent, William, altitudes correspond-
ing to barometric readings, 217;
head in feet of water corre-
sponding to pressure, 219; pres-
sure for different heads, 219.
Kettles to stand red heat, mixture
for, 274.
Ladles and table of capacities, 462-65.
Lag screws, 158.
Land measure, table of, 37.
Le Chatelier, M., on furnace tem-
peratures, 206.
Lead pipes, sizes and weights of. 171.
Ledebur, Prof. A., influence of silicon
on annealing temperature, 391.
Lees, Ernest J., areas and weights of
fillets of steel, cast iron and brass,
145-
Lever, the, 194.
Lifting beams, 503-5; table of safe
loads for, 504.
Lighting, importance, 578-79.
Lime mortar, tensile strength of, 215.
Liquid and dry measures, British Im-
perial, weights of, 39-40.
Liquid measure, table of U. S., 38;
weights of volumes of distilled
water, 39-40.
Liquid pressure on moulds, 529—30.
Locks and hinges, see Hardware, light.
Locomotive castings, mixtures for, 282.
670
Index
Locomotive cylinders, mixtures for,
273, 282; specifications for, 355.
Long measure, table of, 36; miscel-
laneous, 37.
Liingmuir, Percy, on the sulphur con-
tent of cast iron, 261-62; micro-
structure of cast iron, 345-49;
on silicon in malleable castings,
386; on steels, 394.
Loudon, A. M., comparative values
of core binders, 481-86.
Lumber, weight of, per icxx> feet
board measure, 93.
McGahey, C. B., tests of use of steel
scrap in mixtures of cast iron, 291.
Machine-cast pig iron, sec Pig iron,
248-50.
Machinery castings, heavy, average
of four meltings, 457.
Machinery castings, light, average of
six meltings, 456.
Machinery castings, qualities of iron
for, 27s; mixtures for, 283.
Machinery iron test bars, moduli of
rupture of, 299, 300.
McWilliams & Longmuir on malleable
castings, 382; on annealing, 400-
i; on moulding machines, 548.
Magnesite, bricks of, 436.
Malleable cast iron, 382-93: Black
heart, 382-S5; experiments on
varying compositions of, 383-8;;
ordinary or Reaumur, 3S5-88;
mixtures in .\merican practice,
389-91; specifications and tests,
391-93-
Manganese, per cent, 308, 310, 315;
high, 322; for elasticity, 323; as
hardening agent, 324-25; in
chilled iron, 328, 337; effect on
grain structure, 329; increases
shrinkage, 332; little effect on
melting point, 334; for heat re-
sistance, 337; low for permeabil-
ity, 340; for acid resistance, 341;
for resistance to wear, 342; skin
effects, 344; in micrographs, 346-
48; determination of, 379.
Manganese, properties of, 265; in-
fluence of, as constituent of cast
iron, 265-66, 272.
Mann, \V. I., lengths of chords for,
spacing circle whose diameter is
I, 90.
Martcnsite "beta" form of iron, 313.
Mayer, Dr. A. M., on radiation of
heat, 208.
Measures, mi.sccllancous, 39; and
weights, 44.
Measures of work, power and duty,
4S-
Measures, sec Weights and measures;
also name of measure, as Dry
measure. Liquid measure, etc.
Mechanical analysis of cast iron, 371—
77; Keep's shrinkage chart, 372—
74; strength table, 375.
Mechanical equivalent of heat, 207.
Melting, continuous, 551-55.
Melting losses in cupolas, tables of,
4S4-6i-
Melting ratio, 461.
Mensuration, 26—34.
Metalloids, influence of the more im-
portant, on combined carbon,
272; method of adding, to the
iron, 465.
Metals, conductivity of, 206, 209;
weights per cubic inch of, 239.
Metals, sheet, Birmingham gauge for,
except steel and iron, 120;
weights of, per square foot, 142.
Metric measures and weights in U. S.
standard, 40-43.
Micrographs of graphite, 308-11.
Micro-structure of cast iron by P.
Longmuir, 345-49-
Mixing machines in core room, 497.
Modulus of elasticity, iSi-83.
Modulus of rupture, 185-86; for-
mula for, 304; in pounds per
square inch, 29S-303.
Moldenkc, Dr. R., effects of titanium
and vanadium in cast iron, 268-70;
on fusibility of cast iron, 332—33;
contents of malleable cast iron,
389; specifications for foundry
coke, 42S-29.
Molten iron, formulas to find i)res-
sure of, 575.
Moment of inertia, 187; of rotating
body, 197.
Moments, location of, iSo.
Index
671
Monomial, 10.
Mortar, lime and cement, tensile
strength of, 215.
Motor frames, see Dynamo.
Mould, pressure on, by molten metal,
formula to find, 575.
Moulding, dry sand, mixtures for
(West), 477-7S.
Moulding machines, 538-50: Jigs by
S. H. Stupakoff, 540-46; flasks,
547-50; diagram of moulding
operations, 549.
Moulding operations, diagram of
(StupakoiT), 549.
Moulding room and fixtures, 501-37:
Cranes, 502; hooks, slings and
chains, 502-3; lifting beams,
503-5; binder bars, 505 ; clamps,
506; flasks, 506-19; pins, plates
and hinges, 519-21; sweeps, 522-
23; anchors, gaggers, and sol-
diers, 523—24; sprues, risers and
gates, 524-27; tables of areas of
gates, 525 ; strainers and spindles,
528; weights, 528; chaplets, 528-
37; liquid pressure on moulds,
529-30; sprue cutters, 537.
Moulding sand, 468-91: Cohesion,
468; permeability and porosity,
468-69; refractoriness, 469; du-
rability, 469; texture, 469, 471;
grades of various, 470; analysis,
47 1 ; sand for brass, with analysis,
472; test bars of green sand,
473~76; for dry sand moulding,
477-79; skin drying, 479; core
sand, and analyses, 479-80;
core mixtures, 480-86; parting
sand, 486; facings, 486-87;
graphite facing, 488; analyses,
488-91.
Moulds, multiple, 555-58; perma-
nent, 558-61; mixtures for per-
manent, 283.
Multiplication in algebra, 8-10.
Nagle, F. A., on erratic results of in-
vestigation of test bars, 298, 301-
3-
Nails, common wire, 148.
Nails, force required to pull, from
various woods, 238.
Nickel, properties of, 267; eflfect of,
in cast iron, 267; imparts most
valuable properties to steel, 267.
Niter pots, see Acid-resisting.
Nitrogen, properties of, 271; effect
of, on cast iron and steel, 271.
Nonconductivity of materials, 209-10.
Novelty iron test bars, moduli of rup-
ture of, 300.
Nuts and bolt heads, weights of, 159.
Nuts and washers, number of, to the
pound, 152.
Open-hearth methods for steel castings
by W. M. Carr, 411-16.
Ordway, Prof., on non-conductivity,
209.
Ornamental work, mixture for, 283.
Outerbridge, A. E., tests of moulding
sands, 473-75.
Oxygen, effect of dissolved oxide on
cast iron, 315, 318, 319, 320.
Oxygen, properties of, 270; cau.ses
foundryman much trouble, 270-
71; effective deoxidizers, 271.
Parabola, the, 22-23.
Parallelogram, area of, 26.
Parenthesis, in algebra, 10.
•Parting sand, 486.
Pattern lumber, specific gravity and
weight per cubic foot of, 569.
Pattern plates, preparation of, 540-46.
Patterns for test bars of cast iron, 297.
Pearlite, a mixture of fernite and
cementite, 241, 347.
Pentagon, to construct a, 20.
Percentage, 5-7.
Permeability and porosity of moulding
sand, 468-69.
Permeability, importance of, 339~40-
Phosphorus, properties of, 263; in-
fluence of, as constituent of cast
iron, 264, 272; per cent, 308, 320-
21; in micrographs, 309-11; low,
for strong castings, 321; and for
elasticity, 323; slight hardemng
effect, 324; slight influence on
chill, 328; decreases shrinkage,
332; increases fusibility, 332-33,
336; keep high for fluidity, 334-
35; low for wear resistance, 342;
67a
Index
presence in microRraphs, ,^46-49;
determination of, ,?7S.
I'hysic.-il constants, tables of, 202-j.
I'iano plates, mixture for, 283.
Pickling, 567-68.
Pig iron, physical properties of, 241-
42; grading, 242—43; foundry,
244-48; machine-cast, 248-50;
charcoal iron, 250; grading scrap
iron, 250-51; fracture of, index
of composition, 273.
Pig iron directory, 633-59: Coke and
anthracite irons, 635-55; char-
coal irons, 655-59.
Pillow blocks, mi.xture for, 284.
Pins, plates and hinges, 519-21.
Pipe and pipe fittings, mixtures for,
284.
Pipe, cast-iron, specifications for, 356-
63; tables of dimensions, 358;
of thicknesses and weights, 359;
volume and weight, 364-65;
pattern, size and weight, 366-70.
Pipes, contents of, 102-3.
Piston rings, mixture for, 284.
Plane figure, irregular, area of any, 27-
28.
Plane figures, properties of, 24-26.
Plane surfaces, mensuration of, 26-29.
Plow points, chilled, mixture for, 284.
Polygon, area of a, 27.
Polyhedra, 31-32.
Polynomials, lo-ii.
Porter, Prof. J. J., effects of sulphur
on cast iron, 262-63; of phos-
phorus, 264; influence of the
metalloids on combined carbon,
272; refwrt on mixtures for
various classes of castings (al-
phabetical), 276-87; on proper-
ties and mixtures of cast iron,
312-14; pig iron classification
and directory, 633-59.
Pouring temperature, influence of,
318.
Powers of quantities, 9-10.
Prince, \V. F., process for melting
borings, 293.
Printing presses, see Machinery cast-
ing.
Prism, the, 30.
I'rismoid, the, 31.
I'robert, Richard H., analysts of iron
for jK'rmanent moulds, 558-59.
Projx'ller wheels, mixture for, 284.
ProiMjrtion, 1-2.
Pulleys, circumferential speed of, 229-
30; rules for speeds and diameters
of, 231; mixtures for, 274, 284-
85-
Pumps, hand, mixture for, 285.
Pyr^nriid, the, 30-31.
Quadratic cquation.s, solution of, 14-
15-
Quadrilateral, area of any, 27.
Quantities, in algebra, 7-10: addition
of like and unlike, S; multi-
plication of simple and com-
pound, 9.
Radiation of heat, 208.
Radiators, mixture for, 285.
Railroad castings, mixture for, 285;
average of three meltings, 459.
Rake, cupola, 467.
Ratio, 1-2.
Reaumur malleable cast iron, 385-88:
Remelting, 385-86; annealing,
386; analyses, 387-88.
Retorts, See Heat resisting castings.
Richards, horsepower required for air
compression and delivery, 217-18.
Ries, Prof. H., analyses of moulding
sands, 472-73.
Rings, cast iron, formulas to find
weight of, 574.
Rivets, iron, round head, 166.
Rolling mill rolls, mixture for, 274.
Rolls, chilled, mixtures for, 274, 275,
285.
Roofing, corrugated iron, weight of,
141.
Roofing, tin and other, 169-70.
Root Positive Rotary Blowers, 449.
Roots of numbers, 3-5.
Rossi, G. A., on effect of titanium in
cast iron, 268.
Rupture, modulus of, 185-S6; for-
mula for, 304.
Sand blast, the, 566.
Sand bottom of cupola, 441.
Sand conveyors and driers, 497, 498.
Index
673
Sand, rammed, to find weight of, 572.
Sand roll iron test bars, moduli of
rupture of, 299.
Sanitary ware, qualities of iron for,
27s; average of eight meltings,
458.
Sash weight, mixture for, 274, 275.
Sash weight iron test bars, moduli of
rupture of, 299.
Scales, mixture for, 285.
Scott, W. G., influence of the chemi-
cal constituents of cast iron, 252.
Scott, W. G., specifications for coke,
426; for moulding sand, 472;
analyses of core sands, 479-89; an-
alysis of Yougheogheney gas coal,
487; analyses of graphite, coke
dust, coal and charcoal, 488-91.
Scott, W. G., specifications for graded
pig irons, 243.
Scrap iron, grading, 250-51.
Secant, the, 108.
Set screws, steel, list price per 100, 160.
Shafting, See Steel shafting.
Sheath, Mr., on continuous melting,
551-54-
Sheet brass and all metals except steel
and iron, Birmingham gauge for,
120.
Sheet iron. See Iron, sheet.
Sheet metals, weights of, per square
foot, 142.
Shot iron, recovering and melting,
291-93.
Shrinkage chart, by W. J. Keep, 372-
374-
Shrinkage of castings per foot, 234.
Shrinkage or contraction, 329—32.
Signs and abbreviations, v.
Silica brick, analysis of, 435.
Silicon, per cent, 308, 310; should be
low, 315, 321; for elasticity, 323;
for hardness, 325; for chill, 327;
decreases shrinkage, 332; little
effect on fusibility, 334; aids
fluidity, 334; favors growth by
repeated heating, 337; increases
permeability, 340; increases acid
resistance, 341; decreases resist-
ance to wear, 342; unrecognizable
in micrographs, 346; determina-
tion of, 377-78.
Silicon, properties of , 256; influence of
as a constituent of cast iron, 256-
60, 272.
Sines, natural, tangents and secants,
107-8; tables of, 110-14.
Skin drying moulds, 479.
Slag car castings, mixture for, 285.
Slags, comparison of analyses of, 432-
33-
Smoke stacks, locomotive. See Loco-
motive castings.
Soil pipe and fittings, mixture for,
286.
Soldiers, 524.
Solids, and their mensuration, 30-34.
Solids, center of gravity of, 196-97;
lineal expansion for, 205.
Specific gravity of various substances,
197-201.
Specifications for steel castings, stand-
ard, 409-11.
Speeds, grinding wheel, 231.
Speeds, surface, rules for obtaining,
232.
Sphere, the, 33-34-
Sphere, hollow iron, formula for find-
ing weight of a, 572; of a solid
iron, 571.
Spheres, table of surface and volumes
of, 93-98-
Spherical segments, cast iron, for-
mulas to find weight of, 573.
Spill bed, 466.
Sprocket wheels for ordinary link
chains, 176—78.
Sprue cutters, steel, 537.
Square measure, tables of, 37-38.
Square of a whole number ending with
ciphers, to find, 56.
Square root, 3-4.
Square root of large number not in
table, to find, 62.
Square roots of numbers from 1000 to
10,000, 57-61.
Squares and square roots of numbers,
of from .01 to 1000, tables of,
46-56.
Stead, J. E., on relations of iron and
phosphorus, 348.
Steam chests, See Locomotive and
Machinery castings.
Steam cylinders, mixtures for, 286.
674
Index
Steel castings in the foundry, .194-416:
Content of carl>()n in varieties,
.<94-<(.s; mcch:iiiiial |)rti|KTlies
"Normal steels," .nj6; Bessemer
process, 396; liaby converter
(Robert), 397; gases in, 398;
chemical changes in Tropenas
converter, 397-99; annealing,
with micrographs, 400-1; Trope-
nas process, 401-3; chemistry of
the process, 403-4; converter
linings, 404-5; converter practice,
40G-9; standard specifications,
409-1 1 ; open-hearth methods by
VV. M. Carr, 411-16.
Steel, comparative cost of, made by
dilTercnt processes (B.Stoughton),
417-24: Acid open hearth, 417,
419, 422; basic open hearth, 418,
419, 423; converter, 420, 421;
crucible castings, 423; electric
furnace, 424.
Steel, fillets of, areas and weights of,
145-
Steel, flat rolled, weights of, per lineal
foot, 130-35-
Steel scrap, use of, in mixtures of
cast iron, 290-gi; points to be
watched in melting, 316—17;
closes the grain, 319; per cent of,
322.
Steel shafting, cold rolled, weights and
areas of, 140.
Steels, mechanical properties of "nor-
mal, " 396.
Steels, unsaturated and supersatu-
rated, 241.
Stoughton, Bradley, tables of com-
parative cost of steel made by
different processes, 417-21.
Stove plate, qualities of iron for, 275;
mi.xture for, 286; average of
three meltings, 457.
Stove-plate iron test bars, moduli of
rupture of, 300.
Straight line, problems of the, 15-17.
Strainers and spindles, 52S.
Straw rope for core bodies, 499.
Strength of beams, transverse, for-
mulas for, 188-90.
Strength of cast iron, nine factors
which influence, 315-22.
Strength of materials, 185-86, 213-14.
Strength table by W. J Keep, 375.
Strengths, transverse, table of, 185-86
StupakolT, S. 11. Chapter on jigs,
540-46.
Sturtevant Steel Pressure Blower, 448.
Subtraction in algebra, 8.
Sulphur, properties of, 260; deleteri-
ous influence of, in cast iron, 261-
63, 272; per cent, 308, 315, 321;
low for elasticity, 323; harden-
ing effect of, 325; increa.ses com-
bined carbon, 327-28; cflecl on
shrinkage, 332; on melting point,
334. 336; low for heat resistance,
337; and for corrosion resistance,
339-42; increases resistance to
wear, 342; causes dirty castings,
343; in micro-structure, 346-48;
determination of, 378.
Sulphuric acid, use of, in pickling,
567-68.
Sweeps, 522-23.
Tacks, length and number of, to
pound, 148.
Tangent, 107.
Tanks, rectangular, capacity of, in
U.S. gallons, 99-100; number of
barrels in, loo-i.
Tapers per foot and corresponding
angles, table of, 117-18.
Tapping bar, 463.
Taylor and White, temperatures cor-
responding to various colors of
heated iron, 239.
Temperatures, equivalent. Centigrade
to Fahrenheit, 211-12.
Temperatures, furnace, 206.
Tensile strength, ratio of, to breaking
loads, 10 to I, 302; I). K.
Clarke's formula for, 304.
Tensile test, size of bar for, 295-97.
Test bars, report on by committee of
.Vmerican Foundrymen's Asso-
ciation, 294-306: Character of
the heats, 294; making of cou-
pons, 295; specifications for gray
iron castings, 296—97; patterns
for, 297; moduli of rupture, 298^
300; erratic results, 298, 301-2;
comparison of, 302-3; casting
Index
67;
defects, 304; circular, 304-6;
microscopical evidence why simi-
lar irons have different relative
strengths, 306-12; Prof. Porter
on the physical properties of cast
iron, 312-14.
Thermit, use of, in the foundry, 270.
Thermometer scales, comparison of,
213.
Threads, U. S. standard, 149.
Thumb screws, 165.
Tin and copper, alloys of, 222.
Tin, copper and zinc, alloys of, 224—25.
Tin, roofing, 169—70.
Tin, sheet, sizes and weight of, 142.
Titanium, properties of, 267; effect
of, in cast iron, 267-68.
Tobin bronze, 225.
Tons, gross, in pounds, 235.
Transverse strength, See Strength.
Transverse test, size of bar for, 295-
98; See Test bars.
Trapezium, area of a, 27.
Trapezoid, area of a, 27.
Triangle, area of a, 26.
Triangle, right-angled, solution of,
109.
Triangles, oblique-angled, solution of,
109.
Tropenas converter, chemical changes
in a, 397.
Tropenas process of steel making,
401-3; chemistry of the process,
403-4-
Troy weight, table of, 36.
Tubes, brass and copper, seamless,
167-69.
Tumblers and tumbling mills, 563-66.
Turn-buckles, drop- forged, 162-63.
Turner, Prof. T., on varieties of pig
iron, 253; percentages of com-
bined carbon, 256; on the use
of silicon, 257-59; phosphorus
in cast iron, 264.
Tuyeres, construction of, in cupola,
439-40.
Two-foot rule, measurement of angles
with, 1 15-16.
Unit of heat, 207.
Units, electrical and mechanical,
equivalent values of, 220-21.
Valves, mixtures for, 286.
Vanadium, properties of, 268; Mol-
denke's experiments on action of,
on cast iron, 269-70.
Ventilating, See Heating and venti-
lating.
Walker, F. G., shrinkage of castings
per foot, 234; weight of castings
determined from weight of pat-
terns, table, 570.
Washer, lock, 153; positive lock,
154-
Washers, wrought steel plate, 153.
Water, distilled, weights of volumes
of, 39-40.
Water heaters, mixtures for, 286.
Water, pressure of, 219.
Water supply, 577—78.
Watts in terms of horse power, 45.
Wear, resistance to, 342.
Weaving machinery. See Machinery
castings.
Wedge, the, 31, 195.
Weight of castings determined from
weight of patterns, 569-70; for-
mulas for finding, 570-76.
Weights, 528.
Weights and measures, 35-45; tables
of various, 46—106.
Wells, contents of linings of, 104-6.
West, Thomas D., on power of cast
iron to stretch, 332.
Wheel and axle, 194.
Wheels, mixtures for, 287.
Whitehouse, J. S., on side blow con-
verters, 404-8.
Willson, E. M., table of tapers per
foot and corresponding angles,
1 1 7-1 8.
Wind box of the cupola, 445-46.
Window glass, panes of, in a box,
236.
Wine measure, table of, 38.
Wire, brass. See Brass.
Wire, copper. See Copper.
Wire, coppered Bessemer spring,
147.
Wire, coppered market, 147.
Wire gauges, different standards for,
119-20.
676
Index
Win-, iron, gauRcs and weights of, t.\Ci;
list prices of, 147.
WlhkI workinK machinery, See Ma-
chinery castings.
W'rut pi[H.-, dimensions of standard,
167-69.
Wrought Iron, See Iron, wrought.
Zinc and copper, alloys of, 223.
Zinc, copper and tin, alloys of, 224—25
Zones in cupola, 437, 442-43.
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