TIM- SCIENTIFIC WORKS OF C. WILLIAM SIEMENS, KT F.K.S., D.C.L., LL.D. CIVIL ENOINEER. UNIFORM WITH THE PRESENT WORK. With Portraits mid Illustrations, 8vo, 16s. LIFE OF SIR WILLIAM SIEMENS, F.E.S., D.C.L., LL.D., Member of Council of the Institution of Civil Engineers. By WILLIAM POLE, F.R.S., Honorary Secretary of the Institution of Civil Engineers. " For many years Sir W. Siemens has been a regular attendant at our meetings, anil to few, indeed, have they been more indebted fur success. Whatever the occasion, lie had always new and interesting ideas, jmt forth in language which a child could understand. It is no exaggeration to say that the life of such a man was spent in the public service." — LI>I:I> RAM.EIGH at Uritish Association, 1SS4. ."Mr. Pole had a straightforwaid story to tell, and has told it in a way likely to interest and instinct a wide circle of readers. Sir William's biography shows him to have been a man of high talent, which under effective discipline and the teachings of experience, was successfully and profitably applied in devising and carrying out undertakings which form marked features in the history of the period with which this biography deals." — Tiiiirx. "So inseparably connected is the career of this remarkable mini with some of the most wonderful inventions of the past half-century, that the narrative of his life is in fact a history of the progress, in this country, of applied science in the two great departments of heat and electricity. As Mr. Pole justly observes, lie was a civil engineer according to the most comprehensive definition of that profession — the art of directing the great powers in Nature for the use and convenience of Man." — .Scofoman. " The most interesting book of the kind that we have read since Xasmyth's delightful autobiography." — futui'ilni/ Jit-rim: "His success in life was doubtless due in no small degree 1o his innate genius, but this would have been unavailing without the energy and deter- mination which accompanied it. The record of his life and work should be vead by every student, and should be in the library of every Mechanics' Institute in the country. " — ISulltlnr. " It is of much more than merely technical or scientific interest his biographer with admirable skill maintains the personal interest of the narrative throughout." — Manclwster GtuinUan. " A story of great interest, one sure to become familiar in English-speak ing households, as well as in those of Germany."— Liverpool Mercury. " The book will be found full of instruction and interest."— Nature. THK SCIENTIFIC WORKS OF C. WILLIAM SIEMENS, KT F.R.S., D.C.L., LL.D. CIVIL ENGINEER. A COLLECTION OF PAPERS AND DISCUSSIONS. EDITED BY E. F. BAMBER, C.E. VOL. I. HEAT AND METALLURGY. WITH 47 PLATES. LONDON : JOHN MURRAY, ALBEMARLE STREET. 1889. [All Rights reserved.] LONDON : BRADBURV, AONEW, ON STEAM ENGINE GOVERNORS . 139, 159 ON THE EJECTOR CONDENSER 157 ON MODERN LOCOMOTIVES 105 ON PEAT-FUEL MACHINERY 166 ON STEAM-ENGINE CONDENSERS 167 ON COMBUSTION OF REFUSE VEGETABLE SUBSTANCES . . . 168 ON EXPERIMENTS ON STEAM BOILERS ... 170 CONTENTS OF VOLUME I. XI MM NI,\V i;i;\ 1.1; .IN<, \ND Kxi'ANsivi; X'.Ai.vi: (\ KAR . . . 178 \S 1'KHDI . 157 ON STEAM-HEATING FOR TOWNS . . ... . . . !!»<> ON An; Ki.ri;n;i;i:ATiN<; M. \cni\KKV 1'.'-' i IN 'in i; 3 METALLURGY. <>.\ ULAST FURNACES 255, 2(54, 273, 276 ON THE STRENGTH OF IRON AND STEEL -'<;;> ON TESTINI; KAILS .271 ON PUDDLING FURNACES 280, 353 ON TIIK MANUFACTURE OF IRON AND STEEL BY DIRECT PRO- CESSES -'503, 328 TIIK PRESIDENT'S (MR. I. LOTHIAN BELL'S) ADDRESS . . . 309 ON Si'lEGELEISEN 311 ON IRON AND STEEL FOR SHIP-BUILDING 313 O.v STEEL MANUFACTURE 315 ON FLUID COMPRESSED STEEL AND GUNS 320 ON A RETORT FURNACE 324 ON ANTHRACITE COKE 325 ON RECENT METALLURGICAL PROCESSES 330 ON USING MOLTEN METAL DIRECT FROM THE BLAST FURNACE . 331 ON CASTING ARRANGEMENTS 335 ON THE PERMANENT WAY OF RAILWAYS 338 ON THE SEPARATION OF CARBON AND IMPURITIES FROM IRON AND STEEL 353 ON THE PRESENTATION OF THE BESSEMER MEDAL TO PROFESSOR TUNNER 3(50 ON THE SEPARATION OF PHOSPHORUS FROM PIG-IRON . . . 3<>2 ON RECENT IMPROVEMENTS IN THE MANUFACTURE OF IRON SPONGE 305 ON STEEL FOR SHIPBUILDING .... :W7, 409, 426, 448 ON STEEL FOR MARINE BOILERS 361) ON THE MECHANICAL AND OTHER PROPERTIES OF IRON AND MILD STEEL, AND THEIR USE IN CONSTRUCTION . . 373. 409 419 Xll CONTENTS OF VOLUME I. PAGE Ox IKON AND STEEL FOR ARCHITECTURAL CONSTRUCTION . . 402 ON THE ELIMINATION OF PHOSPHORUS .... 413, 416, 436 ON IRON AND STEEL AT Low TEMPERATURES 422 ON STEEL COMPRESSION 429 ON HARDENING IRON AND STEEL : ITS CAUSES AND EFFECTS . 433 ON STEEL-MAKING MACHINERY 437 ON THE CORROSION OF IRON AND .STEEL . . . . " . . 440 ON STEEL PLATES .444 ON A MECHANICAL AGITATOR FOR STEEL MANUFACTURE, AND THE DISTRIBUTION OF ELEMENTS IN STEEL INGOTS . . 450 ON THE METALLURGY AND MANUFACTURE OF MODERN BRITISH ORDNANCE 452 ON STEEL FOR STRUCTURES 458 ON THE INFLUENCE OF THE BOARD OF TRADE RULES FOR BOILERS UPON THE COMMERCIAL MARINE 4 ON THE USE OF STEEL CASTINGS IN LIEU OF IRON AND STEEL FORCINGS . 4(U LIST OF ILLUSTKATIONS. HEAT. PLATES REGENERATIVE CONDENSER 1_2 EXPANSION OF STEAM 3—4 CONVERSION OF HEAT INTO DYNAMICAL EFFECT ... 5 REGENERATIVE FURNACK 6 REGENERATIVE GAS FURNACK 7—18 frtiK Producer 7 — 8 Plate Glass Melt in tj Funnier 9 — 13 Ititiuid Flint (iltlx*. Furiinn- 14 — 15 Puddling Furnace 16 — 17 Steel Mi'Uhiij Fin-nun- 18 UNIFORM ROTATION 19 — 22 Oyrometric (ton rnor 20 — 21 Electric Clock 22 STEAM JET 23—30 As Exhauster or liloiccr 23 — 24 Applied to Pneumatic Despatch Tube 25 — 27 Applied to Raise Water 28 For Sugar Evaporating Pan 29 Applied to 6 as Producer 30 HEATED AIR ENGINE 31 — 32 COAL GAS AS FUEL . . . 33—35 Circular Gas Producer 33 Diagram of Gas Production 34 Regenerative Gas Fire and Gas Lamp 35 REFRIGERATING APPARATUS 36 GAS ENGINE 37 XIV LIST OF ILLUSTRATIONS. METALLURGY. PLATES REGENERATIVE GAS FURNACE APPLIED TO MANUFACTURE OP CAST STEEL 38—40 Gas Producer 38 Steel Melting Furnace 39 — 40 ON PUDDLING 41 — 42 Gas Producer 41 Puddling Furnace 42 ON SMELTING IRON AND STEEL 43—45 Steel Melt ing Furnace 43 — 44 Jllaxt Furnace I) tar/ mm ........ 45 ON THE PRODUCTION OP STEEL AND ITS APPLICATION TO MILITARY PURPOSES \\\ — 47 Section of Steel Melting Furnace 4fi Section of Rotator 47 HEAT. SIK WM. SIEMENS, F.E.S. HEAT. CONDENSER FOR LAND AND OTHER STEAM-ENGINES. BY C. W. SIEMENS.* MR. SIEMENS submitted and explained his condenser for land and other steam engines. The action of the condenser is as follows : as the jet of steam passes over the top of the condenser, water is forced through a series of plates, and passes out at the top in a spray at the rate of 3 feet per second. When the water level falls below the bottom of the plates, a jet of water is then thrown across the end of the plates into the water well. The water level falls to its lowest point during about |th part of the stroke of the piston ; during the last |th stroke the water is driven upwards. The lower end of the plates of the condensers are about 150° of heat, the upper portion are about 212°. The ascending water rushes out at a temperature nearly equal to the temperature of the plates themselves. The gases are then carried into the hot well by the succeeding jet of steam. * Copy Extract from Minutes of Committee of Mechanics ot the Society of Arts, May, 1850. VOL. I. B 2 THE SCIENTIFIC PAPERS OF The ejection pipe at the base of the condenser is furnished with an air vessel for the purpose of obtaining a greater force during the time the vacuum is greatest. The whole condenser bears but a small proportion to the size of the cylinder, and there would frequently be room for it within the cylinder. By Mr. Siemens's condenser, about 6 times the quantity of water to condense the steam, about 20 are required by the ordinary process. The principal application of this condenser is looked for in high-pressure engines. One of his condensers at work on 16 horse-power engine made by Cappel. In low-pressure engines there would not be power to force it into the atmosphere. In this engine three condensations take place : one at 180°, this condenses the steam 200°, and the remaining \ in. is steam first cooled by jet ; two, by contact sur- faces ; and third, condensed at its maximum pressure. Mr. Grampian sees nothing opposed to the condenser but the cleaning, and that may easily be managed by simply having a duplicate set of plates. Mr. Glynn quite convinced that the principle involved is one likely to be highly useful. Resolved: — It is the opinion of this Committee that Mr. Siemens's Regenerative Condenser is new, highly ingenious, and appears to be highly valuable in its application to steam engines, and is therefore well entitled to the Society's reward of their Gold Medal. Signed, C. VARLEY. T. E,. CRAMPTON. S/A WILLIAM SIEMENS, F.R.S. ON A NEW REGENERATIVE CONDENSER FOR HIGH- PRESSURE AND LOW-PRESSURE STEAM-ENGINES. BY MR. C. WILLIAM SIEMENS.* THE condenser of a steam engine has for its object the complete discharge of steam from within the working cylinder after it has served to propel the piston. This is effected by conducting the expended steam into a closed chamber, containing an extended' surface of comparatively cool substance, which absorbs the latent heat of the steam and thereby reduces it to its liquid state. Cold water is generally employed for this purpose, which is either brought into immediate contact with the steam, as is the case in Watt's injection condenser ; or through the medium of metallic walls, as in the surface condenser by Hornblower, improved upon by Hall and others. The more or less perfect condensation of the steam depends, first, on the absence of air from the condenser, and secondly, on the temperature at which condensation takes place. The accompanying table shows the elastic force of steam in TABLE OP THE PRESSURE OP THE VAPOUR OP WATER, PROM THE FREEZING TO THK BOILING POINT. Temperature. Fahr. Pressure. Inches of Mercury. Temperature. Fahr. Pressure. Inches of Mercury. 32 0-20 130 4-34 40 0-26 140 5-74 50 0-37 150 7-42 60 0-52 160 9-46 70 0-72 170 12-13 80 1-00 180 15-15 90 1-36 190 19-00 100 1-86 , 200 23-64 110 2-53 210 28-34 120 3-33 212 30-00 vapour, at various temperatures. It will be observed that, in order to produce a perfect vacuum, the water should leave the condenser at about 32° Fahr., or be introduced in the form of ice. * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers, 1851, pp. 18—34. B 2 4 THE SCIENTIFIC PAPERS OP Condensing water, however, is generally obtained at the tempera- ture of about 60° Fahr., and it leaves the condenser at about 110° Fahr., which latter temperature implies a remaining atmos- phere of vapour equal to 2'5 inches of mercury, or in other words a vacuum of 27'5 inches below the atmospheric pressure at 30'0 inches. If a smaller quantity of condensing water be used, it will be raised to a proportionately higher temperature, and a less perfect condensation will be effected. At 212° Fahr. the pressure of the uncondensed vapour would be equal to that of the atmos- phere, and the object of the condenser would be entirely frus- trated. In all cases where an abundant supply of condensing water cannot be obtained, or where the heafc of the steam employed by the engine is reclaimed for other purposes, steam engines are worked without a condensing apparatus, or at high pressure, at the sacrifice of an effective pressure nearly equal to that of the atmosphere upon the working piston. The regenerative con- denser, forming the subject of the present paper, redeems the engine from this waste of heat in the one case and loss of mechanical effect in the other case, being possessed of the peculiar property of returning the condensing and condensed water at the initial temperature of the steam previous to its discharge from the working cylinder, commonly speaking at 212° Fahr. ; producing nevertheless an efficient vacuum. Fig. 1, Plate 1, shows a sectional elevation of the regenerative condenser, as applied to a 10-horse-power high -pressure engine. It consists of an upright rectangular trunk of cast iron A, the lower end B of which is cylindrical, and contains a working piston C. The trunk A is filled with metallic plates D, which are placed upright and parallel to each other, with intervening spaces of not less than 1-1 6th inch in breadth. The upper extremity of the condenser communicates on one side E to the exhaust port of the engine ; and on the other to the hot well F through a valve G. A stop H prevents the opening of the valve beyond a certain distance, in order that it may shut again more instantaneously. The metallic plates D are fastened together by five or more thin bolts, with small washers between the adjacent plates, which keep them the required distance apart. They can easily be removed from the condenser for the purpose of cleaning, by taking off the .S7A' \\'ll.l. I.].M SIEMENS, F.R.S. 5 cover I and drawing out the whole of the plates. An injection K enters the condenser immediately below the plates ; it is with a small air vessel L, and a regulating cock. Various modes have been provided to give motion to the displacing piston C, among which a knee motion worked directly from the beam or crosshead of the engine is generally found the most convenient, as shown at M M in Fig. 1. The action of the condenser is as follows. Motion is given to the displacing piston C by the engine, causing it to accomplish two strokes for every one of the engine. At the moment when the exhaust port of the engine opens, the plates D are completely immersed in water, a small portion of which has entered the passage above the plates at A, and is, together with the air present, carried off, by the rush of steam, through the valve G into the hot well F, where the water remains, while the excess of steam escapes at J into the atmosphere. An instant after the partial discharge of the steam cylinder has commenced, the water recedes between the plates D, and exposes them gradually to the steam, which condenses on them in the manner following. The upper edges of the plates, emerging first from the receding water, are enveloped in steam. of atmospheric pressure, and in condensing a portion thereof they become rapidly heated to nearly the temperature of the steam, or about 210° Fahr. The partial condensation diminishes the density and temperature of the remaining steam, which re- quires additional and cooler surfaces for its further condensation. This is provided for by the continual emerging of additional portions of the metallic surfaces from the receding water. By the time the water level leaves the bottom of the plates, the far greater portion of the steam is condensed. The condensation of the remaining portion of steam could not so readily be accom- plished by means of metallic surfaces ; but the piston C, con- tinuing to descend, causes it to come into immediate contact with the jet of cold water from the pipe K, which completes the vacuum in the manner of a common injection condenser. The air vessel L, connected with the injection pipe, has the effect of accumulating the injection water at the time when the water has ascended between the plates, and of forcing it into the condenser with increased intensity at the time when it is required to com- plete the vacuum. 6 THE SCIENTIFIC PAPERS OF Although the action of this condenser is strictly consecutive, yet it does not check the continuous flow of steam from the cylinder ; and it completes the vacuum when the working piston of the engine has accomplished only one-tenth part of its stroke. Both the engine crank and the crank driving the condenser are on the top centre at the same moment, but the latter completes its revolution in the time of half a revolution of the engine crank ; consequently when the engine piston has passed through only one- tenth of the whole stroke, the condenser crank will have travelled through nearly half its stroke, by which time the whole process of condensation will have been completed. The principal part of the latent beat of the steam is stored up in the plates D, the upper extremities of which are heated to 210° Fahr., and the lower to about 150° Fahr. The water, in ascending again between the plates during the last tenth part of the engine's stroke, absorbs heat from them in a similar successive manner, passing first the coolest and by degrees the hottest portions of their surfaces ; and it issues finally into the upper steam passage A at a temperature approaching the boiling point, at which moment a fresh discharge of steam from the engine takes place, which carries it off into the hot well, as above described, and raises its temperature fully to the boiling point. Fig. 3, Plate 2, represents an actual indicator diagram, show- ing the time occupied in completing the vacuum ; but it will be observed that the loss of time and power may be diminished by increasing the capacity of the displacing cylinder. As it is how- ever, this loss does not amount to one-seventh part of a uniform vacuum, an equivalent for which is obtained in the saving of the power hitherto absorbed by the air pump ; for it will be observed that the displacing piston works between two vacuums, and there- fore meets with no resisting load. The quantity of condensing water required with this condenser to condense 1 Ib. of steam of atmospheric pressure — taking the initial temperature of the condensing water at 60° Fahr., the final temperature at 210° Fahr., and the latent heat of steam of 212° Fahr. at 960 units — is ^,-7^— - = 6*4 Ibs. of water to condense ZiO — bU 1 Ib. of steam. The common injection condenser, supposing the condensing and condensed water to issue at 110° Fahr., requires SSA WILLIAM SIEMENS, F.R.S. ~ 960 + (212 — 110) = 2T2 Ibs. of water to condense 1 Ib. of ll(i — 00 steam, in place of the 6'4 Ibs. which the regenerative condenser requires. In the case of a locomotive or other high-pressure engine, where the steam is released from the cylinder at a pressure of say 80 Ibs. above the atmosphere, two-thirds would be allowed to escape uucondensed, and the vacuum would be obtained with only G'4 -*• 8 = 2*13 Ibs. of condensing water for every 1 Ib. of steam passed through the cylinders. The small quantity of con- densing water required renders the regenerative condenser ap- plicable to engines in nearly every locality ; and pains have been taken to render the apparatus itself equally light and compact. The advantages resulting from the application of the regenerative condenser to high-pressure engines are as follow. 1. Additional effective power, gained on account of the vacuum. The indicator diagram, Fig. 3, Plate 2, illustrates this gain, which, supposing the average steam pressure to be 40 Ibs. above the atmosphere and the vacuum within the cylinder to be 10 Ibs., amounts to 20 per cent, irrespective of expansion. If both the steam pressure and the work on the engine remain unchanged after the condenser is applied, it is evident that the steam may be worked expansively to a large extent without diminishing the absolute driving power of the engine. 2. Heat saved in generating the steam, by the use of boiling-hot feed water ; and the remaining portion of the hot water may be advantageously used for heating buildings, dyeing, &c. High- pressure engines are frequently provided with heating apparatus for the feed water, which heats it on the average to about the temperature of the condensing water from low-pressure engines, or 110° Fahr. The regenerative condenser heats it to 210° Fahr., which constitutes a saving of -- r - = about 10 per cent. When such heating apparatus is not provided, the saving amounts to 210- GO = about 15 per cent. 3. The steam which is not condensed may be used to cause a draught in the chimney, or for other purposes. 4. The displacing cylinder, unlike the air pump of the injection condenser, abstracts no motive power from the engine. 8 THE SCIENTIFIC PAPERS OF 5. The condenser may be started and stopped at any time, by turning the supply of injection water either on or off. If turned on, it at once forms the vacuum, without involving the necessity of blowing through ; and if turned off, it allows the engine to proceed in the same manner as though no condenser had been applied. 6. The air contained in the condenser is at the commencement of each stroke bodily expelled, which is of great advantage to the formation of a good vacuum, instead of the ordinary air pump removing only a portion of the air at each stroke, and consequently leaving a portion always in the condenser. 7. The regenerative condenser is more compact and even less expensive than the ordinary injection condenser, being less than one quarter of the size and having only one valve instead of three. Its proportionate dimensions are as follows : — Area of plate- chamber, three times the area of exhaust pipe ; length of plates, one-quarter to one-third of stroke of engine ; thickness of plates, l-292nd part of their length ; spaces between plates, the same, but never less than 1-1 6th inch, it having been found that the alternate rush of water and condensing steam prevents the settle- ment of grease and earthy matter between the plates, if they are not less than 1-1 6th inch apart : capacity of displacing cylinder, one and a half times the capacity of the plate -chamber. The total capacity of the condenser is equal to only about one-tenth of the capacity of the working cylinder. In applying the regenerative condenser to existing high-pres- sure engines, a saving. of fuel of from 30 to '65 per cent, has been effected, or an increase of power to that amount with the same expenditure of fuel as previously. This saving may however be still augmented considerably, if advantage be taken of the in- creased effective pressure to work the engine expansively. In most cases this may be easily effected, by merely adding to the lap of the slide valve and increasing the lead of the eccentric proportionately, whereby the additional advantage of a more early discharge of the steam is obtained. The first regenerative condenser was attached to a 16-horse- power high-pressure engine at Saltley "Works near Birmingham in September, 1849, where it has been found to answer, although it is not perfect in its proportions, and could not be kept constantly SfX WILLIAM SIEMENS, F.R.S. 9 in operation in consequence of a deficiency of injection water. The actual indicator diagram, shown in Fig. 3, Plate 2, was taken from this engine ; since then several more of the regenera- tive condensers have been erected, and the results above referred to have been obtained. The dotted line in Fig. 8 shows the indicator diagram taken from the engine before the condenser was applied ; and the full line shows the diagram from the engine working with the condenser, and exerting exactly the same power as in the former case. The shaded portion of the diagram shows the power gained or saved by the use of the condenser. The advantages attending the application of the regenerative condenser to stationary engines being practically proved, the author is desirous to extend it also to that important class the locomotive engine. In inviting the attention of railway engineers to this enquiry, he is prepared for practical objections being raised on account of the great rapidity of motion, the necessity for the greatest possible simplicity and lightness, the deficiency of con- densing water, &c. ; but he thinks that the condenser under consideration is peculiarly well adapted to meet these objections. The peculiarities of the regenerative condenser in this respect are as follow. ' It may be accommodated to any speed of piston, by reducing the length and increasing the breadth of the condens- ing plates, thus reducing the velocity of the displacing piston proportionately. Its dimensions are proportionate to the capacity of cylinder only, and not, as in other condensers, to the horse- power of the engine. The total weight of a pair of condensers, as applied to a locomotive engine with cylinders of 13 inches diameter and 20 inches stroke, is about 3£ cwts. The power of the blast remains nearly undiminished. The condenser requires no attention in working the engine, and in case it should fail to act from any accidental cause the engine will continue to work high pressure as usual. Moreover it does not interfere with the working parts of the engine. The advantages which would result from a vacuum in the cylin- der of a locomotive engine have been ably set forth by Mr. Edward "Woods in his " Observations on the consumption of fuel and evaporation of water in locomotive and other steam engines." The present paper may therefore be limited to the means proposed for that purpose. 10 THE SCIENTIFIC PAPERS OF The two condensers are cast in one piece, and placed immediately in front of the cylinders of the engine. Each of them closely resembles the condensers above described ; only the length of the condensing plates and the stroke of the displacing pistons are much reduced in proportion to the steam cylinder stroke, in order that the velocity of the water between the plates may not exceed certain limits. The two displacing pistons are connected to opposite ends of a short vibrating beam, which receives its motion from the engine. In addition to the exhaust valves leading into the hot well, these condensers are provided with a second set of discharge valves, of a somewhat peculiar construction, which with very limited motion combine the advantage of opening a perfectly clear passage for the exhaust steam of the engine into the chimney, where its remaining expansive force is required to produce the draught. Each' of these valves consists of a longitudinal rectan- gular slot, in the upper wall of the steam passage which leads from the cylinder to the condenser. At the ends of the slot are trian- gular pieces, supporting the sides of two longitudinal lips which cover the aperture, except at times when a higher pressure from within forces them open : the extent of their motion is limited by dead stops. The escape of steam, together with the hot water, into the hot well is regulated by a blow-off valve from the hot well into the atmosphere ; by this means a pressure above the atmos- phere is obtained in the hot well, which acts favourably in forcing the boiling-hot condensing water into the feed pump of the boiler. It has been shown previously that the ordinary supply of feed water in locomotive engines, where two-thirds of the steam is allowed to escape uncondensed, is of itself not quite half-sufficient to maintain a vacuum within the condenser, and an additional supply of water must be provided for. But considering how small the excess of condensing water will be, especially if the diameters of the working cylinders are reduced in proportion to the additional effective power gained, and considering that boiling-hot water will readily part with the principal portion of its heat, it is proposed to take the excess of condensing water back to the tender through a simple refrigerator, in which advantage is taken of the rapid motion of the engine through the air for WILLIAM SIEMENS, F.K.S. II cooling the water. The refrigerator may be placed conveniently on the back of the tender. The application of the regenerative condenser to low-pressure engines, as shown in Fig. 2, Plate 1, requires but a short notice after what has been said already ; the letters refer to the same parts as in the former description of the high-pressure condenser shown in Fig. 1. In the low-pressure condenser the steam at the time when it is released from the cylinder has not sufficient force to expel the air and heated water from- the condenser into the atmosphere, and a partially vacuous space must be provided for their reception. For this purpose the side B of the displacing cylinder, which in the arrangement hitherto described is always empty, is put in communication with the exhaust valve G of the condenser, and receives the charge of water and air at the time when the piston C is at the opposite end ; a second valve 0 is provided, through which the water is expelled into the hot well F during the return of the piston C. For the convenience of arrangement, the displacing cylinder is reversed in this case. The chief advantages obtained by the application of this con- denser to the low-pressure engine are : — 1. The requisite amount of injection water is reduced in the proportion of 3 to 1. 2. The feed water of the boiler is obtained nearly boiling hot, which constitutes a saving in fuel of = about 10 per 960 cent. 3. The whole amount of heat generated under the boiler is given off by the engine in the form of water at 210° Fahr., which in most cases may be advantageously employed for heating build- ings, washing, dyeing, and other purposes. 4. A large proportion of the power required for working the air pump is saved. The author proposes to conclude this paper with a short historic sketch of the steam engine condenser, to illustrate the distinct features of this regenerative system. In Newcomen's engine the condensation of the steam was effected by the alternate introduction of a jet of cold water into the steam cylinder itself. The cold water naturally cooled the walls of the cylinder, which in their turn condensed a large portion 12 THE SCIENTIFIC PAPERS OF of the succeeding charge of steam before it had forced the piston upwards. James Watt, in seeking a remedy against this loss of heat, conceived the possibility of condensing the steam in a separate closed vessel ; and in carrying his idea into effect, he not only realised his immediate object, but at the same time rendered the steam engine susceptible of that degree of perfection and general application which it now possesses. The injection condenser of Watt is the most effectual of its kind, and has maintained its exclusive dominion to the present day. It consists of a closed vessel, which communicates periodically with the steam cylinder. The injection water, together with the condensed steam and the air, which last is partly evolved from the injection water and partly leaks in through the joints of the cylinder and exhaust pipe, are continually discharged from it by means of the air pump. Shortly after the introduction of Watt's condenser, a surface condenser was proposed by Hornblower, which consisted of a close annular vessel of thin metal plate, on the inner surfaces of which the waste steam of the engine was condensed ; its latent heat being continually carried off by a stream of cold water which surrounded the vessel. A comparatively small air pump was provided, which served to discharge the condensed water (to be again forced into the boiler) and any air that might leak in through the joints. This condenser failed in practice, for want of sufficient extent of cooling surface. An effective surface condenser would possess considerable advan- tages over the injection condenser, especially in the case of marine engines. Allowing the condensed steam to be continually returned into the boiler, it prevents incrustation of the boiler, and moreover dispenses with the necessity of blowing off. Its air pump absorbs a much smaller proportion of the power of the engine, and its functions require less personal attention. Stimulated by these considerations, several attempts were made to improve on Horn- blower's invention ; but since all these improvements partake very much of the same character, it is thought sufficient for the present purpose to mention only Hall's condenser, which has obtained the greatest amount of notoriety. It consists of two flat chests or closed chambers, connected together by means of a large number of brass tubes, through which the condensing steam \\-II.I.lAM SIEMENS, F.R.S. 13 circulates. These tubes are surrounded by cold water, which fills up the space between the flat chests. A small air pump removes the condensed water and air from the lower chest. The great weight and cost of this condenser, its liability to derangement, and the impossibility of removing the calcareous deposit of the water from the tubes without taking the whole fabric to pieces, are found to be serious practical objections. In the year 1847 the author had occasion to apply a surface condenser in a situation where economy of space and material were essential. In considering the most rational distribution of surfaces, he happened to find an arrangement which, with less than one half the amount of material used in Hall's condenser, produced a very satisfactory result, and which paved the way to the more important improvement chat forms the principal subject of this paper. The surface, condenser referred to, shown in Figs. 4 and 5, Plate 2, consists of a number of copper plates A A, of ^Vnds inch thickness and about 4£ inches broad by 2 feet long, which are fixed together by two longitudinal flattened wires of the same metal between the adjacent plates ; and the whole pile is screwed up tight together between the sides of a rectangular cast iron vessel, which constitutes the body of the condenser. The ends of the plates project through the top and bottom of the condenser, and are planed flush with its exterior surfaces. The joints at top and bottom are secured by means of india-rubber rings, which are screwed down under small cast iron frames, and yield to the difference of expansion between the two metals. The flattened wires are laid parallel, about 3 inches apart from each other, and form with the plates a large number of narrow passages, through which the cold condensing water flows in a vertical direction, without entering the vacuous space of the condenser, into which the edges of the plates outside the flattened wires project, forming the condensing surfaces. The rationale of this condenser is as follows. The transmission of heat in a surface condenser is threefold : first, from the con- densing steam to the internal metal surfaces ; secondly, from the internal surfaces through the body of the metal to its external surfaces ; and thirdly, from the external surfaces to the surround- ing water by which it is carried off. The first operation (condensa- 14 THE SCIENTIFIC PAPERS OF tion) would, it is presumed, proceed with undefined rapidity, if it were not retarded by the second and third, or by the presence of some permanent gases, which accumulate on the condensing surfaces and prevent their immediate contact with the steam. The second (conduction) varies in direct proportion with the conduct- ing power of the metal, and with its thickness ; but the conducting power of copper is so great that its thickness seems to exercise no appreciable influence on the amount of heat transmitted in a given time. This interesting fact is proved by Dr. lire's experiment with two copper pans, of the same internal area, but very unequal thickness of bottom, the thicknesses being in the proportion of I to 12 ; which were both filled with water, and dipped into a hot solution of muriate of lime. It was found that the water in the thick pan evaporated the quickest, which may be accounted for by its slightly increased external surface in contact with the heating solution ; and this affords additional evidence that the limit of transmission does not lie within the metal, but rather between the metal surface and the liquid. That the absorption of the heat by the water is a slow process may be inferred from the circumstance that water, although possessing a large capacity for heat, is a very bad conductor, and depends for its power to absorb heat on the slow circulation over the heating surface caused by the lower specific gravity of the heated particles of water. A strong artificial current along the heating surfaces greatly accelerates the process. The surface condenser above described was arranged in accord- ance with these observations. It contains : — heat-absorbing surfaces (by the water), 18 square feet per horse power ; condensing sur- faces, 9 square feet per horse power ; computed mean thickness of metal through which the heat is transmitted, 1| inch ; weight of copper, 60 Ibs. per horse power ; space occupied by plates, 0'4 cubic foot per horse power, or about one-tenth of the space occupied by the tubes in the tubular condenser. The essential features of this condenser are its comparative cheapness of construction, and the easy access which it affords to the water channels between the plates. It also requires less con- densing water than previous surface condensers, in consequence of the repeated and close contact in which each particle is brought with the heating surfaces, before it can reach the upper reservoir or hot well. The author considers that the surface condenser just SIR WILLIAM SIEMENS, F.R.S. 15 described may be advantageously applied to marine engines ; and not being subject to a patent, he hopes it will receive a sufficient trial. I'.cing required to save the waste steam of a low-pressure engine in the form of slightly heated water, for Mr. John Graham of Manchester, the author in the spring of 1847 conceived the idea of a regenerative condenser. Figs. 4 and 5, Plate 2, show his first arrangement as already described, which may be termed a regenerative surface condenser. It consists of a revolving valve B, which admits the waste steam of the engine first to the atmos- phere at C, and then successively into the separate compartments, D, E, F, G, where it is condensed at various densities. The cold water enters at H, and first passes between the plates within the last compartment G, and by degrees through those within the first compartment D, where the steam is of nearly atmospheric pressure, and consequently heats the water to nearly 212° Fahr., when it passes out at I. The next step was a regenerative injection condenser on the same principle, as represented by Fig. 6, Plate 2. The revolving valve B admits the waste steam of the engine first to the atmos- phere at C, and then successively into the separate compartments, D, E, F, G, where it is condensed at various densities. The cold water is injected at H, and is passed down through the steam in each compartment in succession by means of the displacing pistons K K, which work all on the same piston rod through each of the divisions between the compartments ; and the heated water passes out at the bottom at I. L L are overflowing distributing trays, for the purpose of bringing the water more rapidly and completely into contact with the steam. M is a small pump to extract the air that is mixed with the steam and water. The regenerative condenser in its present form partakes of the nature of both the surface and the injection condensers. Attempts have been made from time to time to condense the steam of a high-pressure engine without the aid of an air pump, by blowing the steam into a small injection condenser which is provided with a large exhaust valve. It is clear that the steam of high pressure will at first partially blow through the condenser, and rid it of its air and condensing water ; and that by degrees the jet of cold water will overpower the influx of steam, and consequently 1 6 THE SCIENTIFIC PAPERS OF produce a vacuum. An arrangement of this description, although simple, is at least very imperfect ; because it is a matter of considerable difficulty so to proportion the injection of cold water that the first rush of steam may not forthwith be condensed, but may exert its expansive force in a cold vessel, and yet that an instant afterwards a complete condensation of the remaining steam may be effected. If too much water be used, the air and water will not be expelled, and consequently no vacuum will be formed ; if too little, no final condensation will take place. The quantity of injection water must be very large, because the whole of the steam has to be condensed ; and having to complete the condensation in the same vessel, the water must leave it at a low temperature. The principle of the regenerative condenser has been carried still further in the regenerative engine, which has been executed on a large scale by Messrs. Fox, Henderson & Co., under the superintendence of the author. In this engine the steam, after it has served to propel the working piston to the end of its stroke, is received into a series of consecutive chambers, from which it returns to the working cylinder an indefinite number of times. On a future occasion the author will be glad to bring the particu- lars of this engine before the Institution. MR. SIEMENS, in answer to enquiries, replied that the experiment at the Saltley Works, had been tried with one week's working with the condenser, and then one week without it ; and the saving of fuel with the condenser was at the rate of 18 per cent. The apparatus with which the condenser worked was however too light, and had not been made for the purpose ; also that condenser was the first that had been made, and the proportions had been improved in the subsequent ones. There was a deficiency in the supply of condensing water, which sometimes interfered with the regular working of the condenser, as well as the defects arising from the gearing being too light for working it, and these had caused irregularities in the working of the engine ; there was also a difficulty in regulating the engine as a condensing engine with the present governor. The steam pressure was 30 Ibs. per inch ; but a smaller supply of condensing water would be sufficient if a higher pressure of steam were employed. As regarded its use in locomotive engines, Mr. Siemens replied SIR WILLIAM SIEMENS, F.R.S. 1 7 that it would only be necessary for the condenser to work quick enough to condense one cylinder-full of steam before the next cylinder-full was discharged ; and this he thought would easily be effected by widening the plates of the condenser to a proportionate size, and shortening the stroke of the condenser piston, so as to reduce its velocity as far as might be required. The condensed steam would then return to the tender in pipes, between which air was caused to circulate by means of the rapid motion of the engine. He expected the condensing water would be cooled down to about 100° before it was returned to the tender, by the process of passing through the pipes of the refrigerator, from the rapid motion of the engine through the air ; and the water was not re- quired to be so cold as in the ordinary condenser, since only the last portion of the steam was condensed by injection. Mr. Siemens showed by a comparative indicator diagram that with the application of the condenser to a locomotive engine the steam might be cut off at about one-third of the stroke, instead of at two-thirds as usual, and thereby a saving of one-half the steam would be effected with the same power. ON THE EXPANSION OF ISOLATED STEAM, AND THE TOTAL HEAT OF STEAM. BY MB. CHAKLES "W. SIEMENS, of LONDON.* THE object of this paper is to lay before the members the results of certain experiments on steam, purporting, in the first place, to corroborate Regnault's disproval of Watt's law, "that the sum of latent and sensible heat in steam of various pressures is the same ; " in the second place, to prove the rate of expansion by heat of isolated steam ; and, in the third place, to illustrate the immediate practical results of those experiments in working steam engines expansively. * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers, 1852, pp. 131—141. VOL. I. C 1 8 THE SCIENTIFIC PAPERS OF The author pursued these experiments at long intervals since the year 1847, with no other object in view than to extend his own information ; and, consequently, without pretence to generalisation or extreme accuracy. The question, however, is one of great practical importance to engineers, and with the advantage of valuable suggestions and the co-operation of his friends, Mr. Edward A. Cowper and Mr. William P. Marshall, the author has again taken up the experiments, which, having been referred to at the previous meeting by Mr. Cowper, he feels himself called upon to lay before this Institution in their present state, though incomplete. The amount of heat required to convert one pound of water into steam of different pressures has occupied the attention of natural philosophers from the earliest periods of the modern steam engine. Dr. Black observed, about a century ago, that a large quantity of heat was absorbed by water in its conversion into steam (not accompanied by an increase of temperature), which he termed " the latent heat of steam." His apparatus consisted simply of a metallic vessel containing water, which he exposed to a very regular fire ; and from the comparative time which was occupied, first in raising the temperature of the water to the boiling point, and, secondly, in effecting the evaporation, he approximately determined the amount of latent heat. Resuming the experi- ment, in conjunction with Dr. Irvine, he employed a different apparatus, consisting of a steam generator, and of a surface condenser, or 'a serpentine tube, surrounded by a large body of cold water. The steam which condensed in the serpentine tube was care- fully collected and weighed, and the rise of temperature of the surrounding water was observed, which, multiplied by its known quantity, represented the total quantity of heat which the steam had yielded. The quantity of heat requisite to raise the temperature of one pound of water through 1° Fahr. being taken for the unit of heat, Black and Irvine obtained for the total quantity of heat in Steam of atmospheric pressure, the number . . 954 Southern . 1021 SSK WILLIAM SIEMENS, F.R.S. 19 Watt obtained the number 1140 Regnault 1145 Dr. Ure 1147 Desprez, 11 8G, but later li:»-2 Brix 1152 Gay Lussac and Clement 1170 Count Rumford 1206 All of these eminent experimentalists employed essentially the same apparatus, and the differences between their results proves its great liability to error. Brix, of Berlin, was the first to investigate those errors, and to calculate approximately their effect upon the results obtained. "While such a large amount of labour and talent has been expended to determine the latent heat in steam of atmospheric pressure, a far more important question seems to have been passed over with neglect, namely, What is the relative amount of heat in steam of various densities ? The celebrated Watt justly perceived the importance of this question, but contented himself with one experiment upon which he based his law, "Uiat the sum of latent and sensible heat in steam is the name under all pressures." Southern repeated the experiment, and found that steam of greater density contained absolutely more heat than steam of lower pressure, which induced him to adopt the hypothesis that " the latent heat of steam was the same at all pressures" Subsequent experiments and general reasoning seemed to be in favour of Watt's law, which enjoyed the general confidence until it was attacked, only a few years since, by Regnault, of Paris, who proved by a series of exceedingly elaborate and carefully conducted experiments, that neither the law of Watt nor that of Southern was correct, but that the truth lay between the two. The apparatus employed by M. Regnault may be said to be a refinement upon those previously employed, and with the advantage of Brix's labours to determine the amount of errors, he seems to have succeeded in measuring the absolute amount of heat in steam of various pressures with surprising accuracy. The costly and complicated nature of the apparatus employed by M. Regnault has hitherto prevented other experimentalists c 2 20 THE SCIENTIFIC PAPERS OP from repeating the experiment, and in the meantime practical engineers still continue to adhere to Watt's law. Shortly after the publication of Regnault's experiments by the Cavendish Society, in 1848, the idea occurred to the author of the present paper that their results might be brought to a positive test by a simple apparatus, which he places before the Meeting in operation, shown in Fig. 1, Plate 3. It consists of an upright cylindrical vessel of tin-plate A, which is surrounded by an outer vessel filled with charcoal B B, or other non-conducting material. A steam-pipe C, with a contracted glass vein D, enters the inner vessel in a slanting position, in order that the water of priming from the boiler, and of condensation within the pipe, may return to the former, allowing only a small jet of pure steam to enter the vessel, where it suddenly expands and communicates its temperature to the bulb of a thermometer E, which is inserted through a stuffing-box from above. The lower extremity of the inner vessel A is connected on the one hand to a mercury gauge Gr, and on the other to a condenser, by means of a stop- cock to regulate the pressure. The pressure and temperature of the steam within the boiler being known, and the temperature of the expanded steam observed, it will be seen whether that tempera- ture coincides with the temperature which is due to pressure indicated by the mercury gauge. If it did, then Watt's law would be confirmed, but since the temperature rises higher than is due to the pressure, it follows that the high-pressure steam contains an excess of heat, which serves to super-heat the expanded steam. All losses of heat from the apparatus would tend to reduce the temperature, and be in favour of Watt's law ; but it will be shown that those losses may be entirely eliminated, and a true quantitative result be obtained. For this purpose the pressure in the boiler should first be raised to its highest point, and the indicating apparatus be well penetrated by the heat ; the fire under the boiler should thereupon be reduced, and observa- tions made simultaneously, and at regular intervals, of the declining pressure within the boiler, and temperature of the expanded steam of constant pressure. The pressures being nearly equal, the fire under the boiler is again increased, and the observations continued until the maximum pressure is once more obtained ; and the loss of heat by radiation, &c., may be cor- WILLIAM SIEMENS, F.R.S. 2 1 rectly estimated, by a comparison of the two series of observa- tions. Tin; second portion of this paper relates to the rate of expansion of isolated steam by heat, that is, steam isolated from the water from which it is generated. The author has not been able to meet with any direct experi- ments on this subject, except some at a recent period by Mr. Frost, cl1 America, which, however, do not seem entitled to much con- fidence. The rate of expansion of air and other permanent gases by heat was first determined by Dalton and Gay Lussac simul- taneously, who determined that all gases expanded uniformly, and at the same absolute rate, amounting to an increase of bulk equal to 4-J-oth Part °f the total bulk at 32° Fahr. for every one degree Fahr., or -o^th part of the total bulk at 212°. Dulong and Petit confirmed the law of Dalton and Gay-Lussac, but it appears that these philosophers confined their labours to the permanent gases and atmospheric pressure, and merely supposed the general appli- cability of their discovery. Being interested in the application of " super-heated " steam, the author tried some direct experiments on its rate of expansion, in the year 1847, which confirmed his view, that vapours expand more rapidly than permanent gases, or in other words, tliat the rate of expansion of different gases and vapours is equal, not at the same absolute temperature, but at points equally removed from their points of generation, The apparatus employed in these experiments has been placed before the meeting, and its simplicity, when seen in operation, is such that the result, it is hoped, can hardly be doubted. It is shown in Fig. 2, Plate 3, and consists of a metallic trough A A, containing oil, which is placed upon a furnace B B, heated by gas flames. One end of the trough is provided with a stuffing- box, through which a glass tube C, of about TVth inch diameter, and sealed at one end, may be slipped, which will rest horizontally upon a scale below the surface of the oil. The mouth of the glass tube is connected to an open mercury syphon G, with either the one or the other leg filled with mercury, to produce the desired pressure within the horizontal glass tube. A small drop of water and a piston of mercury P being introduced into the bottom of the tube, it is placed in the oil bath, and connected 22 THE SCIENTIFIC PAPERS OF to the syphon. The oil bath is then gradually heated, and the temperature observed. As soon as the boiling point of water under the pressure in question is reached, the mercury piston will move rapidly forward, until all the water is converted into steam. The temperature continuing to increase, the piston will continue its course more slowly upon the scale, where its progress is noted from time to time, together with the temperature. The experiment is continued until the temperature reaches about 400", when the oil begins to boil. The gas flame is then with- drawn, and the bath allowed to cool gradually. The observations of the temperature and the position of the mercury piston are continued until the steam contained behind it is recondensed. A comparison between the two series of observations gives the correct mean of the experiment, by which the effects of the friction of the mercury piston, any possible slight leakage of steam past it, and faults consequent on the slow transmission of heat, are completely neutralized. The curve A on Fig. 3, Plate 4, has been drawn, expressing the rate of expansion of isolated steam according to these ex- periments. The results of nine separate experiments very nearly coincide (as shown by the dotted lines, which give the ex- treme variation in the experiments), except at the starting- point, where the rate of expansion is so very great that it is difficult to obtain correct observations ; changes in the barometer, moreover, affect the curve in the vicinity of the boiling point. To obviate the effect of these inaccuracies, the unit of volume in laying down the curves from each of the nine experiments was taken, not at the absolute boiling point, but at 250°, where the expansion had already assumed a definite course. The diagram also shows a straight line B, expressing the rate of expansion of common air, which at first diverges greatly from the hyperbolic curve of expansion of steam, although the asymptote of the latter seems to run parallel to the former. The author considers it therefore highly probable, " that the rate of expansion of all gases may te expressed by one hyperbola, which starts from the condensing point of the ffas," and that the apparently uniform rate of expansion of the permanent gases may be accounted for by their great elevation, at the ordinary temperature, above their supposed boiling point, in consequence whereof the true curve .s/A1 \VII.UAM SIEMENS, l-.R.S. 2$ approaches so nearly to its asymptote that the difference cannot be detected by experiments. The general result obtained from the above experiments may be stated as follows : that steaui generated at 212*, and maintained at a constant pressure of one atmosphere, when heated out of contact with water to 230° is expanded 5 times more than air would be. 240° „ 4 260° „ 3 370° „ 2 The author intends to extend the range of his experiments upon gases and vapours under high pi'essure, and will be glad to communicate the further results to the Institution. The diagram contains another curve, C, showing the results of Mr. Frost's experiments, alluded to before, which, from the very sudden and irregular rise at the commencement, appears to be affected by some serious source of error. The two curves of pressure and density, P and D, show the rate at which saturated steam increases in pressure and in density, with the rise of temperature marked at the bottom of the diagram. It will be observed that the pressure increases at a rather greater rate than the density ; and it is a remarkable circumstance, that the difference, or the rate at which the pressure increases faster than the density, which is in effect the rate of expansion of saturated steam with the increase of sensible temperature, exactly coincides with the line B, representing the rate of expansion of atmo- spheric air. An extension of our knowledge on the properties of steaui is a matter of such evident importance to engineers, that it would be useless to dwell upon its practical importance. Suffice it to say, that it has been theoretically demonstrated that a perfect Boulton and Watt Condensing Engine (abstracting friction and all losses of heat in the furnace and through radiation) would only yield about seven per cent, of the mechanical force which would be equivalent to the expended heac. It may be argued from this, that the steam engine is destined to undergo another great modification in principle, and in the author's humble opinion this crisis will be accelerated by inquiries into those properties of gaseous fluids which have hitherto excited but little attention, and especially into the properties of dry steam, or isolated steam. 24 THE SCIENTIFIC PAPERS OF The present paper will be confined to showing the effect of the above experiments upon the rate of expansion of steam within the steam cylinder of an engine. It was demonstrated by the first- named experiments, that expanded steam is super-heated steam; and, by the second, it is shown what is the expansion of bulk due to an increase of temperature. Supposing the results of the experiments to be correct, the expansion curve as laid down by Tambour, and which is based upon Watt's law, requires a modification due to the excess of temperature in expanded steam ; and it will be observed that this correction in the curve of expansion is in favour of working engines expansively, as a greater average pressure is obtained during expansion than would be the case if the expanded steam were not thus super-heated. Its correctness is corroborated by some actual observations by Mr. Edward A. Cowper in taking diagrams of expansive engines, previous to his acquaintance with the above experiments. It moreover appears that in Cornwall, engineers have been practically acquainted with the fact, that expanded steam is super-heated steam, and more economic in its use than saturated steam ; for it is a practice with them to generate the steam at very high pressure, and to expand it down to the required pressure previous to its reaching the steam cylinder. Another remarkable practical observation is, that a jet of high- pressure steam does not scald the naked hand, while a jet of low- pressure steam does, although the high-pressure steam is the hotter substance. The cooling effect of a jet of high-pressure steam is so powerful, that, as the' author has been informed, ice has been actually produced in the heat of summer in America, by blowing a powerful jet of steam of 400 Ibs. pressure per square inch against a damp cloth. This phenomenon may be explained by the perfectly dry and under-saturated state of expanded steam, which, with a strong tendency to re-saturate itself, produces a powerful evapora- tion on moist surfaces with which it comes in contact. The rapid rate of expansion of steam by heat, when still near its boiling point, proves the economy of heating the steam cylinder either by a steam jacket, or by the application of fire. It is, however, important to observe, that the specific heat of steam seems to diminish, the more the temperature exceeds the boiling point. The annexed table of observations gives the data from which the curve A in Fig. 3 has been drawn. WILLIAM SIEMENS, F.R.S. TABLE OK EXPERIMENTS ON THK EXPANSION OP ISOLATED ATMOSPHERIC 8TKAM. Ti-ini>«-r:i- ture. BjMMM 1 Is* <~ 2 J- |.S 3 T3 g ti 4 i« 4-s 5 •3 £ SO 6 •i Sg> El 7 i g ti 8 •a g to Descend- ^ \ ing. 209 05-0 210 5-00 212 213 8-00 8-00 10-00 10-00 9-70 8-00 ... '.••D| I'll 216 : 2174 220 2224 L'L':." 2274 230 -2324 8-80 9-00 no ,,.._,., 932 :i;.vi 8-40 8-68 8-90 9-11 ), which is, in effect, the expansion curve of saturated steam indefinitely prolonged. The vertical lines and figures at the bottom signify the pres- sures of saturated steam in Ibs. per square inch ; the horizontal lines and figures on the sides denote the volume of steam compared with the volume of water from which it is produced ; and the horizontal lines, with figures on the curve, express the tempera- tures of the steam corresponding to the pressure and volume of the same. The outer curve, a a «, is that usually employed in calcu- lating the power of expansion engines, being the expression of Watt's law " that the total heat in steam is the same at all pressures." The inner curve, b 1 7>, is the corrected one, in accordance with the recent discoveries of Regnault, " on the total heat of steam," * and may be termed " the curve of equal heat." The fields between the horizontal dotted lines represent the power given out by the steam, in losing equal decrements of 10° of temperature in its expansion, and it is important to observe, that the areas of these fields are nearly alike, between the limits to which the pressure and temperature of steam are experimentally known, increasing only slightly, and in a uniform ratio inversely as the temperatures. This gradual increase may be ascribed to the fact, that the curve in question is one of equal heat, whereas it has been shown, that in expanding behind a working piston, the steam must lose heat in the dynamical proportion to the power given out. Messrs. Rankine and Clausius have first drawn attention to this circumstance, and proved that the expansion of steam, behind a piston, must be attended by partial condensation. * Vide the Publications of the Cavendish Society, Vol. I. VOL. I. D 34 On the other hand, experiments made by the author* prove that steam, when expanded spontaneously, is superheated steam, being a verification of Eegnault's discovery, that the total heat of steam increases with its pressure. When steam is expanded behind a working piston the excess of free heat is first absorbed, or changed into dynamical effect, and if that does not suffice, partial condensation must take place. It appears, however, to the author, that Messrs. Rankine and Clausius undervalue .the amount of free heat, and, therefore, over- estimate the amount of condensation during expansion, by taking the specific heat of steam at 0*305 (Regnault's co-efficient of increasing heat), which there seem good reasons to believe is far too low, because : — 1st. The specific heat of an elastic fluid must be proportionate to its rate of expansion by heat. It has been shown, however, in experiments instituted by the author above referred to, that the rate of expansion of steam near its point of saturation is about three times greater than that of air at the same temperature, which would make its specific heat 3 x -267 = ' 801, diminishing however rapidly with the increase of temperature. 2nd. The actual forms of diagrams, taken from the best ex- pansive steam engines, do not show the effect of condensation : the ordinates of the lower portion of the curve are indeed higher than those given by Watt's law, starting from the same point. This is shown by Fig. 2, Plate 5, which is a diagram taken from the Old Ford Engine, by Mr. W. Pole,t in which a a a is the actual curve, b b J-the curve representing Watt's law, and c c c the curve of equal heat. The rise of the actual curve towards the end may in part be owing to the generation of steam from the heated sides of the cylinders ; but it could not be supposed that the effect of such generation would equal that of spontaneous condensation throughout the body of the steam. Moreover the actual curve proves to be almost the perfect dynamical curve, as is proved by the equal areas, or fields of power, obtained by drawing- lines from points of the curve of equal progression of temperature. If the limits of the sheet of diagrams had admitted of a con- * Vide Proceedings of the Institution of Mechanical Engineers, for June 1, 1852, p. 24, ante. •f Vide Treatise on the Cornish Engine, by W. Pole, Part III. .svA- nv/././. M/ .SY/-;.)//-:.V.V, /--.as. 35 Initiation of the curve horizontally (Fig. 1, Plate 5), it would have exhibited continually decreasing volumes, and increasing temperatures, until finally a point would have been reached, where the volume of the steam was equal only to the water producing it. It may be assumed, that the temperature would, at that point, be 640° Centigrade (11HO° Fahr.), or in other words, that the entire heat of the steam would be sensible. Supposing this steam (which would have at least 2,o()0 Ibs. pressure per square inch) could be introduced below a piston, and in giving out its power be ex- panded, until its temperature was reduced to zero, then the entire 640 degrees of heat would have been converted into their equivalent of power, of which the field of the diagram would represent the integral. The theoretical equivalent of mechanical force for heat is thus represented to the eye ; and in computing the area of the entire figure, it is found to coincide nearly with, but somewhat to exceed, the results of abstract calculation and of 'Mr. Joule's experiments. That portion of the diagram (Fig. 1) which is shaded darker than the rest, represents the power of a perfect low-pressure condensing engine ; it covers only about l-14th part of the entire area. The diagram shows that the expansive steam-engine would be theoretically a perfect engine, if the water was heated in a close boiler to 1180° Fahr., and being then introduced below the working piston, under a pressure of at least 2,000 Ibs., would resolve itself entirely into steam, and was allowed to expand 2000 times before it was discharged into a vacuous space, which, in this case, would not necessarily be a condenser. The impracti- cable nature of such an engine is manifest, and it becomes necessary to seek for other means of obtaining from heat its full value of power. It may not be considered out of place to mention here, the well- known experiments on steam-guns by Mr. Perkins, which went far to prove the actual possibility of charging water with sufficient heat, in close vessels, that, upon liberation, it would resolve itself entirely into steam. Before leaving this part of the paper, it will be necessary to show the effect produced by the expansion of air, or any other permanently elastic fluid, under a working piston. In the diagram (Fig. 3, Plate r>), the figures on the base and vertical D 2 36 THE SCIENTIFIC PAPERS OF lines denote the pressure in Ibs. per square inch, and the figures on the side denote volumes of air, as compared with the volume of the same weight of water. The curve a a a represents Marriotte's law, and is a curve of equal heat. The curve b b 1) is the dynamical curve, representing the real rate of expansion of air, behind a working piston. The difference between the two curves arises from the loss of sensible heat, which is converted into effect. The figures upon the curve show the rate of pro- gression of temperature, in compressing air of atmospheric pressure at 60° Fahr. In constructing this curve, the specific heat of air at constant volume has been taken at '267 as determined by Delaroche and Bernard. It furnishes itself at least an approximate proof of the correctness of this number, because the curve agrees with the ob- served fact, that in compressing air, to double its original pressure, its temperature is raised 70° Fahr. The dotted hori- zontal lines limit the uniform fields of power obtained for every 10° decrease of temperature. This curve is directly applicable to air, which when reduced to atmospheric pressure has a temperature of 60° Fahr. It can, however, easily be corrected, for any degree of temperature, by adding the difference of temperature at a corresponding pressure throughout, and by adding to each volume the same difference of temperature, divided by 508 (the ratio of expansion of air at 60° Fahr.) * Secondly. — " On the performance of actual engines, including the air-engines of Stirling and Ericsson." * The dynamical theory of heat must not be considered the creation of the last few years, but, like all abstract truths in nature, it seems to have presented itself to the minds of the greatest philosophers in all ages, to be, after them, again superseded by theories moulded, as it were to order, to explain some isolated phenomenon, such as the radiation of the sun, the heating flame of a fire, or the latent heat in steam ; until at length the means of observation were sufficiently perfected to cover with absolute proof, what could before be reached only by the imagination. It may here be mentioned, as instances, a quotation by Baron Humboldt from Aristotle, " who considered the first principle in nature to be a unity in all its manifestations, and the manifestations themselves he reduced always to motion as their foundation." Again, in Lord Bacon's Aphorisms, the chapter on "The first Vintages of the Force of Heat," occurs the following remarkable passage : — "From the instances taken collectively, as well as singly, the nature whose limit is heat, appears to be motion." And further on, — " But that the very essence of heat, or the substantial self of heat, is motion, and nothing else limited,'' ult, but he might claim for himself at least that strong con- viction, approaching enthusiasm, which alone could have given him strength to combat successfully the general discouragement and the serious disappointments he had met with. The following illustrations, proving the imperishable nature of physical forces and their mutual convertibility, were made use of to indicate more clearly the principles his engine was based upon. A weight falling over a pulley, to which it was attached by a siring, would impart rotary motion to a fly wheel, fixed upon the same axis with the pulley, and the velocity imparted to the wheel would cause the string to wind itself upon the pulley, till the weight had reached nearly its original elevation. If the friction of the spindle and the resistance of the atmosphere could be dispensed with, the weight would be lifted to precisely the same point from whence it fell, before the motion of the wheel was arrested. In descending again, it would impart motion to the wheel as before, and this operation of the weight, of alternately falling and rising, could continue adinfiniium. If the string were cut at the instant when the weight had descended, the rotation of the wheel would continue uniformly, but it might soon be brought to a stop by immersing it in a basin filled with water. In this case the water was the recipient of the force due to the falling weight, residing in the wheel ; and by repeating the same ex- periment a sufficient number of times, we could find an increase of temperature in the water, a fact discovered by Joule, in 1843, which first proved the identity of heat and dynamic effect, and established their numerical relation. If the weight falling over a pulley were one pound, and the distance through which it fell one foot, then each impulse given to the wheel would represent one foot pound, the commonly adopted unit of force ; and if the water contained in the basin weighed also one pound, it would require 770 repetitions of the experiment of arresting the wheel in the water, before the temperature of that water was increased by one degree Fahrenheit. Another illustration made use of, was that of a hammer falling in vacua upon a perfectly elastic anvil. The hammer would, under these circumstances, rebound to precisely its original elevation, and granting the perfect elasticity of both hammer and anvil, neither 54 THE SCIENTIFIC PAPERS OF sound nor heat would be produced at the point of concussion. If a piece of copper were suddenly introduced between anvil and hammer, the latter would not rebound, but would make the copper the recipient of the expended force. If the hammer were now lifted again and again by an engine, and the piece of copper were turned about on the anvil, so that at the end of the operation it had precisely the same form as at the commencement, then no outward effect would be produced by the force expended, but the piece of copper would be heated perhaps to redness ; and if the engine employed to lift the hammer were perfect, then the heat produced within the copper should be sufficient to sustain its motion. A familiar instrument for converting force into heat was the fire-syringe. The force expended in compressing the air imparted a sufficient temperature (about 600° Fahr.) to the same to ignite a piece of German tinder. When the plunger of the syringe was drawn back, it might be observed that the temperature of the enclosed air was again reduced to its original degree, because the heat developed in compression of the air had been spent again in its expansion behind the piston. If the expansion of the heated and compressed air had been without resistance, no reduction of its temperature could have taken place, because no force would be obtained ; a fact which had been recently proved by Eegnault, and which was perhaps the strongest point in favour of the dynamic theory of heat that could be brought forward. If the heated and compressed air in the fire-syringe could be produced by some ex- ternal cause and be introduced behind the plunger after it had descended freely to the bottom, then the force imparted to the plunger in the expansion might be turned to some useful purpose, and a dynamically perfect engine might be obtained. But although the elevated temperature might be readily supplied by means of a fire, it would not be possible to give a sufficient density to the air, except by an expenditure of force in its compression. If, how- ever, heat were applied to a drop of water confined below the plunger till its temperature was raised sufficiently to effect its conversion into steam of the density of the water itself (Gaignard de la Tour's state of vapours), and then allowed to expand below the plunger till its temperature was reduced to zero, a dynamically perfect engine would be obtained. The impracticable nature of .S7A1 WILLIAM SIEMENS, I-.K.S. 55 such an engine was however manifest, if it was considered that steam of the density of the water producing it, would exert a pressure of probably several hundred atmospheres, which pressure the moving part of the engine must be made strong enough to bear at a temperature of more than 1000° Fahr., and that the capacity of the working cylinder must be sufficient to allow of an expansion of the steam to several thousand times its original volume. It was therefore necessary to look for other means of obtaining from heat its equivalent value of force, which means, it was contended, were furnished by the "regenerative steam-engine." This engine, of which several diagrams and a model were exhibited, consisted of three essential parts, namely, the furnace ; the working cylinder, with its respirator and heating vessel ; and the regenerative cylinder. It consisted also of a boiler and con- denser, (unless the steam were discharged into the atmosphere,) but these were not essential to the working of the engine, although of great practical utility. The regenerative cylinder had for its object alternately to charge and discharge two working cylinders, and the action of its piston might be compared to that of a hammer oscillating between two elastic anvils. The regenerative cylinder communicated at its one extremity with one working cylinder, and at the other extremity with another and similar working cylinder, and these communications were not intercepted by valves. The working cylinders were so constituted that their capacity for steam of constant pressure was the same, no matter where the working piston stood. Each consisted of a cylinder of cast iron, open at both ends, which was completely enclosed in another cylinder or heating vessel, one end of which was exposed to the action of a fire. Within the inner cylinder was a large hollow piston, filled with non-conducting material, to which was attached a long trunk or enlarged hollow piston rod of nearly half the sectional area of the piston itself. This trunk was attached to the working crank of the engine in the usual manner. The trunk of the second working cylinder stood precisely opposite, and was connected with the same crank. The piston of the regenerative cylinder was also connected with the same crank; but stood at right angles to the two working cylinders. The consequence of this arrangement was, that while the two working trunks made their strokes (the one inward and the other out- 56 THE SCIENTIFIC PAPERS OF ward) the piston of the regenerative cylinder remained com- paratively quiescent upon its turning or dead point, and vice versa. Around the two heating vessels boilers were disposed, which received the heat of the fire, after it had acted upon the former. The steam generated within the boilers was introduced into the engine by means of an ordinary slide valve (of com- paratively very small dimensions) at short intervals, and when the piston of the regenerative cylinder was in its extreme posi- tion. The admission of the steam, which was of high pressure, took place on that side of the regenerative cylinder where compression by the motion of its piston had already taken place, and at the same instant a corresponding escape of expanded steam on the other side of the regenerative piston was allowed to take place into the atmosphere. The quantity of steam freshly admitted at each stroke did, however, not exceed one-tenth part of the steam contained in the working cylinders of the engine, and served to renew the same by degrees, while it added its own expansive force to the effect of the engine. The compres- sion of the steam into either of the working cylinders took place when its hollow piston stood at the bottom. While in this position the steam occupied the annular chamber between the working trunk and the cylinder, besides the narrow space between the cylinder and the surrounding heating vessel. The pressure of the steam being the same above and below the hollow piston, but the effective area below being equal to twice the area above, the working trunk, attached to the piston, would be forced outward through the stuffing box, while the steam of the annular chamber above the piston passed through the narrow space intervening, into a space of twice the capacity of the annular chamber below the hollow piston. During its passage the steam had to traverse a mass of metallic wire gauze or plates, the respirator, presenting a large aggregate surface, which reached at one end sufficiently downward into the heating vessel that its temperature was raised from 600° to 700° Fahr., while its other extremity remained at the temperature of saturated steam, or about 250° Fahr. In consequence of the addition of temperature the steam received on its passage through the re- spirator, its elastic force was doubled, and it therefore filled the larger capacity below the hollow piston or displacer without SIR WILLIAM SIEMENS, F.R.S. 57 loss of pressure. When the effective stroke of the working trunk was nearly completed, the regenerative piston commenced to re- ivdr, and the steam below the hollow piston expanded into the regenerative cylinder, depositing on its regress through the respi- rator the heat it had received on its egress through the same, less only the quantity that had been lost in its expansion below the working piston, which was converted into dynamic effect or engine-power, and had to be supplied by the fire. The expansion ami simultaneous reduction of temperature of the steam caused a diminution of its pressure from four to nearly one atmosphere ; and the working trunk could now effect its return stroke with- out opposing pressure, and while the second working trunk made its effective or outward stroke impelled by a pressure of four atmospheres. The respirator, which was invented by the Rev. Mr. Stirling, of Dundee, in 18 l(i, fulfilled its office with surprising rapidity and perfection, if it were made of suitable proportions. Its action was proved at the end of the lecture by a working model. It had been applied without success to hot-air engines by Stirling and Ericsson, but failed for want of proper application ; for it had been assumed (in accordance with the material theory of heat) that it was capable of recovering all heat imparted to the air, and, in consequence, no sufficient provision of heating apparatus had been made. It having been found impossible to produce, what in effect would have been a perpetual motion, the respirator had been discarded entirely, and was even now looked upon with great suspicion by engineers and men of science. Mr. Siemens had, however, no doubt that its real merits to recover heat that could not practically be converted by one single operation into mechani- cal effect, would be better appreciated. The rapidity with which the temperature of a volume of steam was raised from 250° to 650° Fahr. by means of a respirator, was indicated by the fact that he had obtained with his engines a velocity of 150 revolutions per minute. The single action of heating the steam occupied only a quarter the time of the entire revolution of the engine, and it followed that it was accomplished in one-tenth part of a second. But, in explanation of this phenomenon, it was contended, that the transmitting of a given amount of heat from a hotter to a cooler body, was proportionate to the heating surface multiplied 58 THE SCIENTIFIC PAPERS OF by the time occupied, and that the latter factor might be reduced ad libitum, by increasing the former proportionately. The air- engines . of Stirling and Ericsson had failed also, because their heated cylinders had been rapidly destroyed by the fire ; but the cause of this was, that an insufficient extent of heating surface had been provided, and it was well known that even a steam- boiler would be rapidly destroyed under such circumstances. Mr. Siemens was led by his own experience to believe that his heating vessels would last certainly from three to five years, and being- only a piece of rough casting, that could be replaced in a few hours, and at a cost below that of a slight boiler repair, he con- sidered that he had practically solved the difficulty arising from high temperature. It was however important to add, that all the working parts of his engine were at the temperature of saturated steam, and therefore in the condition of ordinary steam-engines ; whereas in Ericsson's engine, the hot air had entered the working cylinder. In surrounding the heating vessel with the boiler, an excessive accumulation of heat was prevented from taking place, and the pressure of the steam in the boiler became the true index to the engine-driver of the temperature of the heating vessel. Another essential property of the heating vessel was, that all its parts should be free to expand by heat without straining other parts, which was accomplished by a free suspension, and by undulating its surface. Lastly, it should be massive, to withstand the fire with impunity, for iron was, strictly speaking, a com- bustible material. The pyropherus, or finely-divided metallic iron, took fire spontaneously on exposure to the atmosphere, a chip of iron was ignited in flying through the flame of a candle ; an iron tea-kettle was destroyed by exposing it (unfilled with water) to a kitchen fire ; whereas, in forging a crank shaft, the solid mass of iron withstands the white heat of the forge fire for several weeks without deteriorating. A heating vessel, properly constructed and protected, might be heated with safety to 700° Fahr., at which temperature it would be almost as able to resist pressure, as at the ordinary temperature of the atmosphere, the point of maximum strength of iron being at 550° Fahr., as had been proved by experiments made for the Franklin Institution. The construction of a heating vessel combining these desiderata was of paramount importance for the success of Mr. Siemens's engine, and had not SfK WILLIAM SIEMENS, F.K.S. 59 been accomplished without combating against considerable practical difficulty. Although heat may be entirely converted into mechanical effect, it would nevertheless be impossible to construct an engine capable of fulfilling this condition without causing at the same time a portion of heat to be transferred from a hotter to a cooler body, and which must ultimately be discharged. This necessity has been generally proved, and in a very elegant manner, by Professor Clausius, of Zurich, and implies at least the partial truth of " Garnet's theory." In the " regenerative steam-engine," pro- vision had been made for absorbing this quantity of heat, arising in this case from the circumstance, that the saturated steam enters the respirator in a state of greatest density or compression, and returns through it (expanding into the regenerative cylinder) at a gradually diminishing density, although the temperature of the extreme edges of the respirator remains proportionate to the con- densing point of the steam of greatest density, by providing water chambers about the cover of the working cylinder, and around the regenerative cylinder, which are in communication with the steam- boiler. The heat absorbed from the slightly superheated steam is thus rendered useful to generate fresh steam. Objection had been raised by casual observers against the re- generative steam-engine, on account of its apparent similarity in principle to the "air-engines" of Stirling and Ericsson, implying similar sources of failure. The apparent similarity in principle arose from the circumstance that both Stirling and Ericsson, as well as himself, had employed the respirator and high tempera- tures ; but these were but subordinate means or appliances, that might be resorted to in carrying out a correct as well as an erroneous principle. In the winter of 1852-53, when Ericsson was engaged upon his gigantic experiment in America, the speaker had had occasion to read a paper to the Institution of Civil Engineers, entitled " On the conversion of heat into mechanical effect," wherein he had endeavoured to set forth the causes of probable failure of that experiment, and to guard against a sweeping condemnation on that account of some of the means Ericsson had employed. According to the dynamic theory of heat, the elastic medium employed in a perfect caloric engine was a matter of indiffcr- 6O THE SCIENTIFIC PAPERS OP ence, and air had been resorted to, because it was perfectly elastic, and always at hand. In practice, however, the elastic medium employed was a matter of very great importance, and he (Mr. Siemens) had given the decided preference to steam, and for the following reasons : — 1. The co-efficient of expansion of saturated steam by heat exceeded that of air in the proportion of about 3 : 2, but decreased with an increase of temperature. This was not in accordance with the established rule by Gay-Lussac and Dalton, but was the result of his own experiments (described in a paper, " On the expan- sion of isolated steam, and the total heat of steam," communicated to the Institution of Mechanical Engineers, in 1852),* and had been borne out by his practical experience on a large scale. Mr. Siemens had been first induced to undertake these experiments in consequence of an observation by Faraday, that the elastic force of the more permanent vapours gave way rapidly, when by abstrac- tion of heat their points of condensation were nearly attained. He conceived that gases and vapours would expand equally by heat, when compared, not indeed at the same temperature, but at temperatures equally removed from their points of condensa- tion. 2. When saturated steam was compressed (within the regenera- tive cylinder), its temperature would not rise considerably (as the fire-syringe evinced in respect of air), because, as Regnault had proved, the total heat of steam increased with its density, and consequently the heat generated in compression was required by the denser steam to prevent its actual condensation. Without this fortunate circumstance, the steam would be heated already by compression to such an extent, that it would be difficult indeed to double its elastic force by the further addition of heat in the respirator. 3. Steam exercised no chemical action upon the metal of the heating vessel and respirator, because the oxygen it contained was engaged by hydrogen, which latter had the stronger affinity for it until a white heat was reached ; whereas the free oxygen of atmospheric air attacked iron and brass at much lower tempera- tures. 4. The specific gravity of steam was only about one-half that * Vide p. 17, ante. S/K U'll.l.IAM .S7/-:.1//-:.Y\, l-.R.S. 6l of atmospheric air at equal temperature and pressure ; moreover it was a far better conductor of heat, and both circumstances qualified it for rapid respirative action. 5. The fresh steam required for starting and sustaining the power of the engine was generated by heat that would otherwise be lost. No air-pumps, &c., were required, and the management of the engine became as simple as that of an ordinary high- pressure steam-engine. In conclusion, it was stated that at present there were several regenerative engines in constant practical operation, in this country (at the works of Messrs. Newall & Co., at Gateshead), in France, and in Germany, varying from five to forty horse-power, which had proved the practicability of the principle involved, although they were still capable of improvement. Several other engines were now in course of construction at establishments celebrated for precision of execution, and with the advantage of Mr. Siemens's increased experience in designing them. He had been fortunate to meet with men of intelligence and enterprise, lately joined together in a public company, whose co-operation insured a more rapid development of his invention than indi- vidual effort could produce. The benefit he had hoped to derive from his discourse, incomplete as it necessarily was, would be realized, if those men, eminent in science, whom he saw around him, would accept his labours as an earnest towards the prac- tical realization of the dynamical theory of heat, and hasten its triumphs by their own researches. It was impossible to over- estimate the benefits that mankind would derive from a motive force at one-third or one-fourth part the cost and iucumbrancc of the present steam-engine. The total consumption of coal would certainly not diminish ; but our powers of locomotion and pro- duction would be increased to an extent difficult to conceive, tending to relieve men from every kind of bodily toil, and hasten the advent of the hoped for period-of general enlightenment and comfort. 62 THE SCIENTIFIC PAPERS OF ON A NEW CONSTRUCTION OF FURNACE, PARTICULARLY APPLICABLE WHERE INTENSE HEAT IS REQUIRED. BY MR. C. WILLIAM SIEMENS, Mem. List. M.E.* THE high importance of the stores of combustible material which are distributed upon the surface of the earth renders their wasteful expenditure and rapid diminution in quantity in many parts a serious subject for consideration ; and in the writer's opinion there is no object more worthy of the earnest attention of engineers and men of science generally than that of causing the generation and application of heat to be conducted upon scientific and economical principles. Our knowledge of the nature of heat has been greatly advanced of late years by the investigations of Mr. J. P. Joule, of Manchester, and others ; which have enabled us to appreciate correctly the theoretical equivalent of mechanical effect or power for a given expenditure of heat. We are enabled by this new dynamic theory of heat to tell, for instance, that in working an engine of the most approved description we utilise at most only one-sixth to one-eighth part of the heat that is actually communicated to the boiler, allowing the remainder to be washed away by a flood of cold water in the condenser. If we investigate the operations of melting and heating metals, and indeed any operation where intense heat is required, we find that a still larger proportion of heat is lost, amounting in some cases to more than 90 per cent, of the total heat produced. Impressed by these views the writer has for many years devoted much attention to carrying out some conceptions of his own for obtaining the proper equivalent of effect from heat : some of the results he has obtained are known to the members of the Institu- tion, amongst which are the regenerative steam-engine and con- denser, the regenerative evaporator, and an apparatus for the economic production of ice. The regenerative principle appears to be of very great importance and capable of almost universal * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers, 1857, pp. 103-111. SIR WILLIAM SIEMENS, f.K.S. 63 application ; and the object of the present paper is to describe an application of this principle to furnaces of every description. The invention of the regenerative furnace is due to the writer's In-other, Mr. Frederick Siemens; and it has been matured and variously applied by the writer within the last few months. The result has in all cases been a large saving in fuel over the plans in rnmmon use, amounting to from 70 to 80 per cent, of the total quantity of fuel hitherto consumed. The apparatus employed is moreover of a very simple and permanent description, and com- bines economy of fuel with other advantages, amongst which are the total prevention of smoke and a general improvement in the quality of the work produced. Figs. 1 to 4, Plate C, represent the new furnace in the form applicable to piling iron, or heating iron, steel, or other substances. Fig. 1 is a longitudinal section of the furnace, and Fig. 2 a sectional plan ; Figs. 3 and 4 are transverse sections. The furnace consists of the heated chamber A, and of two fire- places or solid hearths B and 0, communicating respectively with the two regenerators D and E. Each regenerator consists of a series of walls of firebrick, laid in open Flemish bond, in such a manner that the pigeon-holes of each wall are opposite the solid parts of the succeeding wall, the object being to form a number of zigzag or tortuous passages through the regenerators, leading to opposite sides of the valve F, shown dotted in Fig. 1, at the bottom of the chimney G. The valve F consists of a rectangular box of iron open at the two sides to the two regenerators D and E, at the bottom to the atmosphere, and at the top to the chimney G. A spindle passes through the centre of the two remaining close sides of the box, and carries a rectangular flap or moveable plate, fitting the box sideways and bearing against one of its upper and one of its lower edges, according to the position of the tumbling lever and weight H which are fixed upon .the spindle outside. When the valve is in the position shown dotted in Fig. 1, the atmospheric air entering from below proceeds in the direction indicated by the arrows, passing through the regenerator D, over the fireplace B, through the heated chamber A, over the fire- place C, through the regenerator E, and by the valve F into the chimney G. 64 THE SCIENTIFIC PAPERS OP A fire having been lighted upon the hearth B through the side opening K, the flame passes through the furnace and through the regenerator E to the chimney Gr. In its passage through the regenerator E, the first perforated wall that the flame strikes against will be heated to a considerable degree, the second wall to a lower degree, and so on in succession, the heat of the current being thoroughly exhausted by the time it reaches the chimney. After about one hour's work the position of the valve F is reversed and fuel is supplied through the opening L to the second fireplace C, which is then acted upon by a current proceeding in the opposite direction to that indicated by the arrows. The cold atmospheric air comes in contact first with the least heated wall of the regenerator E, and then with the more heated walls succes- sively, acquiring thereby a degree of temperature approaching the temperature of the heated current which previously entered the same regenerator. The heat thus imparted to the fresh air greatly increases the temperature of the flame which is now being produced upon the hearth C, and consequently the nearest end of the regenerator D will be heated also to an increased degree, the current reaching the chimney comparatively cool. When the valve F is again reversed, the fresh air will be heated nearly to the increased temperature of the hot end of the regene- rator D, and will produce a still hotter flame with the fuel supplied to the hearth B. It is evident that by a continuation of this process an accumulation of heat to any degree may be produced within the furnace, provided only the heat produced in combustion is greater than the heat lost by radiation and the heat absorbed by the metal or other substances in the heating chamber. In the regenerative furnace now described, the temperature at which the heat is communicated to the materials does not affect the quantity of fuel requisite, except so far as increased radiation is concerned ; for the products of combustion pass away in all cases at a temperature not above 200° or 300° Fahr. This new principle of furnace is therefore applicable with the greatest advantage in cases where intense heat is required. It has been applied to furnaces for reheating steel and iron, at the works of Messrs. Marriott and Atkinson at Sheffield. One of these furnaces has now been in constant work for nearly three months ; and according to a statement received from Mr. Atkinson it has worked SIR WILLIAM SIEMENS, F.R.S. 65 quite satisfactorily, and the result of a careful comparison has shown a saving of 79 per cent, to have been effected over the old furnace in heating the same quantity of metal. Mr. Atkinson has also applied this principle of furnace for melting cast steel, and has ohtaiued a still larger saving, although the new melting furnace has not yet been rendered entirely satisfactory for the workman. The regenerative furnace has also been applied to the purpose of puddling iron ; and though the new puddling furnace has been completed and worked only for a few days at the works of Messrs. Rushton and Eckersley at Bolton, the writer is able to state that it converts a charge of 480 Ibs. of pig metal into wrought iron with an expenditure of only 160 Ibs. of common coal, as compared with C cwt. required in the ordinary furnaces : the net yield of wrought iron is higher than that of the ordinary puddling furnace, and the quality of the iron produced seems also to be superior. It is also worth mentioning that the chimney of this puddling furnace may be watched for hours, and no trace of smoke be seen issuing from it. Several other applications of this principle of furnace are contemplated by the writer, which it would be premature to enter upon on the present occasion. In the discussion of Hie Paper, MR. SIEMENS said he considered the durability of the brickwork might be fully accounted for by the circumstance that, on attain- ing the very high degree of temperature, the air had first to heat the ends of the first wall of bricks that it met with to a very intense degree, but the next wall to a less degree, and so on gradually diminishing towards the chimney. It might be expected at first that the cold air entering would have a tendency to crack the hot bricks ; but it should be remembered that the air became gradually heated as it advanced, coming in contact at first with a comparatively cool wall, and afterwards by degrees with hotter and hotter walls, taking up only 100° or 200° of temperature from each successive wall, each one being only a little hotter than the air on reaching it. There was consequently no sudden difference of temperature at any point between the air and the brickwork with which it came in contact, and ah1 risk of sudden chilling and VOL. i. r 66 THE SCIENTIFIC PAPERS OF cracking of the brickwork was thus avoided. The alternating principle of the furnace gave a remarkable result in the extremely high degree of temperature that could be ultimately attained, as each repetition of the process added something to the previous temperature of the furnace, the heat continually accumulating ; and if the surface were sufficiently covered to prevent loss of heat by radiation, it would be possible by continuing the alternation to attain a temperature far higher than in any existing furnace, and limited only by the materials employed. Mr. Siemens had not yet had any long experience of the application of the plan to puddling, but from the results already obtained he thought there was full reason to anticipate its entire success. This case was a peculiar one from the necessity of keeping the puddling door open during the process, the furnace being consequently exposed to the open air ; and some modifica- tions were therefore required in the details, which only the experi- ence of further trials could enable them to get fully matured ; there were also difficulties to be overcome in the working on the part of the men, from the great contrast to the accustomed work- ing of puddling furnaces, so much smaller quantity of fuel and so much less draught being required. Besides the saving in fuel, he expected a decided advantage both in the quantity and the quality of the iron made, by removing the violent draught produced by the intense heat of the chimney in the ordinary puddling furnaces ; the comparatively cold chimney in the new furnace, with the damper lowered to within two inches of the top of the chimney, gave so small a draught that the flame did not cut the iron and waste it as in the ordinary furnace, a higher temperature being obtained with a more quiescent atmosphere. There was also the advantage that no flame or particles of fuel were carried over the surface of the iron, bringing sulphur and other impurities from the firegrate. Ashes had. to be cleared out frequently from the regenerators, but they were readily removed through the holes provided for the purpose at the back of the furnace, and the puddler simply raked them out on putting a fresh charge into the furnace. The new furnace was found to puddle the iron in about the same time as the ordinary ones, a charge being brought out about every two hours if the fires were sufficiently attended to. It took rather longer to WILLIAM SIEMENS, F.R.S. 67 get up the heat at first, but the furnace retained the heat longer and a higher temperature was obtained ; one night's stoppage required about the same time as the ordinary furnace to get up tin heat again in the morning, but a longer stoppage would cause a somewhat longer time to be required. The principal difficulty experienced in working was from the men putting on too much coal at once, being accustomed to the necessities of the old furnace, and thus choking the fire and retarding instead of accelerating the working of the furnace. The experience with the new puddling furnace was too limited at present to determine fully the difference in the time of the pro- cess ; in the furnace now working at Bolton it was found that the iron was about 10 minutes longer in melting down, but was rather quicker in coming to nature than in the ordinary puddling furnaces ; and there was no decided difference in the whole time of working. Some difference in management from the ordinary furnace was of course required, which caused a difficulty at first in carrying out the new plan ; but the principle of the furnace was quite simple, and no more skill and care was needed than was to be looked for in the men concerned. The quantity of fuel consumed and amount of firing required were much less ; and by keeping the fire low a large proportion of oxygenated air was allowed to enter during the puddling process, which was supplied at a very high temperature, preventing fluctuations in the tempe- rature of the furnace ; and the very low draught of the chimney was an important point in greatly reducing the quantity of cold air unavoidably drawn in at the puddling door whilst open during the process. Mr. Siemens said he had not attempted the application of the principle at present to steam-engine furnaces, the trials having been first made in those kinds of furnaces where the highest temperature was employed, and where consequently the greatest economy could be effected by the regenerative plan ; but even in the case of steam boilers, a considerable portion of the fuel was generally wasted, by the air being allowed to escape into the chimney at a higher temperature than was required for the purpose of maintaining the draught. v 2 68 THE SCIENTIFIC PAPERS OF In the discussion of the Paper "DESCRIPTION OF TWO PAIR OF HORIZONTAL PUMPING ENGINES," by Mr. E. A. COWPER, ME. C. TV. SIEMENS * said he was acquainted with the pumping-engines at the Berlin "Waterworks, where there were twelve powerful beam-engines, coupled in pairs at right angles with fly-wheels, and working vertical pumps under a pressure of 160 feet head of water. The present double ring valves allowed an easy and unrestricted motion of the water, as the joint cir- cumferences of the four openings gave a large area of passage with a little lift of the valves. With regard to the employment of the crank and fly-wheel for pumping-engines, in place of the Cornish system of lifting the water by the weight of the plungers, it was true that a large fly-wheel with a great weight in the rim, running at a considerably higher speed than the weight in the Cornish engine, had the advantage of more vis inertice ; but only a limited fluctua- tion in its speed was available, and the weight was never stopped as in the Cornish engine, where the whole weight of the pump- rods was stopped and started again at each stroke. It was there- fore to be expected that a greater economy could be obtained by the latter plan, in case of very great lifts, a larger proportion of moving power being absorbed at the commencement of the stroke, allowing the expansion to be carried to a higher degree by ad- mitting of greater extremes of pressure in the stroke. He accordingly thought there were cases, such as pumping from deep pits, where the Cornish plan would prove the most economical, the pump rods falling gradually by their own weight, and being then lifted by the free action of the steam in the cylinder ; but in many cases, such as low lift pumps, the horizontal direct con- struction was preferable. He observed that the engines described had not been designed for such a high degree of economy as was attained in the Cornish engines, since the steam was cut off only * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers, 1858, p. 57. WILLIAM SIEMENS, F.R.S. 69 at erne-third the Btroke ; and there did not appear to be a steam-jacket to the cylinders. He had found a great advantage in employing a jacket not only round the sides of the cylinders, but also at the ends, and it was more important to have a jacket at the ends than round the sides ; for on the steam first entering the cylinder, a much larger extent of surface was offered to it by tin,1 end than by the small portion of the sides then exposed. "When the cylinder was not protected by a jacket, the end of the cylinder being cooler than the steam on first entering, caused a portion to be condensed, which was partly evaporated again in the latter part of the stroke, when the pressure and consequent temperature of the steam was lowered by expansion. The effect of this generation of steam in the cylinder was to increase the pressure at the end of the stroke beyond that due to the expansion ; and the line of the indicator diagram was thus raised in the latter part of the figure above the regular curve of expansion. But this did not appear to be the case in the indicator diagram from the Crystal Palace engines, which showed the steam entering the cylinder at a total pressure of about 34 Ibs. per square inch, cut off at one-third of the stroke, and expanded down to a final pressure of 11 Ibs. due to the expansion. In the discussion of the Paper "ON THE PERFORMANCES OF THE SCREW STEAM SHIP ' SAHEL,' fitted with Du Trembley1 s combined-vapour engine, AND OF THE SISTER SHIP ' OASIS,' fitted with steam-engines worked expansively, and provided with partial surface condensation" by JAMES WAEDROP JAMESON, MR. SIEMENS * said, when treating of air-engines, in a paper which had been read at the Institution in the Session 1852-53, | he * Excerpt Minutea of Proceedings of the Institution of Civil Engineers, Vol. XVIII. Session 1858-59. pp. 256-259. t Vide Minutes of Proceedings of the Institution of Civil Engineers, Vol. XII. p. 571, and p. 29, ante. 7 J> " ,, ,, 5> " 55 55 55 *0 ,, ,, A KK° 55 55 55 5> » ,, 55 10 „ „ „ 80° „ ,, * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers 1860, p. 78. SIX WILLIAM SIEMENS, F.R.S. 79 Comparing these theoretical results with the experiments given in Table V., it appeared that in practice with steam of 51 Ihs., or about 3 atmospheres effective pressure, the rise of temperature was 74°, while the calculation gave only a little more than 50° ; but then it was assumed that there had been no loss of power by friction, and .the quantity of feed-water propelled into the boiler had been supposed to be the maximum amount theoretically possible. The calculation accordingly gave the minimum rise of temperature when the steam was only just able to balance the pressure of the water tending to escape from the boiler ; and consequently in practice the actual rise of temperature must always be greater than that obtained by the calculation ; but the two results differed not more, he thought, than might be expected, if all losses of effect were taken into account. The table agreed moreover with the calculation in giving a greater rise of tempera- ture at higher pressures of steam ; although the losses of effect must necessarily increase with the pressure, or rather with the increase of velocity of the jet. Much must also depend upon the proper adjustment of the instrument to make the quantity of water injected a maximum. In the discussion of the Paper "ON AN APPLICATION OF GIFFARD'S INJECTOR AS AN ELEVATOR FOR THE DRAINAGE OF COLLIERY WORKINGS," by Mr. C. W. WARDLE, MR. C. W. SIEMENS * said, that although the injector was very beautiful and economical in action where water had to be raised and also to be heated, as in feeding a boiler, it was remark- ably deficient in respect of economy when employed simply as an elevator for raising water, where the water was not required to be * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers, 1861, p. 227. 8O THE SCIENTIFIC PAPERS OF heated. This was shown in the experiment which had been men- tioned, where the water was raised only 36 feet high in being heated 26° ; but the perfect equivalent of heat as established definitely by Joule's investigations and others subsequent, was that the heat required to raise 1 Ib. of water 1° in temperature would raise 1 Ib. a height of 772 feet, and 1 Ib. heated 26° would raise 1 Ib. a height of 772 x 26 or 20,072 feet ; hence the economy of the elevator was as 36 to 20,072, or only -^th of the theore- tical perfect duty of the heat. A very good pumpiug-engine realized £th of the theoretical effect, and ordinary steam-engines realized T\-th to TVth, and were consequently 40 to 56 times superior in duty to the elevator. The elevator was therefore economically applicable only where fuel was no object, or as an injector where the heat came in again usefully, as in feeding a steam boiler. The injector, indeed, although inferior to a pump in mere propelling power, he considered the most perfect instrument for feeding boilers, so long as the supply-water was cool enough to allow it to work ; for then all the heat imparted to the water was returned into the boiler without any waste, whereas in using steam to work a pump the larger part of the heat was wasted by being thrown away with the exhaust steam. The in- jector, however, would not be economical if the supply water could be heated by other means free of expense, since its action required the supply water to be kept cool. The amount of condensation in the long steam pipe mentioned in the paper seemed small for such a length of pipe, and he thought a good deal of water must be carried across the depositing box by the current of steam and pass through into the elevator. He had seen lately in France a simple and efficient contrivance by M. Le Chatelier, for freeing the steam from water, by making the steam pipe from the boiler descend vertically into the depositing box, surrounded by a cylindrical and concentric casing, from the top of which the steam was taken off for the engine ; the wet steam rushing into the depositing box in a vertical current, carried for- ward all the water it contained down to the bottom of the box by the velocity imparted to it, while the steam itself turned sharp round the bottom of the steam pipe and ascended through the annular space, passing off dry, and the water was allowed to drain S/fi WILLIAM SIEMENS, F.R.S. 8 1 back into the boiler. This apparatus was applied to a boiler which previously consumed 8 Ibs. of water per Ib. of fuel, and the result was that the consumption was reduced afterwards to only 6 or 6f Ibs. of water real evaporation per Ib. of fuel, while the engine went, much faster in conse.quence of having drier steam. But where the steam simply shot across the top of the depositing vessel, as in the apparatus that had been described, he was satisfied that a considerable quantity of water must be lost by being carried across with it. OX A REGENERATIVE GAS FURXACE, AS APPLIED TO GLASSHOUSES, PUDDLING, HEATING, ETC. BY MR. C. WILLIAM SIEMENS.* THE arrangement of furnaces about to be described is applicable with the greatest advantage in cases where great heat has to be maintained : as in melting and refining glass, steel, and metallic ores, in puddling and welding iron, and in heating gas and zinc retorts, &c. The fuel employed, which may be of very inferior description, is separately converted into a crude gas, which in being conducted to the furnace has its naturally low heating power greatly increased by being heated to nearly the high temperature of the furnace itself, ranging to above 3000° Fahr. ; undergoing at the same time certain chemical changes whereby the heat developed in its subsequent combustion is increased. The heating effect produced is still further augmented by the air necessary for combustion being also heated separately to the same high degree of temperature, before mixing with the heated gas in the combustion chamber or furnace ; and the latter is thus filled with a pure and gentle flame of equal intensity throughout the whole chamber. The heat imparted to the gas and air before mixing is obtained from the products of combustion, which after leaving the furnace are reduced to a temperature frequently not * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers, 1862, pp. 21-36, and 40-44. VOL. I. G 82 THE SCIENTIFIC PAPERS OF exceeding 250° Fahr. on reaching the chimney, whereby great economy in fuel is produced, with other advantages. The transfer of heat from the products of combustion to the air and gas entering the furnace is effected by means of regenerators, the principle of which has been recognised to some extent since the early part of the present century, but has not hitherto been carried out in any useful application in the arts, unless the respira- tor invented by Dr. Jeffreys be so considered. The discovery of this principle is ascribed to Rev. Mr. Stirling of Dundee, who in conjunction with his brother, James Stirling, attempted as early as the year 1817 to apply it to the construction of a hot-air engine : their engine did not however succeed, nor did Captain Ericsson's later attempts in the same direction lead to more satis- factory results. The economical principle of the regenerator having attracted the writer's attention in 1846, he constructed in the following year an engine in which superheated steam was used in conjunction with the regenerator : many practical difficulties however prevented a realisation of the success which theory and experiments appeared to promise ; but it is gratifying to find that one principle then adopted, that of superheating the steam, has since received the sanction of an extended application. The employment of regenerators for getting up a high degree of heat in furnaces was suggested in 1857 by the writer's brother, Mr. Frederick Siemens, and has since been worked out by them conjointly through the several stages of progressive improvement. The results obtained by the earlier applications of the principle were communicated by the writer in a paper read at a former meeting of this Institution (see Proceedings Inst. M.E., 1857, page 103) * : and two or three of the furnaces then described, employed for heating bars of steel, remain still in operation. In attempting however to apply the principle to puddling and other larger furnaces, serious practical difficulties arose, which for a con- siderable time frustrated all efforts ; until by adopting the plan of volatilising the solid fuel in the first instance, and employing it entirely in a gaseous form for heating purposes, practical results were at length attained surpassing even the sanguine expectations previously formed. * Vide ante, p. 62. S/fi WILLIAM SIEMENS, F.R.S. 83 1 11 the early form of the regenerative heating furnace, which has been in continuous work during the lost three years for heating Icirs of steel at Messrs. Marriott and Atkinson's Steel Works, Sheffield, and also at the Broughton Copper Works, Manchester, there is a single fireplace containing a ridge of fuel fed from the top ; and two heating chambers, in which the bars of metal to be licatrd are laid, with a regenerator at the end of each chamber, by which the waste heat passing off from the furnace is intercepted on its way to the chimney, and transferred to the air entering the furnace. Each regenerator is composed of a mass of open fire- bricks, exposing a large surface for the absorption of heat, through which the products of combustion are made to pass from the furnace, and are thus gradually deprived of nearly all their heat previous to escaping into the chimney : the end of the regenerator nearest the furnace becomes gradually heated to nearly the tempera- ture of the furnace itself, while the other end next the chimney remains comparatively cool. The direction of the draught being now reversed by means of a valve, the air entering the furnace is made to pass through the heated regenerator in the contrary direction, encountering first the cooler portions of the brickwork, and ac- quiring successive additions of heat in passing through the re- generator, until it issues into the first chamber of the furnace at a very high temperature, and traversing the ridge of fuel produces a flame which fills the second heating chamber ; whence the products of combustion passing through the second cold regenera- tor deposit their heat successively in the inverse manner, reaching the chimney comparatively cool. By thus alternating the current through the two regenerators, a high degree of temperature is maintained constantly in the furnace. This arrangement of fur- nace is evidently applicable only in exceptional cases where two chambers are to be heated alternately, nor does it admit of being carried out upon a large scale. In heating a single chamber the expedient was resorted to of providing two fireplaces to be traversed in succession by the heated air, with the heating chamber placed between, as in the furnace shown in the drawings accompanying the previous paper (Proceedings Inst. M.E., 1857, Plate 118). Here the difficulty arose that the air, the oxygen of which was already combined with carbon (forming carbonic acid) in traversing the first fireplace, o 2 84 THE SCIENTIFIC PAPERS OF took up a second equivalent of carbon (forming carbonic oxide) in traversing the second, so that the fuel of the second fire was con- sumed to no purpose. In order to dimmish this loss and also avoid impairing the draught by a double resistance, the ridges of fuel were discontinued and the coal was fed into the furnace from the sides, resting on a solid hearth, to be there volatilised by the heated air passing over it. By frequently stirring the first fire its combustion was favoured until the current was reversed, when it was left undisturbed until the next change, and so on alternately. It was found very difficult however to maintain an active and uniform combustion and to burn the purely carbonaceous substance that was left in the fireplace after the gaseous portion of the fuel had been volatilised ; and it had frequently to be raked out in order to make room for fresh gaseous fuel. This circumstance led to the first step towards the employment of fuel in the form of gas, by providing a small grate below the heap of fuel, through which a gentle current of air was allowed to enter, forming car- bonic oxide, which afterwards further combined with oxygen on meeting with the hot current of air entering the furnace from the regenerator. The two fireplaces of alternating activity were how- ever attended with considerable practical inconvenience : the furnacenien in particular disliked the idea of attending two fire- places instead of one, and being little interested in the saving of fuel, took no pains to work the furnace in a satisfactory manner. It therefore became necessary to devise a plan of heating a single chamber continuously by one fireplace, in combination with the alternate reversal of currents through the regenerators, but without reversing the direction of the flame. This was accom- plished by means of double reversing valves, and was practically carried out in a puddling furnace that worked for a considerable length of time at the ironworks of Messrs. K. and W. Johnson near Manchester. The two regenerators were placed longitudinally side by side, with a flue between, underneath the puddling chamber, and the fireplace was put at one end of the puddling chamber, as in an ordinary puddling furnace, and fed with fuel from above. The heated air from the first regenerator was brought up at the back of the fireplace, and meeting there with the fuel produced the required flame in the puddling chamber ; whence the products of combustion passed down at the end of the chamber, and were SSK WILLIAM SIEMENS, F.R.S. 85 •il buck along the flue below to the hot end of the second Tutor, through which they made their way to the chimney. For reversing the currents through the regenerators two valves led, connected by a lever, one at the hot end of the Mcrators near the fire, and the other at the cool end next the chimney ; whereby the heated air was made to enter the fireplace by the same passage as previously, and the direction of the flame through the puddling chamber was not changed. By this arrange- ment the regenerative furnace was assimilated as nearly as could be to an ordinary puddling furnace in form and mode of working. The few furnaces constructed in this manner produced a great heat with little more than one-half the consumption of fuel of ordinary furnaces in doing the same amount of work. A con- siderable saving of iron was also effected in puddling, owing to the absence of strong cutting draughts, a mild draught being found sufficient to produce the necessary heat. There still re- mained drawbacks however which prevented an extensive appli- cation of this form of furnace : the fire required frequent attention, and it was difficult to maintain a uniform volume of flame in the furnace ; the reversing valve at the hot end of the regenerators was moreover liable to get out of order, and the furnace was costly to erect. The most important step in the development of the regenerative furnace has been the complete separation of the fireplace or gas producer from the heating chamber or furnace itself. When a uniform and sufficient supply of combustible gas is ensured, it can evidently be heated just like the air, by being passed through a separate regenerator before reaching the furnace, whereby its heating power is greatly increased. The difficulty of maintaining a uniform flame in the furnace is thereby certainly removed, and there is no longer any necessity for keeping the flame always in the same direction through the furnace, since the gas can be introduced with equal facility at each end of the heating chamber in turn, and the periodical change of direction of the flame through the furnace tends only to make the heat more uniform through- out : whereas in the previous plan of employing solid fuel for heating in the furnace, the relative position of the fireplace and heating chamber being fixed and unchangeable required tne direc- tion of the flame to be kept always the same, unaltered by the 86 THE SCIENTIFIC PAPERS OF reversal of currents through the regenerators. The new plan of a separate gas producer has now been successfully earned out in practice, and there are already a considerable number of the regenerative gas furnaces in satisfactory operation in this country and on the continent, applied to glasshouses, iron furnaces, &c. In the neighbourhood of Birmingham, at Messrs. Lloyd and Summerfield's Glass Works, a flint glass furnace constructed upon this plan has now been in continuous operation for nearly twelve months, and affords a good opportunity for ascertaining the con- sumption of fuel of the regenerative furnace as compared with the previous furnace performing the same work. At the Glass Works of Messrs. Chance Brothers and Co. near Birmingham, the regene- rative gas furnace has been under trial for the same length of time, and has latterly been adopted for the various purposes in crown and sheet glass making upon a very large scale. Messrs. James Russell and Sons, Crown Tube Works, Wednesbury, are also applying the furnace to the delicate operation of welding iron tubes, and in a short time will probably employ no solid fuel for any furnaces at their works. Another flint glass furnace erected by Messrs. Osier in Birmingham, and several puddling furnaces erected by Messrs. Gibbs Brothers at Deepfields, and by Mr. Richard Smith at the Round Oak Iron Works, are amongst the latest applications of the regenerative gas furnace, the designs having in all cases been furnished by the writer and carried out under his brother's immediate superintendence. The gas producer is shown in Figs. 1, 2, and 3, Plates 7 and 8 : Fig. 1 is a longitudinal section, Fig. 2 a front elevation and transverse section at the front, and Fig. 3 a transverse section at the back. The producers are entirely separate from the furnace where the heat is required, and are made sufficient in number and capacity to supply several furnaces. The fuel, which may be of the poorest description, such as slack, coke dust, lignite, or peat, is supplied at intervals of from 6 to 8 hours through the covered holes A, Figs. 1 and 2, and descends gradually on the inclined plane B, which is set at an inclination of from 45° to 60° accord- ing to the nature of the fuel used. The upper portion of the incline B is made solid, being formed of iron plates covered with firebrick ; but the lower portion C is an open grate formed of horizontal flat steps. At the foot of the grate C is a covered S/K WILLIAM SIEMENS, F.R.S. 87 water trough D, filled with water up to a constant level from the small feeding cistern E, supplied by a water pipe with a ball tap. Tlii- large opening under the water trough is convenient for draw- ing out clinkers, which generally collect at that point. The small stoppered holes F F at the front and G- G at the top of the pro- ducer are provided to allow of putting in an iron bar occasionally to break up the mass of fuel and detach clinkers from the side walls. Each producer is made large enough to hold about 10 tons of fuel in a low incandescent state, and is capable of converting about 2 tons of it daily into a combustible gas, which passes off through the opening H into the main gas flue leading to the furnaces. The action of the gas producer in working is as follows : the fuel descending slowly on the solid portion B of the inclined plane, Plate 7, becomes heated and parts with its volatile constituents, the hydro-carbon gases, water, ammonia, and some carbonic acid, which are the same as would be evolved from it in a gas retort. There now remains from 60 to 70 per cent, of purely carbonaceous matter to be disposed of, which is accomplished by the slow current of air entering through the grate C, producing regular combustion immediately upon the grate ; but the carbonic acid thereby pro- duced, having to pass slowly on through a layer of incandescent fuel from 3 to 4 feet thick, takes up another equivalent of carbon, and the carbonic oxide thus formed passes ofi' with the other combustible gases to the furnace. For every cubic foot of com- bustible carbonic oxide thus produced, taking the atmosphere to consist of £th part by volume of oxygen and £ths of nitrogen, two cubic feet of incombustible nitrogen pass also through the grate, tending greatly to diminish the richness or heating power of the gas. All the carbonaceous portion of the fuel is not however volatilised on such disadvantageous terms : for the water trough D at the foot of the grate, absorbing the spare heat from the fire, emits steam through the small holes I under the lid ; and each cubic foot of steam in traversing the layer of from 3 to 4 feet of incandescent fuel is decomposed into a mixture consisting of one cubic foot of hydrogen and nearly an equal volume of carbonic oxide, with a variable small proportion of carbonic acid. Thus one cubic foot of steam yields as much inflammable gas as five cubic feet of atmospheric air ; but the one operation is dependent 88 THE SCIENTIFIC PAPERS OF upon the other, inasmuch as the passage of air through the fire is attended with the generation of heat, whereas the production of the water gases, as well as the evolution of the hydro-carbons, is carried on at the expense of heat. The generation of steam in the water trough being dependent on the amount of heat in the fire, regulates itself naturally to the requirements ; and the total production of combustible gases varies with the admission of air. And since the admission of air into the grate depends in its turn upon the withdrawal of the gases evolved in the producer, the production of the gases is entirely regulated by the demand for them. The production of gas may even be arrested entirely for 12 hours without deranging the producer, which will begin work again as soon as the gas valve of the furnace is reopened ; since the mass of fuel and brickwork retain sufficient heat to keep up a dull red heat in the producer during that interval. The gas is however of a more uniform quality when there is a continuous demand for it, and for this reason it is best to supply several furnaces from one set of producers, so as to keep the producers constantly at work. The opening H leading from each producer into the main gas flue can be closed by inserting a damper from above, as shown in Fig. 7, in case any one of the producers is required to be stopped for repairs or because part of the furnaces supplied are out of work. It is important that the main gas flue leading to the furnaces should contain an excess of pressure however slight above the atmosphere, in order to prevent any inward draughts of air through crevices, which would produce a partial combustion of the gas and diminish its heating power in the furnace, besides causing a deposit of soot in the flues. It is therefore necessary to deliver the gas into the furnace without depending upon a chimney draught for that purpose. This could easily be accomplished if the gas producers were placed at a lower level than the furnaces, but as that is generally impossible, the following plan has been adopted. The mixture of gases on leaving the producers has a temperature ranging between 300° and 400° Fahr., which must under all circumstances be sacrificed, since it makes no difference to the result at what temperature the gas to be heated enters the regenerators, the final temperature being in all cases very nearly that of the heated chamber of the furnace or say 2500° Fahr. SfX WILLIAM SIEMENS, F.R.S. 89 The initial heat of the gas is therefore made available for produc- ing a plenum of pressure by making the gas rise about 20 feet above the producers, then carrying it horizontally 20 or 30 feet through the wrought iron tube J, Plate 7, and letting it again descend to the furnace, as shown by the arrows in Fig. 1. The horizontal tube J being exposed to the atmosphere causes the gas to lose from 100° to 150° of temperature, which increases its density from 15 to 20 per cent, and gives a preponderating weight to that extent to the descending column, urging it forwards into the furnace. The application of the regenerative gas furnace as a plate glass melting furnace is shown in Plates 9 to 12, which represent a melting furnace now in course of erection at the British Plate Glass "Works near St. Helen's. This furnace does not differ materially from the regenerative gas furnaces previously erected and at work at Messrs. Chance's and Messrs. Lloyd and Summer- field's, but is selected in preference because it is the most improved in details of construction. Plate 9 shows a longitudinal section of the furnace, Plate 10 a transverse section, and Plate 11 a sectional plan above and below the bed or " siege " as it is termed of the furnace. Figs. 7, 8, and 9, Plate 12, show the detail of the gas and air valves. The heating chamber A of the furnace, Figs. 4 and 5, contains twelve glass pots B, which are got out through the side doors when the glass is ready for casting upon the moulding table. Underneath are placed transversely the four regenerators C C, composed of open firebricks built up on a grating, which are arched over at the top and support the bed or siege D of the furnace. The regenerators work in pairs, the two under the right hand end of the siege communicating with that end of the heating chamber, while the other two communicate with the opposite end, as shown in Fig. 4. The gas enters the chamber through the three passages E, Figs. 5 and 6, and the air through the two intermediate passages F, whereby they are kept entirely separate up to the moment of entering the furnace, but are then able immediately to mingle intimately, producing at once an intense and uniform flame in the heating chamber. The siege D is built of firebrick, with a number of transverse channels, shown black in Figs. 4 and 8, through which the cold entering air is made to 9O THE SCIENTIFIC PAPERS OF pass on its way into the air flue G-, as shown by the arrows in Fig. 5 ; by this means the siege is kept comparatively cool, so that no fluid glass can pass through crevices into the regenerators. Any melted glass that may fall from the heating chamber through the apertures at the ends of the siege does not get into the regene- rators, but falls into the pockets M, Fig. 4, whence it can be removed through the opening at the bottom. The passage N, Fig. 5, by which the air enters, affords the means of getting at the regenerators through an opening at the end of each. From the air flue G-, Fig. 8, the entering air is directed by the reversing valve H into the air regenerator, as shown by the arrows, and there becomes heated ready for entering the furnace ; at the same time the gas entering from the gas flue I, Fig. 7, is directed by the reversing valve J into the gas regenerator, where it becomes heated to the same temperature as the air. Similarly the products of combustion on leaving the opposite end of the furnace pass down through the second pair of regenerators, as shown by the arrows in Fig. 4, and after being here deprived of their heat are directed by the reversing valves H and J into the chimney flue K. When the second pair of regenerators have become considerably heated by the passage of the hot products of combustion, and the first pair correspondingly cooled by the entering air and gas, the valves H and J are reversed by the hand levers, as shown dotted in Figs. 7 and 8, causing the currents to pass through the regenera- tors and the heating chamber in the contrary direction, whereby the hot pair of regenerators are now made use of for heating the gas and air entering the furnace, while the cool pair abstract the heat from the products of combustion escaping from the furnace. The supply of air and gas to the furnace is regulated by the adjustable stop valves L, whereby the nature and volume of the flame in the furnace may be varied at pleasure ; whilst the chim- ney damper is used to regulate the amount of pressure in the furnace in relation to the atmosphere, so as to allow the opening of working holes. The construction of furnace above described may be varied in many ways to suit local circumstances. The regenerators are in some instances not placed immediately under but at the side of the furnace ; but it is important that they should always be placed at a lower level than the furnace, in order that the air and gas WILLIAM SIEMENS, l-.R.S. 9! may rise naturally into the heating chamber, forming there a plenum of pressure. Plates 13, 14, and 15 show the application of the regenerative gas furnace as a round flint glass furnace. Plates 13 and 14 show vertical sections of the furnace taken at right angles to each other, and Plate 15 a sectional plan above and below the siege. The round form of furnace is found convenient in flint glass-houses, affording the greatest amount of accommodation to the glass- blowers. The four regenerators C are here arranged below the siege as before, and the air and gas from the hot regenerators enter the annular heating chamber A at one side of the furnace, as shown by the arrows in Fig. 10, and pass all round it, the products of combustion escaping at the opposite side into the cold regenerators. The direction of the current is reversed at intervals exactly as in the plate glass furnace already described, by means of the re- versing valves H and J in the air and gas passages, Figs. 11 and 12. Furnaces of this construction have lately been got to work at Namur in Belgium and at Montlucon in France, and several others of the same description are in course of erection at the present time. The furnace just started by Messrs. Osier in Birmingham also partakes of this form, being made semicircular. In setting out each individual furnace, the heating effect required, the quality of the fuel employed, and the particular nature of the process to be performed, have to be considered. The amount of heat required determines the capacity of the regenerators ; and the gas regenerators require fully as large a capacity as the re- generators, and sometimes even a greater. This would perhaps hardly be expected, but will be seen to be the case from the following considerations. The gases proceeding from the gas producers are a mixture of olefiant gas, marsh gas, vapour of tar, water and ammoniacal compounds, hydrogen gas and carbonic oxide ; besides nitrogen, carbonic acid, some sulphuretted hydrogen, and some bisulphuret of carbon. The specific gravity of this mixture averages 0'78, that of air being TOO ; and a ton of fuel, not including the earthy remnants, produces according to calculation nearly 64,000 cubic feet of gas. By heating these gases to 8000° Fahr. their volume would be fully six times increased, but in reality a much larger increase of volume ensues, in consequence of some important chemical changes effected at the same time. 92 THE SCIENTIFIC PAPERS OF The olefiant gas and tar vapour are well known to deposit carbon on being heated to redness, which is immediately taken up by the carbonic acid and vapour of water, the former being converted into carbonic oxide and the latter into carbonic oxide and pure hydrogen. The ammoniacal vapours and sulphuretted hydrogen are also decomposed, and permanently elastic gases with a pre- ponderance of hydrogen are formed. The specific gravity of the mixture is reduced in consequence of these transformations to 0'70, showing an increase of volume from 64,000 to nearly 72,000 cubic feet per ton of fuel, taken at the same temperature. This chemical change represents a large absorption of heat from the regenerator, but the heat is given out again by combustion in the furnace, enhancing the heating power of the fuel beyond the increase due to elevation of temperature alone. The chemical transformation is also of importance in preventing " sulphuring ; " for it is believed that the sulphur in separating from its hydrogen takes up oxygen supplied by the carbonic acid and water, formiug sulphurous acid, a firm compound, which is not decomposed on meeting with metallic oxides in the furnace. This view is so far borne out by experience that glass containing a moderate proportion of lead in its composition may be melted in open crucibles without injury, instead of requiring covered pots for the purpose as in ordinary furnaces. In dealing with the highest quality of flint glass, however, it is found necessary to retain covered pots ; but every other description of glass is melted in open pots. In all branches of glass manufacture, saving of fuel is of relatively small moment as compared with the im- provement effected in the colour and general quality of the glass by the use of the regenerative gas furnace, owing to the absence of dust and cinders and the high degree of temperature which may with safety be maintained throughout the heating chamber. These advantages of the regenerative gas furnace are of equal value in the case of puddling and welding iron. Plates 1C and 17 represent a puddling furnace constructed on this plan. Fig. 13 is a longitudinal section of the furnace, Fig. 14 a sectional plan of the puddling chamber, and Fig. 15 a sectional plan of the re- generators ; Fig. 16 is a transverse section at the end of the furnace, and Figs. 17 and 18 are vertical sections through the gas and air passages. WILLIAM SIEMENS, F.K.S. 93 The four regenerators C are in this case arranged longitudinally underneath the puddling chamber A, which may be of the usual form. In order to complete the combustion of the gas and air in passing through the comparatively short length of the puddling chamber, it is necessary to mix them more intimately than is requisite in the large glass furnaces previously described. For this purpose a mixing chamber 0, Fig. 13, is provided at each end of the puddling chamber, and the gas and air from the regenerators are made to enter the mixing chamber from opposite sides, as shown in Fig. 16 ; the gas aperture E is moreover placed several inches lower than the air aperture F, so that the lighter stream of gas rises through the stream of air while both are urged forward into the puddling chamber, and an intense and perfect combustion is produced. The mixing chambers 0 are sloped towards the furnace, as shown in Fig. 13, in order to drain them of any cinders which may get over the bridge. The reversal of the current through the furnace is effected about eveiy hour by the reversing valves H and J in the air and gas flues, the arrangement of which is exactly similar to that already described in the glass furnace : the supply of gas and air is regulated by the throttle valves L, and the draught through the furnace by the ordinary chimney- damper. This same arrangement, with obvious modifications, may be applied also to blooming and heating furnaces, the advantages in both cases being a decided saving of iron, besides an important saving in the quantity and quality of the fuel employed. The space saved near the hammer and rolls by doing away with fireplaces, separate chimney-stacks, and stores of fuel, is also a considerable advantage in favour of the regenerative gas furnace in ironworks. The facility which it affords for either concentrating the heating effect or diffusing it equally over a long chamber, by effecting a more or less rapid mixture of the air and gas, renders the furnace particularly applicable for heating large and irregular forgings or long strips or tubes which have to be brought to a welding heat throughout. It has already been applied to a considerable extent in Germany for heating iron, having been worked out there under the direction of the writer's eldest brother, Dr. Werner Siemens, who has also contributed essentially to the development of the system. The furnaces at the extensive iron and 94 THE SCIENTIFIC PAPERS OF engine works of M. Borsig of Berlin are being remodelled for the adoption of this system of heating, as have also been those at the imperial factories at "Warsaw. Another important application of the regenerative gas furnace is as a steel melting furnace, in which the highest degree of heat known in the arts is required, presenting consequently the greatest margin for saving of fuel. Plate 18 represents a regenerative steel furnace which has been in satisfactory operation in Germany for a considerable length of time, being worked with lignite, a fuel little superior to peat in heating power. This application of the re- generative gas furnace is indeed rapidly extending in Germany, but has not yet practically succeeded in Sheffield where it was also tried : it is however in course of application at the Brades Steel works near Birmingham. Fig. 19 is a longitudinal section of the furnace, Fig. 20 a transverse section, and Fig. 21 a sectional plan. The two pairs of regenerators C C, Figs. 19 and 21, are situated at the ends of the long melting chamber A, in which the steel melting pots B B are arranged in a double row. The chamber is covered with iron cramped arch-pieces P, any of which can be readily removed for getting at the pots. The arrangement of the reversing valves and the air and gas flues is similar to that in the glass furnace previously described. Other applications of the regenerative gas furnace are being carried out at the present time : among which may be mentioned one to brick and pottery kilns for Mr. Humphrey Chamberlain near Southampton, for Messrs. Cliff of Wortley near Leeds, and for Mr. Cliff of the Imperial Potteries, Lambeth ; also to the heating of gas retorts at the Paris General Gas Works, and at the Chartered Gas Co.'s Works, London. The description already given however is sufficient to show the facility with which this mode of heating may be adapted to the various circumstances under which furnaces are employed. The important application of the regenerative system to hot-blast stoves for blast furnaces by Mr. E. A. Cowper has already been separately communicated to this Institution (see Proceedings Inst. M. E., 18GO, page 54). The experience hitherto obtained with the regenerative mode of heating shows that it is attended with the greatest proportionate advantage in localities where good coal is scarce but where an WILLIAM SIEMENS, F.R.S. 95 inferior fuel abounds. This applies most forcibly to the South Staffordshire district, where the best coal in lumps is worth 12s. Gd. per ton, whereas good slack can be had at 3s. or 4s. per ton. The question gains moreover in importance when it is considered that, according to the best authorities, the thick coal of the district is coming to an end, while millions of tons of coal-dust have accu- mulated, of no present commercial value, which on being converted into gas in the manner described by means of the gas producers would acquire a heating value equal at any rate to the same weight of the best coal in the manner in which it is at present used. Considering also the proximity of the pits to the ironworks in this district, it may be suggested whether the gas producers being of very simple construction might not with advantage be placed near the banks of fuel above or even under ground, the gas being con- veyed to the works by a culvert so as to supersede carting of the fuel. Such an arrangement might notably contribute to per- petuate the high position which South Staffordshire has so long maintained as an iron producing district. In the discussion of the Paper MR. SIEMENS observed that the essential features of the regene- rative gas furnace described in the paper, as now matured and carried out in practice, were the separate gas producers, in which the solid fuel was converted into a gaseous form for use in the furnace, and the regenerators, in which the gas and air were each raised to a high degree of temperature previous to their mixture and com- bustion in the furnace, whereby the heat produced by the combus- tion was very greatly increased. In the gas producers the fuel underwent a slow digestion, and the whole of the combustible constituents were drawn off into the furnace in the form of gas. while the incombustible ash or valueless portion of the fuel was left behind. The gas produced was of a crude nature in its original state, and much inferior to common gas for illuminating or heating purposes, and if burnt only with ordinary air would give very poor results : but it underwent a further change in the regenerator where it was heated up to about 3000° Fahr., at which temperature the several gaseous compounds contained in it became decomposed, the rich carburetted hydrogen depositing g6 THE SCIENTIFIC PAPERS OF carbon which was at once taken up by the vapour of water present, producing carbonic oxide and hydrogen ; so that there was then present the greatest amount of free hydrogen, which had three or four times the heating power of any other gas. The air used for burning the gas was also heated by the regenerator up to about 3000° and then mixed with the gas at the same temperature, producing perfect and most intense combustion : the regenerative system thus presented the means of attaining an almost unlimited degree of temperature. At the same time there was no great current or draught through the furnace, since the chimney draught was not required in this furnace to urge the combustion as in ordinary furnaces heated by solid fuel, and the cutting draughts destructive of ordinary furnaces were therefore entirely avoided. There was no difficulty in keeping up an abundant supply of gas if there were enough gas-producers and if the passages to the furnace were large enough ; the puddling chamber could then be completely filled with flame at any moment, or the flame could be as instantly stopped, by means of the regulating valves and chimney damper. By having separate air and gas valves the chemical nature or heating power of the flame could also be regulated to any desired degree, by altering the proportion of air admitted with the gas, so as to produce any required effect from a smoky flame to a pure bright flame. In the furnace for flattening the cylinders of sheet glass a quantity of bright clean flame was required for softening the glass without melting it ; but in the melting furnace, on the contrary, an intense soaking heat was wanted, with very little variation : and both sorts of heat were obtained in the new furnace from the same gas main, by simply regulating the quantities of air and gas admitted. Of the puddling furnaces two were now just being started in the South Staffordshire district, but about twenty puddling and heating furnaces had been at work in Germany for some months already with complete success. They had not yet obtained any absolute results with the regenerative puddling furnaces in this country, but at present the time of working a heat was about the same as in the ordinary puddling furnaces. The puddling furnaces working on this plan near Wolverhampton were not yet in a complete state for operation as they had been expected to be before this time, on account of a defect in the chimney flue and SfK WILLIAM SIEMENS, F.R.S. 97 in the drainage of the premises. No permanent difficulty could be anticipated in carrying out the new puddling furnace in practice, on account of the large amount of experience gained in the application of the regenerative furnace for other purposes. There was only one chimney to a number of furnaces, and the draught was simply regulated by a separate damper to each furnace. The chimney was not required to be lined with fire- brick, but was built of red bricks, as the heat passed off from the puddling chamber was all arrested in the regenerators and the chimney was always cool. The chimney damper regulated only the force of draught in each furnace, but the quantity and quality of flame were regulated by the gas valve. No furring- up had taken place in the regenerators, because the steam mixed with the gas would volatilise any carbon that might otherwise be deposited on the walls of the regenerator : it was for this purpose that care was taken to supply an excess of vapour of water from the water trough in the grate of the gas producer A regenerative heating furnace had been three years in constant work at Messrs. Marriott and Atkinson's Steel Works, Sheffield, heating" the steel for the rolling mill, and no inconvenience had been experienced from vitrification of the materials of the fur- nace. Mr. Atkinson was prevented from being present at the meeting himself as he had wished, but had sent "a letter ex- pressing his satisfaction with the furnace, as especially advan- tageous for heating steel on account of the uniformity of the heat obtained in it. The glass-melting furnace at Messrs. Lloyd and Summerfield's had also been in constant work for nearly a year without sustaining any injury from the great heat employed in it. The temperature in the furnace was at least a full welding heat of iron, as a bar of iron held in it dropped melted in half a minute ; the hot end of the regenerator had a temperature of about 3000° Fahr., and the heat in the furnace must of course be greater. For measuring such high temperatures he made use of the pyrometer described at a previous meeting,* consisting of a well protected vessel containing a measured quantity of water, and a piece of copper or platinum of definite size, which was exposed for a suffi- cient length of time to the heat to be measured and was then dropped * See Proceedings of the Institution of Mechanical Engineers, 1860, p. 59. VOL. I. H 98 THE SCIENTIFIC PAPERS OF into the water ; the rise of temperature produced in the water showed the degree of heat upon a thermometer scale graduated in the proper proportion, and the results thus obtained must certainly be correct within 10° or 15" Fahr. Rather larger yields were obtained with the regenerative puddling furnace, but it had not been long enough at work yet to give any definite results. The puddling furnaces at work in Germany however showed at least 4 or 5 per cent, increase in the yield of iron, and this result was indeed to be expected, because the new furnace was free from the cutting action of the flame produced by a strong draught, and the ball was surrounded on all sides by an equally hot flame. As regarded cost, Mr. Siemens said that the alteration of present fur- naces would be attended with a considerable expense, as there was all the extra bottom brickwork of the regenerators, besides the separate gas producers and the valves and mains ; but the separate chimneys for each furnace were saved, and the cost of maintenance was greatly reduced, judging from the condition of the glass furnaces that had been twelve months at work. In new works however the cost of construction of the regenerative puddling furnaces would not much exceed the total cost of the present furnaces complete ; and the new furnaces had the advantage of occupying only their own space, without requiring room for a coal pen to each furnace ; they could thus be built closer together and consequently more could be brought within reach of one hammer. Mr. Siemens thought a pair of the new puddling furnaces would cost about £300 complete. The regenerative glass furnaces hitherto erected had been very expensive in construction, having heavy iron plates in the sieges and a great deal of ironwork in the fittings of the furnace and in the gas producers, much of which had been greatly reduced or dispensed with in the furnaces sub- sequently put up. In starting the new plan of furnace he had thought it best to keep all the work very substantial, to be on the safe side for strength and durability ; and the gas producers had also been provided each with a separate gas tube and valve, so that each could be shut off from the furnace if desired, to avoid risk of the furnace being interfered with in its working by a defect at any particular point. S/A' WILLIAM SIEMENS, F.R.S. 99 In Hie discussion of the Paper "OX THE DISTILLATION OF COAL, THE UTILIZA- TION OF THE RESULTING PRODUCTS, AND THE MANQFACTURE OF COKE," by M. PERNOLET,* MR. C. W. SIEMENS said he had lately paid considerable attention to the subject of coke-making ; and he believed that the coke-ovens generally used, especially in the north of England, were very primitive. The admission of air into them caused a portion of the coke to burn, and the gases from the remaining coal, being driven out, went to waste. He thought it hardly possible to conceive anything more rude than that system, because those gases, possessing heating powers of nearly equal value to the remaining coke, were allowed to escape freely into the atmosphere, involving not only a great loss of fuel in the most valuable form, but also a serious nuisance in populous districts. As regarded the quality of the coke produced in the ordinary oven, it had been satisfactorily proved to be inferior to that produced in the close oven when properly arranged, although it was, perhaps, more lustrous in appearance. The reason of its real inferiority was, that the coke first acted upon by atmospheric air was partially burned ; but the carbonic acid formed by this combustion passed through the remaining mass in the oven, and robbed it of such an amount of carbon as was necessary to reduce the carbonic acid to carbonic oxide. Hence the earthy constituent of the coke was relatively increased, and, as was stated in the paper, the coke pro- duced in close ovens contained, for the same amount of earthy matter present, 1 5 per cent, pure carbon. This, with a poor description of coal, was a most important feature, irrespective of the value of the additional yield, both of coke and of the secondary products. As regarded the conversion of the ordinary coke-oven into a close oven — which he understood to be the subject of this paper — he considered that it was practicable, and that the kind of oven now brought before the notice of the Institution, had many ex- * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Yol XXIII., Session 1863-64, pp. 452-3. H 2 100 THE SCIENTIFIC PAPERS OF cellent qualities, but, that it was not the only one possessing im- portant improvements. The plan had been tried, indeed, at Lambeth, with this difference, that coal was burnt to effect the carbonization, the gases being used for illuminating purposes. Those ovens were being pulled down, because the gas produced in them was found to be deficient in brilliancy. Those most in use on the Continent were of two different descriptions. The first, was a semi- cylindrical horizontal oven, closed at the ends with movable doors, and provided with a covering arch forming an annular chamber, through which the gases generated in the oven circulated, and were consumed there by the admission of atmo- spheric air, in order to continue the distillation of the coal inside. That was an improvement, inasmuch as the gases did not go to waste ; and he believed ovens of that description were used at the Ebbw Yale works, with great effect. In South "Wales excellent coke was formed by mixing anthracite with bituminous substances, and by exposing the mixture to great heat in close ovens. Another description of coke-oven which he had seen in France, and which seemed to be a favourite in many establishments, was in the form of a number of upright retorts, and was known as the " Four Appold." Each retort was slightly conical, and was filled by shooting the coal from carts at the top. The gases evolved, passed through the sides of the retort, and were burnt there by the admission of atmospheric air. After a distillation of 24 hours or 40 hours, a trap-door at the bottom was opened, and the whole of the coke, amounting to several tons, was dropped into railway trucks, or carts, and carried away. That was another instance where the full value of the carbonaceous material was obtained. He might mention, also, an oven he had lately tried, which was based upon the same principle, as regarded the general arrangement. It was an upright retort, but, instead of being simply heated by the gas issuing from the coal, a poorer kind of gas was used, which had been previously heated by passing through a regenerator ; the air necessary to combustion being also passed through a regenerator placed at the side of the retorts, so that only a portion of the gases evolved was required to heat the coal, the rest being applied to other uses, either for illuminating purposes or for the heating of working furnaces, &c. He had noticed the remarkable fact, that when the gas was drawn from the bottom of the retort, S//? WILLIAM SIEMENS, F.R.S. IOI instead of from the top, a much higher illuminating power was obtained. Operating on Staffordshire coal, which, in the ordinary way, yielded gas of about 10 candle-power, he had obtained, by this method, an illuminating power of eighteen candles, or twenty candles. Very little tar, or other secondary products were formed because, in passing over the heated surfaces, they were decomposed and turned into gas, or combined with the coke, which latter was thereby increased in hardness. It might be considered a drawback that there were no secondary products, but it was in reality not BO ; for in most places the tar and ammoniacal liquor were difficult to dispose of, and if used to improve the coke they were applied to the best advantage. He thought the question of coke making had oeen treated too lightly. The present tendency of engineers was to burn coal in locomotive engines, because coking, as generally performed, was a wasteful process, in which the mosfi valuable part of the fuel was lost. But by improving the coke ovens, and by making judicious use of the gases, both for illuminating and heating purposes, coke might be produced at a reduced rate, to be used for locomotive engines and blast-furnaces, and a larger aggregate saving of coal might be effected. In the discussion of the Paper " ON GIFFARD'S INJECTOR," By JOHN ENGLAND, M. Inst. C.E., MR. C. "VV. SIEMENS* said he thought that the cause of action of this instrument should be better understood than it appeared to be, on account of the physical principles involved, which were, without necessity, at present invested with mystery. He could not agree in the view, expressed by Mr. Phipps, that the action of the Injector was due to the circumstance, that the impact produced * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Vol. XXIV. Session, 1864-65, pp. 222-225, and 236-238. IO2 by a jet on a solid surface was equal to double the pressure due to the area which produced it ; but he thought it might be shown, that the jet produced by the steam possessed a very much higher velocity than a jet of water produced by the same pressure which would come out to meet it from the boiler. Thus the steam from the boiler issued with a velocity v = 8 Jh, or nearly so, neglecting the error arising from the circumstance of its being an elastic fluid ; while the water of the boiler would issue with a velocity represented also by the formula v' = 8 Jti ; but the pressure being the same in the two cases, it followed that the height of the column h was superior to h' in the proportion of the relative densities of steam and water. Hence the velocity v of the steam would exceed the velocity v' of the water in the proportion of *J/t : *J~R, or in the case of steam of four atmospheres' pressure, v\v'= Jl : ^47 7, water being 477 times denser than steam of that pressure, or v : v' = 1 : 21-8. It was therefore evident, that every particle of steam rushed forward with a velocity nearly twenty-two times greater than that with which the water could meet it, only if it were to rush forward in its elastic state, it was evident that each particle of steam would have to encounter 477 particles of water within the same volume, and must be forced back notwithstanding its superior velocity. But if the steam were imagined to be condensed between the point of issue and that of its meeting with the jet of water, if, for instance, its elastic force could be destroyed by making it pass through an infinitely cold space, then the result would be a very contracted jet of water passing forward with the extraordinary velocity of v' = 8 *Jh' = 8 ^/477 x 3 x 32 = 1712 feet per second, meeting a column of v — 8 Jh = 8 *J3 x 32 = 78 feet per second. The effect would be, that the column of water resulting from the condensation of the steam would pierce the comparatively sluggish jet of water meeting it, as though it were a steel wire forcing its way into the boiler. This was, however, an impossible position, for the steam could not be condensed by itself spon- taneously. But the injector effected the spontaneous condensa- tion of the jet of steam by incorporating with it a sufficient quantity of cold water, which was so regulated, that the mean velocity of the united jet of steam and water still exceeded the velocity of 78 feet per second with which the opposing jet from WILLIAM SIEMENS, F.R.S. 103 the boiler would meet it. Supposing the initial temperature of the water to be about 70" Fahr., the weight of the condensing water should exceed the weight of the condensed steam about ten times to effect perfect condensation ; the velocity of the united 1 712 jet or sheaf would be in this case = -r^ — = 155 feet per second, or nearly doubly sufficient to force its way into the boiler. It might here be remarked, that the author of the paper was dourly in error when he stated that the steam was only partially condensed in the sheaf. Uncondensed steam encountering water could not drive it back ; but a column of water encountering another column of inferior velocity must drive it back. It was essential that water of sufficiently low temperature should be brought into contact with the jet of steam to effect its entire condensation, without reducing its velocity below the limit indicated by the imaginary velocity of the opposing column. In the case assumed, the weight of condensing water, or of the water injected into the 1 712 boiler, must not exceed the weight of condensed steam by -— - 78 = 22 times, or making allowance for losses of effect, say by 18 times. Taking the total heat of steam at 1,150 units, it followed that the rise of temperature of the injected water would be - = 64° Fahr., and assuming that the final temperature of 18 the sheaf must not exceed 190°, in order to effect entire con- densation, it followed that the initial temperature of the injected water mustjiot exceed 190 - 64 -= 126° Fahr. If it should be attempted, under the circumstances, to inject water of a tempera- ture exceeding 120° Fahr., the sheaf must break up, and the action of the instrument be paralyzed. On the other hand, the greatest quantity of water which each pound of steam would be able to take depended upon the relative velocity of steam and water when acted upon by the same pressure, and might be expressed by 1 712 -^wrr- = 22 Ibs. That would be the greatest quantity of water which each pound of steam could urge forward into the boiler, or could urge forward if there were no loss from friction or by the vortices formed. In reality it would probably not deliver much above half that quantity into the boiler. 104 THE SCIENTIFIC PAPERS OF The subject had been considered irrespective of the question of heat, but that, in his opinion, was a fallacious method, for, it would be seen, that without complete condensation the instrument could not act ; neither could its effect, nor the limits of its action, be determined, without taking into account the amount of heat contained in the steam and in the water, as well as their proper velocities when acted upon by pressure. Mr. Siemens thought the injector could only be advantageously applied as a motor, in cases where the water had not only to be raised but also to be heated, and its legitimate application would probably remain confined to the feeding of steam boilers. Its practical advantages were not overstated in the paper, where feed- water of sufficiently low temperature was used. The minimum temperature, to obtain an advantageous result, would be about 100° Fahr. In the case of a high-pressure engine, it was a question whether a heater and a pump would not be more advan- tageous than this instrument. The author had stated that 2'3 cubic feet of steam would be expended to pump one cubic foot of water into the boiler. But even this calculation, unfavourable as it might seem, still left a great margin in favour of the pump, inasmuch as the water could be raised by waste heat to nearly 212°. He believed that the injector would be found applicable with the greatest advantage in the case of marine engines, or of condensing engines in general, where there were no means of heating the feed-water to above 100°. Under such circumstances the power expended to work the feed-pump could be entirely saved, because although the injector would expend heat on the water, it would return the same to the boiler ; whereas the pump used the steam to work it, and gave nothing in return. Mr. Siemens said, the areas of the different jets of water and steam, which had been stated to be adopted in practice, agreed very well with his own calculations.* The areas were determined by the quantity of steam necessary to condense in order to impel the water. Taking the case of a pressure of 60 Ibs., or an effective pressure of three atmospheres, the steam was 477 times lighter than water, while its velocity was only in the ratio of J i77, or nearly 22 times greater than that of the water ; the * Vide Minutes of Proceedings of the Institution of Mechanical Engineer*, 1860, pp. 48-78. SJR WILLIAM SIEMENS, F.R.S. 105 consequence was, that the area must be larger to allow a given weight of steam to issue from an orifice, than if water issued under the same pressure, in the proportion of ^477 : «/ 1, or about 21 times the area. But, inasmuch as the quantity of water had to be increased ten -fold, it followed that -^th of 21 times, or 2'1 times, ought to be the area of the steam orifice as compared with the orifice in the boiler. This calculation agreed accurately with the proportions it had been found expedient to adopt ; but he was surprised to learn that the same proportions of area were given to the injector, although the conditions of its application, especially as regarded the pressure in the boiler, might be very different. With a pressure of twenty atmospheres, for instance, the density of the steam was 110 times less than that of the water ; therefore, the relative velocity would be as *J 110 : J 1, or as 10'5 : 1, and about double the area of steam would be required to supply the necessary quantity to impel the water forward into the boiler. He felt convinced many of the partial failures they had heard of might be due to this, — that the injector had been calculated, or determined experimentally, for ordinary high-pressure engines, but if applied to low-pressure, or very high-pressure engines, it failed to work satisfactorily. It could even be shown, that the injector was not applicable at all if the pressure exceeded certain limits. As, with a pressure of twenty atmospheres, the velocity of the steam was only 10 '5 times greater than that of the water, and as the steam must take up about 10 times its own weight of water in order to condense, it would consequently possess only just power sufficient to impart to that amount of water the requisite velocity, when that point would be reached, where the injector would no longer work with water of ordinary temperature. The author had referred to the dynamical theory of heat, and had said, that a sudden change in the sheaf took place, when there was an instantaneous conversion of heat into work, a vortex being found in the sheaf, producing this result. Mr. Siemens had been one of the earliest disciples of this new theory of heat ; and in the year 1853,* a paper by him was read at the Institution in which the caloric engines were passed in review by the light of that theory. Taking the case of a pressure of GO Ibs., the force repre- * Vide Minutes of Proceedings of the Institution of Civil Engineers, Vol. XII. p. 571, and p. 29, ante. 106 THE SCIENTIFIC PAPERS OF scnted by a jet of steam issuing out into the atmosphere was simply the product of the column in feet representing that pressure, multiplied by the weight of steam in Ibs. issuing in a given time. The column representing the pressure of steam of four atmo- spheres total pressure was, according to the table, 45,792 feet ; — that was, steam of a pressure of 60 Ibs. would be produced by a column of its own weight 45,792 feet high. Therefore, 45,792 foot-lbs. was the mechanical work due to 1 Ib. of that column of steam. Now the quantity of heat contained in 1 Ib. of steam was 1,150 units. These 1,150 units of heat produced in the injector 45,792 foot-lbs. of work, or for every unit of heat 45 792 — - = 39'8 foot-lbs. The full mechanical equivalent of a unit l,loO of heat was however = 772 foot-lbs., or units of force, and therefore 39 *8 the maximum useful effect of the injector did not exceed _^j,or / la about the twentieth part of the theoretical effect due to the heat in the steam. A good expansive steam-engine would give as much as one-sixth part of the full theoretical effect due to the heat expended, and supposing that there was 33 per cent, loss in an ordinary pump, it followed that water could be raised with an 33 expenditure of 6 + y^; = 8 times the theoretical expenditure of heat, instead of 20 times that quantity which the injector required. Consequently, the injector could only be advantageously applied, when the water was required to be both heated and raised ; and it could never compete with an engine and pump for simply rais- ing and propelling water. WILLIAM SIEMENS, F.R.S. 1 07 ON UNIFORM ROTATION. BY C. W. SIEMENS, F.R.S.,* Mem. Inst. C.E. AMONGST the means at our disposal for obtaining uniform rota- tion, there is none for which the same degree of accuracy can be claimed as that which distinguishes the vibrating pendulum, or the oscillating spring-wheel of the common watch ; yet there are many purposes, both in physical science and in the mechanical arts, for which smaller subdivisions of time than the period of one oscillation are matter of considerable importance, and which can only be measured by uniform rotation. CONICAL PENDULUM. — The apparatus by which continuous rotation of the greatest regularity has hitherto been obtained, is the conical pendulum, which was first applied by James "Watt to regulate the speed of his engines, and which has since received further development in the instrument known as the Chronometric Governor. On examining into the principle involved in the conical pen- dulum, it will be found that the time t of its rotation is dependent upon its length I, and on the angle a which it makes with its vertical axis of rotation, which dependence is expressed by the formula t = cj> *Jl cos a, the coefficient <£ being a function due to gravitation. The value of t being dependent upon a, it follows that " uniform rotation of a conical pendulum cannot be obtained except on condition that the angle of its rotation remains constant" WATT'S GOVERNOR. — In the case of Watt's centrifugal governor, the angle of rotation of the pendulum varies with every change in the relative condition of power and load on the engine, and the change of angle is, indeed, taken advantage of to close or open the steam-supply valve. In order to close the steam- (or throttle-) valve the angle of rotation has to be increased, which necessitates a corresponding increase of the engine's velocity ; on the other hand, an increase of the valve-orifice must be consequent on a reduction of the speed of the engine. Considering this dependence of the action of the instrument * Excerpt Philosophical Transactions of the Royal Society, 1866, pp. 657-670. 108 THE SCIENTIFIC PAPERS OF upon permanent change of speed of the engine, the name of " governor " seems inappropriate, the instrument being, in fact, only a " moderator " of the amount of fluctuation to which the engine would be subjected without its agency. The amount of these fluctuations depends, in a great measure, upon the mechanical construction of the instrument, which is, generally speaking, very objectionable, inasmuch as the pendulous arms are mostly sus- pended at points beside the common axis of rotation, giving rise to an increased variation of time for a given change of angle ; the reason being that the true pendulous length has to be measured from the point of intersection of the pendulums or rods with the axis of rotation, which point descends as the angle increases, causing the pendulous length to diminish at both extremities. A better result would be obtained if each pendulous rod were suspended from the point past the axis of rotation (as shown by dotted lines in Plate 19, Fig. 1), causing the two rods to cross in the line of the axis at a point which would rise with increase of angle, and render the true pendulous length approximately uniform between certain limits. The governor of Watt is, however, subject to another defect which does not admit of an easy rectification, and which consists in its want of power to operate on the steam-valve at the moment when the equilibrium between the power and load on the engine is disturbed. It will be seen that while the engine proceeds uniformly, gravitation and centrifugal force must be in equilibrium as regards the governor-balls, but at the moment when, for instance, a portion of the load on the engine is removed, steam-power will be set at liberty for accelerating the fly-wheel. This acceleration proceeds in accordance with the well-known gravitation laws until the increase of centrifugal force imparted to the governor-balls suffices to overcome the friction of the valve and its mechanical connexions, which are not inconsiderable. In the mean time the speed of the engine will have been increased to an extent con- siderably beyond what is required in order to maintain the valve in its new adjustment ; the action of the governor, when it does take place, will therefore be excessive, and a series of fluctuations in the speed of the engine must follow before the proper readjust- ment of its valve can be effected. CHRONOMETRIC GOVERNOR. — Impressed with these imperfections WILLIAM SIEHfENS, F.R.S. 109 in Watt's centrifugal governor, I proposed, twenty-three years ago, in connexion with my brother, Werner Siemens, a governor based also on the conical pendulum, which in this case was to be independent in its action of change in its angular rotation, and, moreover, was to be provided always with a store of power ready to overcome the resistance of the valve at the first moment when the balance between the power and load of the engine was dis- turbed. This instrument (the chronometric governor) has been applied with success in many cases where engines were required to work with great regularity under varying conditions of load ; it has also received an interesting application by the Astronomer Royal for regulating astronomical and chronographical instru- ments, proving the high degree of precision of which it is capable. The leading idea involved in this governor consisted in providing a conical pendulum in uniform rotation, and in establishing a differential motion between it and the wheel driven by the engine, which differential motion was made to act upon the source of power of the latter. If this idea could be carried out, it was evident that the engine, or machine to be governed, must suit its motion closely to that of the independent rotating pendulum, because the least retardation on its part must immediately result in an enlargement of the valve-orifice (it being understood that an increase of available power is always obtainable), and the least motion in advance of the pendulum must automatically reduce the source of power. This action would be effected instantly, notwith- standing a considerable resistance in the valve, because' the weight of the pendulum in rotation represents, in this case, a store of power, inasmuch as its angular velocity would have to be suddenly checked or increased as the case may be, unless the valve obeyed to the first appearance of a differential motion. In order to realize these conditions, it was necessary to maintain the conical pendulum in question at a uniform angle of rotation, notwithstanding the changes of driving- or sustaining-power which must necessarily arise through its action upon the regulating valve of the engine ; and this could only be accomplished by providing the means of destroying or absorbing any excess of driving-power beyond what was necessary to overcome the friction of the instrument, and which must tend otherwise to increase its angle of rotation. On the other hand, a surplus of driving-power had to be provided to 110 THE SCIENTIFIC PAPERS OF prevent an occasional collapse of the pendulum in opening the valve. The sustaining- or driving-power of the pendulum was obtained in taking advantage of the differential motion, a weight being attached to a horizontal lever upon the throttle-valve spindle, which, in exerting a pressure of the differential wheel against the two principal wheels, caused an impulse to be given to the one connected with the pendulum, whereas the third wheel was driven by the engine in the direction proper to raise the weight continually. The excess of driving-power imparted to the pendulum was destroyed by calling into action a friction between two solid substances at the moment when the angle of rotation had reached its intended maximum ; or a liquid resistance was intro- duced, such as a fan, rotating with the pendulum, being dipped into a bath of mercury or other liquid, at the moment when the extension of the pendulum was attained (see Plate 19, Fig. 2). The governors constructed on this principle are remarkable for their instantaneous action upon the supply-valve of the engine, when a sudden disturbance of the balance between load and power takes place ; and they possess also, to the fullest extent, the power of maintaining the regulated machine at the same speed, when the load reaches its maximum, as when it is at its minimum. In the hands of the Astronomer Royal the uniformity of motion obtained by the use of this governor approaches indeed that of an ordinary chronometer, yet it is not free from objections resulting from the delicate adjustment and frequent attention requisite to maintain it in good working condition. In its application to the regulating of physical apparatus it has, moreover, been found that the conical pendulum is apt to fall into elliptical rotation, whereby the sub- divisions of time below the half second become inaccurate. FOUCAULT'S GOVERNOR. — Monsieur Foucault, of Paris, has treated the same question in a different manner, substituting for the friction between solids, or of solids against fluids which we employed to fix the angle of rotation of the conical pendulum, the varying resistance of an air-propeller, according to the amount of area for the escape of air, which area he regulates by means of the angular elevation of his conical pendulum. The conical pendulum he employs is mounted in the manner of a Watt's governor of the best construction, which renders his apparatus portable, and therefore convenient for general purposes, while, on SSK WILLIAM SIEMENS, F.R.S. Ill the other hand, it appears to depend for its correct action upon the perfect condition of many mechanical details. Some months since an idea suggested itself to me which, while it furnishes the elements of a very general and complete solution of the problem under consideration, appears to possess also a separate scientific interest, which chiefly induces me to bring the subject before the Royal Society. LIQUID IN ROTATION. — If an open cylindrical glass vessel or tumbler containing some liquid be made to rotate upon its vertical axis, the liquid will be observed to rise from the centre towards the sides to a height depending on the angular velocity and the diameter of the vessel. As soon as the velocity has reached a certain limit the liquid will commence to overflow the upper edge of the vessel, being thrown from it in the form of a fluid sheet in a tangential direction. If the velocity remain constant from this moment, the overflow of the liquid will be observed to cease, although the liquid remaining in the vessel will continue to touch the extreme edge or brim. Supposing that the velocity of the vessel be now diminished, the liquid will be observed to sink, but will rise again immediately to its former position when the rotation returns to its previous limit of angular velocity. This velocity is the result of the balance of two forces acting on the liquid particles, namely, gravity and centrifugal force. It is a well-known fact that the curvilinear surface produced by a liquid in rotation is that of a paraboloid, the parameter of which is expressed by -^, and the curve itself therefore by the formula x signifying vertical distance from the apex, y the corresponding horizontal distance from the axis of rotation, w the angular velocity of rotation, and g acceleration by gravity in one second. In this formula there is no factor denoting the density of the liquid, which proves that the point to which the liquid is raised by a given angular velocity is independent of the specific gravity of the liquid employed. By substituting for y the radius r of the rotating cup at the brim, and for x the height h of the brim above the lowest level 112 THE SCIENTIFIC PAPERS OF of the liquid, we may write the foregoing general formula as follows : — rzw~ A-^-, ....... (II.) and (III.) two convenient formulae for determining the height to which liquid will rise when the diameter of the rotating vessel and its angular velocity are given, or for determining the angular velocity due to a given height and diameter, it being understood that the values of g, r, and h, must be expressed in the same unit of length. If it is desired to determine the number of revolutions per w second n, instead of the angular velocity w, we may put n = ^- , and Z7T in putting this value for w ( = 2nri) into the last formula, we have w = lSr ...... (IV° These formulas are applicable to vessels of every possible exter- nal form rotating upon their vertical axis, and to every possible liquid, but they are based upon the supposition that the liquid is raised by rotation to the upper edge or brim of the vessel, a condition which it may appear at first sight difficult to realize for practical purposes. If the production of uniform rotation be the object in view, it is necessary that the liquid in the rotating vessel should always be at the point of overflow, although the driving-power might vary considerably, and that all surplus driving-power should be absorbed by other work than that of accelerating the rotating vessel, also that the stock of liquid within the vessel should never diminish. I hope to prove by the following demonstration that these various conditions can be fulfilled by suitable mechanical arrangements resulting in the construction of a simple and efficient instrument, which is represented by Plate 20, Fig. 1, and which has sur- vived the ordeal of experimental proof. LIQUID PYROMETER. — The rotating vessel consists, in this case, of a cup C open both at the top and bottom, but widest at the top, the sides being made to close in towards the bottom in a parabolic curve analogous to that formed by the liquid in rotation. SIR WILLIAM SIEMENS, l-.R.S. I 1 3 This cup contains upon its inner surface three or four radial ribs which unite in a central boss, by which the cup is supported upon the spindle S. This support is not an absolute one, but the spindle is armed with a screw-thread of rapidly ascending path, into which the screw-threads upon the inner surface of the boss are made to fit ; a fixed connection between the driving-spindle and the cup C is established by means of a spiral spring E, one end of which is fastened to the projecting end of the spindle S, and the other to the cup. Before this spring is fixed, it is drawn out longitudinally to such an extent as to balance the weight of the cup, which latter may therefore be said to float upon the screw-threads without exercising any pressure upon the same. The upper support of the spindle S is a boss projecting from the bottom of a cylindrical vessel B of glass sides and glass-domed top, which completely enclose the cup C, while it renders its action visible : this outer vessel is filled with liquid to such a height as to submerge the lower edge of the cup. Rotation of the liquid in the outer vessel is prevented by radial ribs upon its bottom surface ; and upon the external surface of the rotating cup C two concentric projections are provided, one at the upper edge, and the second near the surface of the outer liquid, for the purpose of throwing off some liquid which would otherwise be apt to adhere to the external surface of the cup, in defiance of centrifugal force, and interfere slightly with its proper action. Rotation being imparted to the shaft S and the cup C by clock- work or from any other source, the liquid at the bottom of the cup will be acted upon by centrifugal force and rise upon its inner sides, while additional liquid will enter from without and maintain the apex of the liquid curve nearly on a level with the surrounding lake. At the moment when the liquid in rotation touches the upper edge of the cup, the speed should be such as is determined by the formula n = ~-^-, in which h may be taken £TlT for the height of the brim of the cup above the lake surface ; but considering that the power necessary to maintain the cup at its velocity, after the liquid has been raised to its upper edge, is exceedingly small, because no fresh material has to be put into motion, it would be practically impossible to prevent further acceleration. In order to make sure that the liquid will not fall VOL. i. i 114 THE SCIENTIFIC PAPERS OF below the brim of the rotating cup, an excess of driving-power must be applied, and that excess must be disposed of otherwise than in producing further acceleration of the cup. This is accom- plished by means of a continual overflow of a thin sheet of liquid, which is projected against the sides of the outer vessel and falls back into the lake at the bottom, whence a similar quantity of liquid penetrates into the cup, to be also raised by its rotation and projected over its edge. The power absorbed in raising and projecting the liquid must be strictly proportionate to the quantity of liquid so acted on in a given time, or to the thickness of overflow, provided the condi- tion of uniform velocity be realized ; but the velocity of the cup depends upon the height to which the liquid has to be raised, and must therefore be increased in order to raise the liquid column above the brim of the cup. The. necessary increase of velocity to produce such an overflow is not great, considering that the height of the liquid column increases in the square ratio of the velocity, and may be neglected in all cases where only approximate results are required, or where variations in the driving-power are com- paratively small ; but no high degree of accuracy could have been claimed for this instrument unless the following compensation action had suggested itself : — AUTOMATIC DIP OF CUP. — We have assumed hitherto a rigid connexion between the cup and its driving-spindle, and unless the cup does overflow, we are, indeed, justified in this assumption, the spring E being too rigid to yield to the resistance of the cup in motion when no work is performed. With an increase of power the resistance of the cup also increases, and an overflow of liquid proportionate to the power is produced ; the connecting spring E must yield, at the same time, proportionately to the torsional resistance thus created, and in the same ratio the cup will descend upon the helical surface which serves for its guide. While, there- fore, on the one hand, the h of our formula increases with the overflow, it is diminished, in the same ratio, by the descent of the cup, both depending directly upon the driving-power. In so ad- justing the stiffness and length of the spring that the one action equals the other for any given increase of power, it must equal it also for other amounts of increase within reasonable limits, and strictly uniform rotation must le the result. The S7K WILLIAM SIEMENS, F.R.S. 115 " reasonable limits " to this automatic adjustment are imposed by the restricted orifice through \vhich the liquid has to penetrate into the cup, and also by the range of action of the spring, for which the law of Mariotte is applicable. Experiments, to be hereafter described, have shown that the driving-power may be varied between wide limits without producing any sensible varia- tion of speed. The final adjustment of the instrument to the normal velocity required is, moreover, easily effected by raising or lowering the cup while it is running, for which purpose the lower end of the upright spindle S is supported in the axis of an adjusting screw E, as will be seen by inspection of Plate 20, Fig. 1. RANGE OF POWER INCREASED. — The range of power through which uniform rotation can be obtained, may be further increased by an arrangement which is represented in Plate 20, Fig. 2, and Plate 21, Fig. 6, and which consists in arresting the liquid projected over the edge of the cup by a belt of fixed vanes M, whence it drops through the zone of rotating radial vanes L, which again impart tangential motion to it at the expense of the superfluous driving- power of the cup of which they form part. It is hardly necessary to add that these fixed and rotating vanes only increase the range of power of tJie instrument, ivitfwut in any way affecting its rate of rotation, and that a second set of fixed and rotating vanes might be added with the same effect as the first. Although the rotating cup represented in Plate 20, Fig. 2, and Plate 21, Fig. G, is not pro- vided with the automatic dip, it is equally evident that the fixed and moveable vanes do not preclude that arrangement, which is only dispensed with in such cases where great uniformity of motion is not required. An interesting application of such a " Liquid Gyrometer," as this instrument may appropriately be called, would be that of obtaining synchronous motion at different places connected by a telegraphic wire, for philosophical or telegraphic purposes ; but in order to test its fitness for such purposes, I have constructed a clock of which it constitutes the regulating principle, the moving power being obtained by electro-magnetism. CLOCK REGULATED BY LIQUID IN ROTATION. — This clock is represented by Plate 22, Figs. 7 and 8, and consists of three principal parts : — i 2 Il6 THE SCIENTIFIC PAPERS OF 1. The pedestal containing a battery of two " Marie Davy's elements " suitably arranged. 2. The body of the clock, with sides formed of plate glass, con- taining an electro-magnet, by which rotatory motion is imparted to an iron bar or keeper fixed upon the vertical main axis which passes into 3. the regulating chamber, consisting of a close cylindrical glass vessel with domed glass top containing the rotating cup and a certain quantity of paraffin oil, which fluid is particularly appli- cable on account of its perfect fluidity and non-affinity for the materials composing the regulator. The regulating cup is in this instance formed of vulcanite, and is suspended from the top of the vertical axis by means of a spiral spring, which, being fixed at both ends, not only supports the weight of the cup but acts also as a torsional spring, enabling the cup to descend upon its helical central guide whenever an increase of driving-power calls into existence its equivalent of torsional resistance. The rings of stationary and rotating vanes are dispensed with in this instance, because no great variations in the driving-power are contemplated. The electro-magnet acts by attraction of the armature during a small portion of its rotation, and one contact only is required, which is so arranged that no destruction of the metallic surfaces can arise through the discharge of extra-current sparks, which latter are received by an elastic point of platinum slightly in advance of the proper contact surface and moved by the same eccentric. By this simple arrangement the usual diffi- culty attending dry contacts is avoided, and a continued action of the instrument ensured. A train of reducing-wheels communi- cates the motion of the cup-spindle to hands upon the face of the clock, which record hours and minutes in the usual manner. The diameter of the rotating cup being = 0'040 metre, and the height of its edge over the surface of the liquid = 0-034 metre, the number n of its rotations per second in accordance with our formula metre x -038 metre=6.9 reyolutions gecon(L Experiment gave, on the contrary, a speed of 7*5 revolutions .s/A' WILLIAM SIEMENS, F.K.S. Ii; per second, or *G revolution per second more than was indicated by t lift »ry, a result which seemed to stamp the action of the instru- ment with uncertainty, when it was recollected that no allowance had been made for the aperture at the bottom of the cup, leaving a portion of the rotating liquid without an external support. CORRECTION FOR LOWER ORIFICE OF Cur. — If we assume, for instance, that the sides of the cup were cylindrical and merely descended below the surface of the liquid without closing in at the bottom, we should find that by rotation of this cylinder, supposing the inner surface to be rough or armed with radial projections, the liquid would rise on the circumference above the external level of surface, but would also form a depression or vortex in the centre of rotation. The surface of the rotating liquid would be that pro- duced by the rotation of a vertical parabola, as represented in the diagram (Plate 19, Fig. 3). In order to maintain the hydrostatic equilibrium between the rotating column with the external liquid, it is necessary that its mean height of column must remain the same, or that the plane of external liquid level must divide the solid figure comprised between the cylinder and the curve of rotation into equal parts. In order to realise these conditions experimentally, it would be necessary to provide the lower portion of the rotating cylinder with an easy fitting and balanced piston> without which circular currents would be produced within the rotating liquid (descending by force of gravity at the sides, and rising again in the centre) and mar the result. The body comprised between a paraboloid of the height ti and a cylinder is, however, divided equally by a horizontal plane cutting it at the distance of — - -— from the edge, or at ti — -j- = -293# from \['£ »J i the apex. The form of the curve depends upon the angular velocity alone, and would remain the same if the upper diameter of the tube were to be increased, only the curve would in that case have to be continued until it met the sides (as shown by dotted lines), and to the extent of these prolongations the liquid would be raised higher above the external level without producing a corresponding depression in the centre of rotation. It follows that the aperture at the bottom of the rotating cup causes a vortex or depression of the apex of the curve of rotation below the external liquid to the extent of '293 part of the height Il8 THE SCIENTIFIC PAPERS OF due to its own diameter, and to the correct number of rotations ri per second. it is 2m and also n'=^2ffh' 2pir if p is the radius of lower aperture of cup ; therefore 2rir Or *' = V--298p>; and in substituting this value for h' into the first formula, we have n = 2rir or for our corrected formula to determine the velocity of cup with continuous overflow). In applying this formula to the clock, taking for p its value of 8 millimetres and the other values also in millimetres in order to avoid fractions, we find 19600 *881+ 400 -16-05) = 7*4 revolutions per second, or '1 revolution per second less than the actual speed. This remaining excess of the actual over the calculated velocity of the cup is rather more than what may be fairly attributed to error of measurements, and appears to be due to adhesion of a film of liquid (which may be estimated at nearly '25 millimetre thickness) to the inner sides and edge of the cup, whereby its effectual dimen- sions are proportionately reduced. For a uniform speed this error must be a constant quantity, which cannot affect the working of the instrument injuriously, so long as the other conditions are such as to produce uniform rotation. The discrepancy is diminished by increasing the dimensions of the cup, and its amount is such WILL/AM SIEMENS, F.R.S. 119 that the compensation is effected, under all circumstances, by one or two turns of the regulating screw supporting the vertical spindle. \Ylien the regulation of the cup is once effected, it continues to rotate at a remarkably uniform rate. Change of temperature affects the density of the liquid considerably, but does not in- fluence the rate of the cup otherwise than inasmuch as it affects the level in the cup-chamber, which will rise with increase of temperature proportionately to the depth of liquid it contains, and which is inconsiderable. The lineal dimensions of the cup, and the length of the suspending spring, will also increase, all tending to lower the rate with increase of temperature ; but, on the other hand, the length of the upright cup-spindle increases with increase of temperature, and in regulating the length and com- position of that spindle properly, entire compensation for change of temperature is effected. The cup-chamber being entirely closed against the atmosphere, no fault can arise through evaporation or dispersion of the liquid within moderate periods of time. In the case of the clock under consideration, no compensation for change of temperature was provided, nor is the cup entirely balanced by the spring, yet its rate is as uniform as that of the common clock with which it has been compared ; but in order to test the regulating-power of the instrument, the driving-power was varied by the introduction of artificial resistances into the galvanic circuit, when the following results were observed : — Time of Common Clock, in Seconds. Mercury units of Resistance of Clock and Battery. Units of Resistance put into Circuit. Relative Value of Driving- power. Time of Liquid Gyro- meter Clock, in Seconds. Variations in Time produced, in Seconds. 720 110 0 100 736 16 slow 720 110 10 92 734 14 „ 720 110 20 85 734 14 „ 720 110 30 78 733 13 „ 720 110 40 73 732 12 „ 720 110 60 69 731 11 „ 720 110 60 64 729 9 „ 720 110 70 61 726 6 ,, 720 110 80 58 723 3 „ 720 110 90 55 720 correct 720 110 100 52 723 3 fast 720 110 110 50 726 6 „ 720 110 120 48 725 6 „ 720 110 130 46 724 4 „ 720 110 140 44 722 2 „ 720 110 150 42 729 9 slow when the overflow had ceased. 120 THE SCIENTIFIC PAPERS OF This result shows that the spring employed was decidedly too weak, producing a decrease, of speed with increase of power. A more careful adjustment of the spring would improve these results, which suffice, however, to prove the capabilities of the instrument. It appears at first sight as though the friction of the cup upon the threads of the screw must interfere with its automatic adjust- ment ; but this is practically not the case, owing to the circumstance that small fluctuations in the resistance continually occur, causing torsional oscillations of the cup, the mean of which must be its true position notwithstanding friction, which friction moreover is reduced to a minimum, owing to the suspension of the weight by the spring. Another interesting quality of the gyrometric cup is its com- parative indifference to a vertical position ; it may, indeed, be tipped very considerably without interfering with the uniform overflow all round, and the time of its rotations is diminished only in the ratio of the square roots of the vertical mean heights, or it is ri : n = JOT: >Jh cos /3, or for a tipping angle /3 = 3°, ri : n = 1 : 1*0007, showing that no particular care is requisite to place the instrument upon a horizontal foundation. G-YHOMETRIC GOVERNOR. — The most useful practical applica- tion of this instrument is that of regulating the power and velocity of steam-engines. A cup of very large dimensions, provided with several belts of check-vanes and with the automatic dip arrange- ment, might be conceived which, in being connected by gearing with the main shaft of an engine, would limit its velocity by absorbing directly all its surplus power. This surplus power would appear in the cup-chamber in the form of molecular motion or heat, and would have to be got rid of by the application of cooling agents, if the natural dispersion of heat by radiation would no longer suffice to keep down the temperature. This would, however, be a wasteful proceeding, and it becomes necessary to operate, not upon the power produced, but rather upon the source of power, by rendering it always equal to the accidental resistance or load in order to maintain uniform velocity. The arrangement adapted for this purpose is represented by Plate 20, Fig. 2, and Plate 21, Figs. 3, 4, 5 and 6. S is the main shaft of the engine, which imparts motion to the WILLIAM SIEMENS, F.R.S. 121 upright spindle H carrying an inverted wheel E. The axis A of the regulating cup, being concentric with the spindle H, carries a pinion F, and both the wheel and the pinion gear into two inter- mediate or planet-wheels G and G', which latter are loose upon studs and are suspended from a rocking-frame I, the latter being free to turn upon its central support. The rocking-frame I is connected by a rod R to a bell-crank lever 0, which is fastened upon the spindle of the steam-regulating or throttle-valve V ; but the horizontal arm of the lever 0 carries a weight P which, being acted upon by gravity, tends to open the valve and at the same time to force the rocking-frame I, with its planet-wheels G and G', round the vertical axis. This pressure is resisted, on the one hand, by the teeth of the pinion F, which can only yield in the ratio imposed by the rotating cup C, and on the other hand, by the teeth of the inverted wheel E, which latter, being driven round by the engine in the direction contrary to the effort pro- duced by the weight P, causes the latter to be continually raised. If the engine should succeed in raising the weight P, say 100 millims., while the regulating cup yields also to the extent of 100 millims., then the lever 0, and with it the regulating valve V, will retain their relative position ; but if the engine should raise it, say 95 or 105 millims., while the cup yields 100 millims., then the valve will be either opened or closed by 5 millims., and the engine will be urged or checked, as the case may be, to such an extent as to make its revolutions coincide again absolutely with those of the regulating cup. The driving-power of the cup is limited by the weight B, and may be considered as a constant regulated quantity (although it is derived indirectly from the engine) ; but whenever the valve has to be opened or closed, a resistance arises which goes either in diminution of or in addition to the weight P, and the power of the cup must be such that its speed remains sufficiently uniform under the influence of these occasional variations. By means of the automatic dip arrangement it would not be difficult to obtain perfect uniformity, notwithstanding these irregu- larities in the driving power ; but in the case of steam-engine governors this arrangement is dispensed with for the sake of a more immediate action upon the valve at the moment when a differential velocity arises. Supposing that the greatest amount of 122 THE SCIENTIFIC PAPERS OF occasional variation of speed is to be 1 per cent., and that the dimensions of the cup are as follows, Diameter at upper rim . . . = 200 millims. Diameter of rim above the liquid . . = 200 millims. Diameter of orifice at bottom of cup . = 90 millims. we find the available power of the instrument in the following manner : — The normal speed of a cup of these dimensions is, according to our formula. = 3-31 revolutions per second. The height to which the liquid is raised by rotation increases in the square ratio of the speed of rotation, the increase of height due to 1 per cent, increase of speed would therefore result from the following proportion, 100 v : 101 v = ,Jh : JR, or the height due to the increased speed, ti = 204 millims., that is to say, the liquid would be raised 4 millims. above the brim of the cup, which, being an unbalanced column, will produce an upward flow of the liquid in the cup, as expressed by the well-known formula, v = ftgh ; or h being in this case = 4 millims., we have v = *280 metre flow per second, which, if multiplied by the least sectional area at the entrance into the cup = "0057 square metre, gives the quantity of liquid '280 metre x '0057 square metre = '0016 cubic metre, or r.6 litre of liquid raised 204 millims. high and projected with a velocity of \%^ x 3*31 x 27ir = 2*1 metres per second over the brim of the cup, to be stopped by the stationary wings and once more accelerated by the rotating wings, which, being one-fifth more in diameter than the cup itself, impart to the liquid a velocity of f x 2'1 = 2'5 metres per second. These accele- vn- rations represent a power which, according to the formula h =-x-, *9 is equal to the same liquid being lifted for v = 2*1 metres . to '225 metre height, . and for v = 2'5 . . to "320 metre height. In the cup it was lifted to '200 metre height, making a total lift . to '745 metre height. WILLIAM SIEMENS, F.R.S. 123 If the liquid employed is water, the 1'6 Hire represents 1'6 kilogram., and the resistance produced by 1 per cent, increase of ity is 1'G x '745 = l"2 kilogrammetres per second, which is equivalent to forcing a valve rod or lever through one decimetre space in fen seconds against a resistance of 120 kilograms. This force exceeds by far what is usually required of a governor, and fits the new instrument for the accomplishment of objects which could hitherto not be attempted, such for instance as regu- lating the power of engines by the link motion or other variable expansion gear (whereby a considerable saving of fuel may be effected), or moving the gate of a water-wheel. The most striking feature of this governor is, however, the rapidity with which a readjustment between power and load of an engine is effected ; experiment has proved that two-thirds of the Mai load upon an engine may be suddenly thrown off without pro- ducing any visible change in its rotation. It must be borne in mind that the variation of 1 per cent., which was assumed in calculating the power of the instrument, applies only to the short period of ten seconds, when the readjustment of the valve is effected, after which the cup and, with it, the engine returns to its normal rate of rota- tion ; but an increase or decrease of speed of 1 per cent, during ten seconds is so small a total amount that it is not perceptible to the eye, and may be regarded as non-existing for practical purposes. A uniform velocity of engines, such as is secured by this instrument, is of considerable practical importance in spinning, grinding corn, and other manufacturing operations, because it not only prevents breakages and irregularities in the quality of the work produced, but it enables manufacturers to attain to the maximum speed at which their work can be produced. It has been shown that the rotating cup is not sensitive to tipping, a circumstance rendering the gyrometric governor also applicable to marine engines, which are much in need of a means for maintaining a uniform speed, particularly where the screw propeller is used, which, in being raised by waves above the water, allows the engine to fly off at a dangerous speed. The gyrometric cup appears therefore to be equally applicable for maintaining powerful machinery at a nearly uniform velocity and for obtaining the higher uniformity of rotation requisite for philosophical and telegraphic instruments. 124 THE SCIENTIFIC PAPERS OF In the discussion of the Paper entitled "DESCRIPTION OF THE STEAM STEERING ENGINE IN THE 'GREAT EASTERN' STEAMSHIP," By Mr. J. MCFARLANE GRAY, MR. 0. "W. SIEMENS * observed that the present paper was the first they had had upon a subject which he thought was a very important one ; for to see a large number of men at the helm of a big ship, trying to bear her round, certainly showed great imper- fection in the present mechanical arrangements for steering. The apparatus now described as applied to the steering of the " Great Eastern " gave evidence of a great deal of thought ; and the details of the arrangement for starting the steering engine, and making it obey signals given from a distant part of the ship, were highly ingenious, and the results of the working in practice showed, that all the requirements of the case had been duly con- sidered beforehand. He inquired whether any difficulty had ever been experienced in starting the engine after it had been standing for a time, owing to accumulation of water in the cylinders ; and whether a difficulty did not arise from the same cause whenever the rudder had to be held by the engine for any length of time in the same position ; and he asked what provision was made for getting rid of water in the steam cylinders. Another question that had occurred to him, though somewhat beyond the immediate subject of the paper, was whether the steering engine during the time it was standing might not be made serviceable for aiding in the propulsion of the ship by means of a Ruthven re-action propeller, discharging a jet of water from the stern in the opposite direction to the ship's motion. He did not advocate such a plan of propulsion in substitution for the screw and paddles ; but he thought it might be advantageously applied in conjunction with these, for utilizing a moderate auxiliary power from a separate engine like that employed for the steering- * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers, 1867, pp. 279-281. WILLIAM SIEMENS, f.K.S. 125 r, which was not required to be constantly at work for steering. The stream of water projected backwards from the stern might either be discharged in a line parallel to the keel of the vessel, or by means of deflectors it might readily be diverted to either side for changing the ship's course. Such an arrangement, he thought, would have several advantages over any plan of steering by a rudder, because the action of a rudder depended upon the onward motion of the ship, and without onward motion a rudder could produce no effect ; whereas by a jet of water issuing laterally from the stern the ship could be steered round while she was not moving forwards or moving very slowly, which in some circumstances was an important consideration. In managing a ship for the purpose of picking up submarine telegraph cables, he had himself found very great difficulty in turning the ship round by means of the rudder, while obliged to remain stationary upon the same spot for the performance of the necessary operations. Moreover, if such a plan of steering by a water jet were thoroughly carried out, the rudder, which was the most vulnerable portion of a ship, might be dispensed with. In the discussion of the Paper "ON LIQUID FUEL," by BENJAMIN H. PAUL, THE Chairman * (Mr. C. "W. SIEMENS) said that the discussion had elicited quite a conflict of opinions, while those held on each side were apparently based on independent facts ; but he believed it was not impossible to reconcile many of the statements which were apparently contradictory, by properly discriminating between theoretical and practical results. These two ought to be kept distinctly apart. The practical result would ultimately approach to the theoretical, if all the conditions of the various operations were perfect, but it could never quite attain it ; and, unfor- tunately, in the consumption of solid fuel, the practical results did * Etccrpt Journal of the Society of Arts, Vol. XVI. 1867-1868, pp. 409-410. 126 THE SCIENTIFIC PAPERS OF not nearly approximate to the theoretical ones. He believed that some years hence any engineer who looked at the furnace of one of our present marine boilers would be ashamed of it. The mode of throwing the fuel on a kind of volcano, giving off a large proportion of valuable substance in the form of thick smoke, was very objectionable. As far as he could follow the calculations given, he thought Dr. Paul had rather overstated than otherwise the theoretical evaporating power of liquid fuel as compared with coal. He gave the evaporating power of hydrogen at 64 Ibs., which agreed with the statement laid before the United Service Institu- tion by Professor Macquorn Rankine, but there was a correction to be made in that. Professor Rankine gave the evaporating power of hydrogen at 64*2, and of carbon at 16 '05, but he con- sidered, in this calculation, the hydrogen as existing in a gaseous state, and the carbon in that of a solid. He made an allowance for the chemical affinity between the hydrogen and carbon when in the form of marsh gas, but he did not allow for the hydro- carbon as being in a liquid condition, in which state it was when in the form of oil. There must be a correction made on that account, though he could not precisely say what it should be. There was another correction to be made with regard to the latent heat of the steam resulting from the combustion of hydrogen, by which, no doubt, the results would be very sensibly modified. However, if they went from theory to practice, they had certainly great allowances to make in favour of the oil. For instance, coal contained not only alkaline matters, but also a great deal of water, which oil did not ; then, a certain portion of oxygen was already absorbed by the coal, and there was a great waste by smoke. Further, it was impossible, whilst burning fuel upon a grate, to obtain that regularity of proportion between the air and the material consumed, which was necessary to produce an economical result. All these points were arguments in favour of the liquid fuel. He must say, that he quite agreed with several of the speakers, that volatile liquid fuel was totally inapplicable, and would be one of the most dangerous things imaginable on board ship ; they must, therefore, consider the question as confined to the use of heavy oils, which might, no doubt, be employed with advantage. They admitted of better stowage than coal, occupied much less bulk, and would save on board ship a great deal of Sffi WILLIAM SIEMENS, F.R.S. 127 labour, which meant space, of course, as less men would be required. Then there was another great advantage — there was no smoke. This, in the case of men-of-war, was very important, because a fleet of steam vessels at present could be seen while they were many miles below the horizon. For the mercantile marine, however, the question would reduce itself to one of price ; and if the oil were £5 a ton, and the coal £1, no doubt the advantage would be in favour of the latter. Captain Selwyn said he was now using oil at Id. a gallon, or not quite £1 Is. a ton. The Chairman said, that so long as the oil could be obtained at anything like the price now mentioned, no doubt it would be a most valuable fuel ; but the question was, would the price remain so favourable to the consumer if the demand should increase ? Of that he must say he had considerable doubt. If they had to distil the oil specially for the purpose from coal it must be expensive, and they must therefore fall back upon the natural supplies, or those which were incidental to other manufactures, which supplies must necessarily be limited. As to the use of water for burning, he was quite sure that no one acquainted with the subject would attribute any special evaporating power to water itself. . Water might be usefully applied sometimes in conveying heat from one place to another, as, for instance, the introduction of a jet of steam under a grate on which anthracite coal was burning pro- duced a gaseous fuel, the heat from which might be readily con- veyed to a considerable distance, but as to getting heat out of water it was absolutely impossible. He would conclude by moving a vote of thanks to Dr. Paul, to which he was sure they would feel he was fully entitled for his able and carefully written paper. 128 THE SCIENTIFIC PAPERS OF In the discussion of the Papers "ON MACHINES EMPLOYED IN WORKING AND BREAKING DOWN COAL, so AS TO AVOID THE USE OF GUNPOWDEE," by SAMUEL PAEKEE BIDDEE, Jun. Assoc. Inst. C.E. ; and "ON COAL GETTING MACHINERY, AS A SUBSTITUTE FOE THE USE OF GUNPOWDEE," by CHAELES JOHN CHUBB, ME. C. W. SIEMENS*" remarked that it was of the greatest interest to all that coal should not only be got economically, but without involving human suffering. Although it had been as- serted that the casualties caused by the explosion of powder were not so numerous as might have been supposed, nevertheless it was acknowledged that there was a serious loss of life every year. Independently, however, of that, there was the question of annoy- ance and injury to health that might be produced by noxious vapours arising from the explosion of powder in confined spaces. Moreover, it had been shown that coal could be got more economically by wedging than by blasting. The quantity of coal released by wedge action must be greater than that released by explosions, inasmuch as powder threw out the cone of least resistance, whereas a wedge would exert its power upon a larger range of coal. The question of undercutting the coal was no doubt important. He had been endeavouring to calculate what force would be expended in each case, but he had not been able to obtain a satisfactory result. If the coal was holed, or undercut, a disc of it had to be dealt with, and with the wedge the line of cleavage would be contained in that disc. He expected that the force expended would increase with the depth at which the force was applied ; so that if the machine was inserted into a hole 4 feet deep, it would expend four times the force that it would if the machine was put in only 2 feet deep. But the question became much involved if the coal was to be torn out of the face, because * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Vol. XXVIII. Session 1868-1869, pp. 141-142. S/R WILLIAM SIEMENS, F.R.S. 129 then the top and bottom rocks formed an element which he thought no calculation could reach. If the working was carried out in a mass of coal of infinite extent, then one might be disposed to consider the resistance to the circumference of the semicircular or shallow cylinder and the sphere which would have to be separated if the force were applied in a mass ; but inasmuch as the layer was confined between sides of rock, and that rock was pressed by a superincumbent weight of untold amount, the question was incapable of solution. On general grounds he believed it would be impossible for the Institution to arrive at any definite conclusion with regard to the best machine. The machines of Mr. Chubb and of Mr. Jones were similar in principle, and were both no doubt powerful though limited in range of expansion ; but, while such limited range was sufficient to separate the coal, he believed that the largest quantity of coal could be got with a minimum expenditure of force, because all the force of that short range was directly applied. It was, how- ever, necessary that the coal should be sufficiently hard to allow of a perfectly cylindrical hole being drilled or bored, and that it should not yield more than the length of the stroke of the pistons. Mr. Bidder's machine, on the other hand, was capable of greater range, and by it greater force could be brought to bear upon one point. It seemed also to have the advantage that a smaller hole sufficed for its action ; but, on the other hand, that hole must be deeper than was necessary in the case of Mr. Chubb's machine. He subscribed to the objection urged by Mr. Mallet, that a pro- portion, not easily ascertained, of the force expended must be lost by pressing the front of the wedge against the mass of dead coal. The wedges pressed not against the coal that was going to be loosened, but against the dead mass of coal further on ; and it was a question, which would puzzle a mathematician to determine, what proportion of force was expended in compressing the coal, and what proportion in cracking it away from its position. With Mr. Bidder's machine the loss of a portion of the pressure by the compression of the coal suggested to Mr. Siemens a modification which was this : — where coal was naturally tender, and where it was advisable to work it in comparatively thin layers, there might be applied a machine composed of three strong steel bars, arranged like a pair of scissors, with a hydraulic ram driving at the ends VOL. i. K 130 THE SCIENTIFIC PAPERS OP into gudgeons, so as to press out the ends of the scissors ; the ends of the bars being provided with little surface-plates to distribute the pressure over a certain extent of surface. Such a machine, in coal sufficiently tender, would work rapidly, because with one piston in operation a range of at least 9 inches could be obtained, and the fissure in that case would be in aid of the separation of the mass. In the discussion of the Paper " ON THE PROGRESS OF LIQUID FUEL," * By Captain J. H. SELWYX, MR. CHARLES W. SIEMENS said, as the Chairman has called upon me, I may say I go so far with the author of the paper, in the able manner in which he has put it forward, that in burning a fuel, a hydro-carbon, such as oil is, we may expect very superior results to those which we obtain from evaporating water by carbon or ordinary coal. No doubt, the calculation which Captain Selwyn has put before us is the correct one, according to the best facts with which we are acquainted. Only I would observe that if the 6'4G per cent, of non-combustible matter in the oil is oxygen there should be a tare allowed on account of it. Captain Selwyn. I think I gave that. Mr. Siemens. It appeared to me that Captain Selwyn did not make any distinction between oxygen and mere foreign matter. Captain Selwyn. I took both cases and gave you the result of both cases. Mr. Siemens. Well, in the case of oxygen, of course combus- tion takes place without generation of heat, inasmuch as the fixed oxygen in combining with fixed carbon produces a gaseous com- pound, carbonic acid, without generating heat at all. Therefore, for the equivalent of the oxygen, carbon ought to be taken off the result. It may be asked, why should oil give such a superior result * Excerpt Transactions of the Institute of Naval Architects, Vol. X. 1869, p. 37. .S7A' WILLIAM SIEMENS, F.R.S. 131 to coal, which, if you analyze it, contains very often not more than <; |> r cent, of foreign matter. I think an explanation maybe attempted in this way, that in burning coal we feed the furnace in an exceedingly irregular manner, charging the grate at one time with an excess of hydro-carbon, which flies off" and finds an in- sufficient amount of oxygen in the atmospheric air that enters the Lrnu<- to burn it ; and at other times the air that rushes through the grate has not time to take up its equivalent of carbon to pro- duce carbonic acid. The result is, that in examining the products of combustion of an ordinary furnace, we find as much as 25 or 30 per cent, of pure oxygen on one hand, and we find a consider- able amount of unconsumed carbonaceous matter going into the chimney along with it. This must be attributed not only to the unequal feeding of the coal into the grate, but it must also be attributed to the cooling effect exercised by the boiler, in checking combustion before the chemical action is completed. The first consideration in constructing a suitable grate ought to be to main- tain the. temperature of the flame for a sufficient length of time to complete the chemical action between the oxygen and car- bonaceous matter. That, no doubt, can be obtained in a much more perfect manner in dealing with a liquid fuel like oil. This liquid in itself would be rather difficult to deal with, inasmuch as the surface it presents in the liquid state to the oxygen of the atmosphere would be very limited ; but in blowing in it, as Captain Selwyn does, by a jet, you get an extreme subdivision of the oil, and in consequence you may obtain a perfect combustion. From the results brought before us by Captain Selwyn that seems to be the case ; we get an extremely perfect combustion, and, therefore, we get an extremely great duty performed. The practical question then arises, what are the sources of supply of this oil ? I do not know whether the author of the paper has gone into that point, but it is a question of very great practical importance. As long as we have liquid fuel, there can be no doubt that, weight for weight, it is superior to solid fuel. These heavy oils are free from the great objections that apply to light hydro-carbons, on account of their volatile qualities. But the question with me is, whether we can obtain such a supply of heavy oils at a moderate cost as will justify their employment upon a large scale ; for instance, will justify their application to our marine boilers. K 2 132 THE SCIENTIFIC PAPERS OP In the discussion of the Paper "ON RECENT IMPROVEMENTS IN REGENERATIVE HOT BLAST STOVES FOR BLAST FURNACES," By EDWARD ALFRED COWPER, M. Inst. C.E., MR. C. W. SIEMENS* said, the apparatus described by Mr. Cowper for heating the blast differed from the ordinary hot blast stove in this essential respect, — that the same surface of refractory material that absorbed the heat from the products of combustion served also to impart heat to the incoming blast. It was neces- sary, under these circumstances, that there should be two stoves, or air-tight receivers, filled with the refractory materials : the one to give off its heat to the incoming blast on its way to the furnace, and the other to be heated up for continuing the operation when the heat of the first-named stove was exhausted, valves being pro- vided for reversing the currents from time to time, as described in the paper. By these means the same surface of refractory materials was made to take up the heat from the burning gas and to impart it to the blast ; and as a consequence it followed, that the degree of heat that might be imparted to the blast was not limited by the point of safety of the iron tubes composing the ordinary stoves, but was limited only by the point of fusion of the refractory material's composing the regenerator of the new stoves. For heating blast to a moderate degree only, this stove possessed some advantages over the ordinary tube-stove, as the use of re- generators was always attended with a saving of fuel : but when- ever a high degree of heat was desired exceeding 1,000° Fahr., then the tubular stove altogether failed, and the regenerative stove must be used. The question of importance connected with this subject was, whether it was desirable to use blast of such very high tempera- ture. Some years ago it was the opinion of practical ironmasters, that the quality of the pig metal produced was deteriorated when * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Vol. XXX. Session 1869-70, pp. 315-317. 5Y/? WILLIAM SIEMENS, F.R.S. 133 mperature of the blast exceeded 500° or 600°. Now, how- i-vrr, ironmasters saw the advantage of raising the temperature of the lilast from G(>»>° to 800° or 1,000° ; and in using this regenera- tive stove, the temperature had been raised as high as 1,400°, without any deterioration of the quality having been observed. At the same time, there were ironmasters of high intelligence who asserted, that though the quality of the metal was maintained, yet that there was very little or no economy whatever in increasing the temperature of the blast above 1,000° ; but although this view had been gravely advanced lately, in discussions that had taken place before another Institution, he felt convinced that the conclusion in question was based upon a misapprehension, and would share the fate of the former objections to the introduction of hot blast generally. In inquiring into the chemistry of the blast furnace, it would be difficult to separate carefully the operations going on at each stage within the vast mass of incandescent matter ; but if the problem was to decide upon the goodness or the efficiency of a mechanical contrivance for transmitting power, consisting of a number of wheels, cams, and differential pulleys, there would be no very minute inspection of the effect produced by each crank, wheel, or pulley ; but the conditions of power applied to the machine would be taken, and the power judged by the motion of the load at the other end, taking it for granted that, according to the law of the conservation of force, nothing could be added or taken away except by friction. In the same way he looked upon blast furnaces. It was known that carbon, fluxing material, and ore, consisting for the most part of sesqui-oxide of iron and of silica, were put into the furnace, and atmospheric air was blown in at bottom. It was known that atmospheric, air on coming into contact with carbon in a state of incandescence formed one of two combinations — viz., carbonic acid if the combustion was perfect, and carbonic oxide if the combustion was imperfect. It was known that when a pound of carbon was burned into carbonic acid 14,000 units of heat were liberated ; whereas if carbonic acid was formed, only 4,000 units of heat were liberated. It depended, therefore, entirely upon the composition of the gases resulting from the combustion in the blast furnace what would be the effective duty performed. Analyses of the gases issuing from the top of the furnace proved 134 THE SCIENTIFIC PAPERS OF them to consist of about -ifchs of carbonic oxide and -J-th of car- bonic acid, and if this proportion was invariable, it would be possible to say with great precision what would be the amount of heat developed by a given amount of blast of a given temperature. There were several duties to be performed by the heat thus developed. The iron oxide had to be deoxidized or reduced, and the iron had to be melted. The " gang " and flux had to be combined and melted; and the products of combustion themselves escaped at the top at a certain temperature, which im- plied a loss of heat. But, without going into a priori calculations of these separate duties, he found that the necessary consumption of coke to smelt a ton of iron from Cleveland iron-stone, contain- ing 40 per cent, of iron, could not be less than 19'6 cwt. This limit of economy could not be surpassed, however much the capacity of the furnace might be increased ; it was the limitation which could be approached but never exceeded, except by raising the temperature of the blast to a higher point. In doing that there was heat im- parted from without the furnace, which necessarily saved a similar amount of heat that had to be developed inside the furnace, by com- bustion of coke by means of the blast. In continuing this argument it might be thought, at first sight, that the burning of 1 pound of fuel in the stoves would save 1 pound of coke in the blast furnace ; and this would really be the case, if the products of combustion of the blast furnace were carbonic acid, as in the stove ; but in- asmuch as the escaping gases were a mixture of carbonic acid with carbonic oxide, in the proportion of 1 to 4, the number of units of heat produced within the furnace per Ib. of fuel would be reduced in the proportion of 14,000 : $ 4,000 + £ 14,000 or of 14,000 : 6,000 ; that was to say, the number of units of heat produced by each pound of carbon consumed in the blast furnace did not exceed 6,000 ; whereas each pound of carbon burned in the stove would produce 14,000 units. It was evidently, therefore, important to raise as much heat in the stove as possible, in order to save more than double the amount in the blast furnace ; and when it was borne in mind, that the fuel in the stoves was obtained for nothing by burning the waste gases from the top of the blast furnace, it was obvious that there was the strongest argument for getting as much heat as possible in that way. The argument in- sisted upon by some ironmasters, that it would be no use to go Sffi WILLIAM SIEMENS, F.R.S. 135 beyond 1,000°, was based upon a misconception. They showed that each degree of extra heat in the blast produced a diminishing amount of saving in coke per ton of iron ; but they lost sight of this circumstance, that the quantity of blast used per ton of iron was greatly reduced when raised to a high temperature, — the quantity of blast used being proportionate to the amount of carbon burnt in the blast furnace. In effecting, therefore, a re- duction of the coke from 24 cwt. to 20 cwt., the amount of blast used per ton of iron was diminished in the same proportion, and 1" of temperature added to the blast did not represent the same amount of heat as 1° of heat communicated to blast of a lower temperature, when relatively a larger quantity was used ; but if the effect of 1 unit of heat added to the blast in the stove at various degrees was taken into account, it would be found that as much saving of coke was effected in the blast furnace by adding to the blast above 1,000° as there was by adding 1 unit of heat below that limit. There was the further important saving of fuel and engine-power, in effecting an increased duty with a given amount of blast, which had been neglected in these calculations. It would take up too much time to go further into this some- what complex question, as it would be necessary to take into account the increased proportions of the carbonic acid gas and the lower temperature of the waste gases which resulted from high temperature of blast ; but the question resolved itself into a simple one if it was looked at from a general point of view — that each unit of heat given to the blast before entering the furnace must save fuel equivalent to between 2 and 3 units of heat in the furnace, and moreover, that a much cheaper fuel was available in the stoves than within the blast furnaces. 136 THE SCIENTIFIC PAPERS OF In the discussion of the Paper "ON THE WARSOP AERO-STEAM ENGINE," By Mr. RICHARD EATON, THE CHAIRMAN (MR. C. WILLIAM SIEMENS) * remarked that the subject of the paper was a very interesting one, both on account of the theoretical questions involved, and also in conse- quence of the practical results that had been arrived at, which seemed to be of a decidedly favourable character. The main question that presented itself in regard to the use of the air injection was, what was the cause of the advantages ascribed to it. These advantages were of two kinds : — first, the advantage in the boiler of preventing sediment and preventing priming by the injection of heated air into the water ; and secondly the advantage in the engine of getting more work done by a given volume of the mixed steam and air than would be performed by an equal volume of steam alone at the same pressure. With regard to the advantage in the boiler, consequent upon the injection of divided currents of heated air into the water, he thought there was reason to, anticipate a marked effect from such a process ; for each bubble of heated air rising through the mass of hot water would naturally become saturated with steam by its contact with the water, increasing in volume many times, and would thus relieve the evaporating surface of the boiler of part of the work it woukj otherwise have to perform. Moreover in ordinary boilers, the steam being generated only in contact with the evaporating surfaces of the boiler-plates and tubes, each bubble of steam at the moment of its generation left behind it a liberated particle of solid matter, which had previously been contained in the water ; and this being liberated in immediate contact with the boiler surface, it was natural and probable that it should attach itself at once to that surface in the form of a solid incrustation. If however the required evapora- tion in a boiler could be produced otherwise than in contact with the * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers, 1870, pp. 245-248. SIX WILLIAM SIEMENS, F.R.S. 137 N it appeared likely that the sediment in the water would form its'-lf into mud composed of an aggregation of separate small particles ; and from the facts brought forward in the paper this •d to be the action that really took place with the injection of the heated air. With regard to priming, an interesting point to ascertain in a boiler working with the air injection would be the temperature of the water with reference to the working pressure of the mixed steam and air : because when two gases co-existed in the same space, each exerted its pressure independently of the other, and therefore it seemed reasonable to infer that the temperature of the water would be lower than the temperature corresponding to the pressure in the boiler, in the proportion of the original pressure of the steam alone to the actual pressure of the combined steam and air in the boiler. Thus supposing that the steam in the boiler were at a total pressure of three atmospheres, the water being at the corresponding temperature of 275° Fahr., and that an equal volume of air at atmospheric pressure were compressed and forced into the boiler, the compressed air would expand again to atmo- spheric pressure in the boiler during the transit of the air-bubbles through the heated water, and each bubble of air would take up steam by vaporisation until the point of saturation was reached. The pressure of the mixed steam and air in the boiler would then be four atmospheres, while the temperature of the water would correspond to the density of the steam irrespective of the air present, and would consequently remain that corresponding to a pressure of only three atmospheres, the atmosphere of air permeating the whole steam space in equilibrium, in accordance with the law of the mutual diffusion of gases. It would be interesting to observe whether this were really the fact ; and if it were so, he thought it would explain the circumstance which had been mentioned in the paper, that the moment the air was turned off violent ebullition and priming took place. For as soon as the air was turned off, the mixture of air and steam over the water in the boiler would no longer be replenished by a similar mixture of gases ; and the temperature of the water being below that corresponding to the pressure of the mixed air and steam, a sudden collapse of the steam would necessarily take place ; and as a consequence the engine would require more steam, the throttle valve would open wide, and the larger volume of steam suddenly called for would of itself 138 THE SCIENTIFIC PAPERS OF naturally induce priming, independently of the further circumstance that the liberation of the steam from the water would no longer be facilitated by the passage of bubbles of heated air through the mass of the water. In reference to the other question — why the mixture of steam and air should do more duty in the engine than an equal volume of steam alone at the same pressure — he did not think this could be because the air-compressing engine which was united with the steam-engine was more economical than the steam-engine itself. On the contrary, mere air-engines, wherever they had been tried, had not given such favourable results as good steam-engines ; and there were theoretical reasons why they could not give better results than a proper steam-engine. It had however occurred to him as an explanation which might be suggested of the economy found to result from the use of mixed steam and air in the engine, that the presence of air in the steam cylinder would certainly prevent the condensation of steam against the sides of the cylinder : and the loss from this cause he believed to be much greater than was usually supposed. If the cylinder was uncovered, the loss by condensation was very great, and was shown by the form of the indicator dia- grams taken from such engines ; and even when the cylinder was carefully clothed, there was a considerable condensation from the high-pressure steam coming in contact with surfaces that had been cooled by previous exposure to the condenser or to the exhaust steam at atmospheric pressure. This condensation he believed took place even when the steam cylinder was thoroughly steam-jacketed all round and at the ends, although to a much less extent, and in that case it arose from the slow conducting power of the thick metal sides of the cylinder allowing the inner surface to continue considerably cooler than the outer surface heated by the steam in the jacket ; and though the steam thus condensed in the cylinder was afterwards evaporated a£ \n in the latter part of the stroke, yet its mechanical effect was aln ^! 15J 4 l.H 154 17J 17 f> 1 .>-,• 155 18 17f (i 184 m 7 18J 184 Another set of experiments has been tried with the steam jet used as a blower for compressing air into the same closed vessel of 225 cubic feet capacity. For this purpose the conical delivery funnel of the steam jet was connected with the vessel by means of a 3-inch pipe containing a stop-cock ; and into this pipe was delivered a small jet of cold water through a pipe of | inch diameter under a pressure of 40 Ibs. per square inch, with the object of condensing the steam from the blower, the water being turned on simultaneously with the starting of the steam jet. The sectional area of the outer annular air passage in the blower was 0'20 square inch, and of the inner air passage in the centre of the jet T 1 1; square inch, making a total of 0'36 square inch of air section. The sectional area of the annular steam jet was 0'07 and (fl 2 square VOL. i. L 146 THE SCIENTIFIC PAPERS OF inch in the different experiments, the results of which are given in the following Table II. : — TABLE II. EXPERIMENTS WITH STEA'M-JET BLOWEK COMPRESSING AIR INTO A CLOSED VESSEL. AREA OF ANNULAR ORIFICE OF STEAM JET. Time of 0'07 sq. in. 0-12 sq. in. 0'07 sq. in. With With Without Condensing Condensing Condensing Water. Water. Water. Pressure. Pressure. Pressure. Minutes. Inches of Inches of Inches of Mercury. Mercury. Mercury. 1 6 5 9 I 10 !) 11 i 12 12 14 H 13 16 15 if 13£ 19 15J 2 14 21i 16 3 15 24 16£ 4 15i 25 16J 5 15 24i 12 8 14| 24i 11 7 14^ 233 .io| 8 14| 23£ 10 Final temperature of air in vessel. 113° Fahr. 158° Fahr. At the end of the fourth minute the stop-cock was closed, shutting off the steam-jet blower, and at the same time the condensing water was shut off ; it will be seen that the pressure in the vessel then fell slightly, owing to the condensation of the small residue of the steam from the jet. In the third experiment, in which no con- densing water was used, the fall of pressure was more considerable, and the final temperature of the air in the vessel was higher. The steam pressure in the boiler was 50 Ibs. per square inch. The following are some of the applications which have already been made or are in course of being made of this improved form of steam jet. PNEUMATIC DESPATCH TUBES. — First, to the working of pneu- matic despatch tubes. For this purpose the steam jet has a great SfK WILLIAM SIEMENS, F.R.S. 147 advantage over an ordinary steam-engine and air-pump in first cost and simplicity, and also in taking up much less space : the latter advantage being of the greatest value when it is required to work pneumatic despatch tubes in crowded localities where it is di Hi cult to obtain room for steam machinery. A pneumatic tube % inches in diameter, to be worked on the circuit system arranged by the writer, has been laid down by the postal authorities in London, from the Central Telegraph Station in Telegraph Street to Charing Cross and back, with intermediate stations at the General Post Office and near Temple Bar. The length of tube forming the whole of this circuit is 6,890 yards, or nearly four miles. This line was designed to be, and is, as a rule, worked by means of an air-pump A, driven by a steam-engine, as indicated in the diagram, Fig. 6, Plate 25. The pump draws air out of a vacuum vessel V, and forces it into a pressure vessel P, both vessels being in connection with the pneumatic tube T, as indi- cated by the arrows. These vessels are introduced in order to prevent the pulsations of the engine from being felt in the work- ing of the tube, and are of course unnecessary when the tube is worked by means of the steam jet. The piston carriers, which are propelled through the tube by the vacuum produced, are of the cylindrical form shown in Figs. 7 to 9, Plate 26 ; they consist of a gutta-percha case covered with drugget or felt, and are made an easy fit in the tube, so as to slide freely through it. This line has been experimentally worked by means of three steam-jet exhausters, similar to the one shown in Fig. 2, arranged in the manner shown at E E E, Fig. 6, so that all three draw air out of the same tube F, the steam being supplied to them by the steam pipe G. When working with these three exhausters, the mean speed of a piston carrier travelling through the tube from Charing Cross to Telegraph Street was 14| miles per hour. The vacuum maintained in the tube was equivalent to 10 inches of mercury, the steam pressure being 40 Ibs. per square inch ; and the quantity of coal consumed under the boiler was 5G Ibs. per hour. In the case of long lines of pneumatic tubes, it will be better to work them with an exhauster at each end. For placing the piston carriers into the tube or taking them out of it at the different stations S S, Fig. 6, without interrupting the current of air, the intercepting apparatus shown in Figs. 10 to 12, L 2 148 THE SCIENTIFIC PAPERS OF Plates 20 and 27, is employed. This consists of two short tubes B and C, fixed side by side in a rocking frame, each of which can be brought into line with the circuit tube T at pleasure. Each end of the rocking frame is faced, and works against the faced side of a boss on the end of the circuit tube. Three annular grooves are turned in the faced side of the boss round the end of the circuit tube, for the purpose of preventing the leakage of air between the ends of the rocking frame and the bosses. One of the tubes B in the rocking frame is used as the sending or " through " tube, and is simply a hollow cylinder of the same internal diameter as the circuit tube T ; when this is in line with the circuit tube, a earner can pass through the instrument without being stopped, and this tube is also used for putting carriers into the circuit. The other or receiving tube C has a perforated diaphragm at its down-stream end, so as to arrest the carriers when it is placed in line with the circuit tube, as in Figs. 11 and 12. This receiving tube is D- shaped in section, with a flat cover, which can be taken off if required ; as for instance, to remove carriers, in the event of two arriving at once and so preventing the rocking frame from being moved. The flat cover is furnished with a pane of glass, to enable the attendant to see when a carrier has arrived. In order to prevent the continuous flow of air in the whole circuit of tube from being impeded by the receiving tube being left in the circuit after it has caught a carrier, a by-pass F for the air is provided, which communicates with the circuit tube T at both ends of the instrument. A sliding rod H, Fig. 10, held on suitable supports, is supplied for pushing the carriers out of the receiving tube, when intercepted and brought out of the circuit. The manipula- tion for sending and receiving the carriers is exceedingly simple ; and a treadle is provided for moving the rocking frame with the foot. RAISING OF WATER. — A second application of the improved steam jet is to the raising of water. For lifts not exceeding 20 feet a steam-jet exhauster could be used with advantage in situations where the erection of an engine and pumps would be attended with considerable cost and inconvenience, or where the work to be done was of short duration or of an occasional character, such as in draining lands, &c. When employed for this purpose the exhauster would be applied in the manner shown in Fig. 13, .sy/i1 WILLIAM SIEMENS, F.R.S. 149 Plate L>8, where A and B are two closed air-tight chambers fixed at a height of from 16 to 20 feet above the level of the water to be raised; inlet valves C are provided in the bottom of the chambers for the water to enter from the suction pipe I), and outlet valves (T for the discharge of the water raised. The exhauster E, supplied with steam by the pipe H, exhausts the air from the chambers A and H through the pipe F, which is provided with a reversing vuKv L for placing the exhauster in communication with each of the two chambers alternately ; and the delivery end of the rxhaiisU-r, which may be closed by a valve, also communicates with the chambers through the pipe K and the same reversing valve L. The chamber A is provided with a float M, the rod of which works by tappets the tumbling lever N, and this throws over the weighted lever of the reversing valve L by means of the looped rod R. The action of the apparatus is as follows. While the exhauster is drawing the air out of the chamber B through the pipe F, as shown in Fig. 13, thus causing the water to rise into the chamber through the suction pipe D under the pressure of the atmosphere, the discharged jet of combined steam and air from the exhauster passes through the pipe K into the top of the other chamber A, which is full of water. The water in this chamber will consequently flow out through the bottom outlet valve G, its discharge being aided by the forcing action of the entering current of steam and air from the exhauster ; and this forcing action may be regulated by closing the top of the delivery funnel of the exhauster, in which case the discharge pipe for the water from the outlet valve Gr may be raised above the level of the chamber A. As the water descends in the chamber A, the float M sinking with it moves over the tumbling lever N into the vertical position, from which when the chamber is emptied the lever will fall into the reversed position, thereby throwing over the reversing valve L. The action of the exhauster upon the two chambers is now reversed, the air being exhausted from the emptied chamber A, and the combined jet discharged into the chamber B, which during this time has become filled with water ; in this way the two chambers become alternately filled and emptied, and a continuous delivery of water is thus obtained. As the steam contained in the combined jet entering either chamber from the exhauster becomes 150 THE SCIENTIFIC PAPERS OF gradually condensed by contact with the water, a partial vacuum will be already formed in the chamber as soon as emptied, whereby the work to be done by the exhauster in then exhausting the chamber will be diminished. In order to prevent the noise which would be caused by the combined jet of steam and air issuing from the open top of the delivery funnel of the exhauster, a " sound killer " S may be placed on the top of the funnel, consisting of a cylindrical metal vessel containing a series of perforated wooden diaphragms ; this contrivance has been found by experi- ment to be very efficient in preventing noise. The following are the results of a preliminary experiment made with a rough apparatus for raising water, arranged as shown in the diagram, Fig. 14, Plate 28. The exhauster E was connected by a 2-inch pipe F to a closed vessel A capable of holding 10*3 cubic feet, into which the water was raised from varying depths through the suction pipe D of 2 inches diameter. The sectional area of the outer annular air passage in the exhauster used in this experiment was 0'35 square inch, and of the inner air passage in the centre of the jet 0'16 square inch, giving a total of 0'51 square inch of air section. "With the sectional area of the annular steam orifice adjusted to (VOS) square inch, and with a steam pressure of 60 Ibs. per square inch in the boiler, the exhauster raised 10'3 cubic feet of water 12 feet high in 40 seconds, and the same quantity 17^ feet high in 75 seconds. With the same area of air section, but with the area of the steam orifice adjusted to 0'08 square inch, and with 50 Ibs. steam in the boiler, 10'3 cubic feet of water were -raised 15 feet high in 40 seconds. The height of lift attainable depends upon the pressure of steam employed ; and the quantity of water raised depends within certain limits upon the magnitude of the jet. EVAPORATION OF SUGAR. — A third application of the improved steam jet is to the evaporation of sugar. In consequence of the remarkable results obtained with this steam-jet exhauster, it is proposed by Mr. R. A. Robertson of London to apply it to sugar- boiling in the West Indies ; and he has communicated to the writer the following notes on the subject. The steam-jet exhauster has been employed experimentally with considerable success in exhausting vessels for evaporating liquids in vacuo, and its application for this purpose promises to SIR WILLIAM SIEMENS, F.R.S. 151 become of great value in the colonies for evaporating cane juice, principally on account of the simplicity of the arrangement. The Lrivut, loss and deterioration consequent on the high temperature to which cane juice must be exposed for evaporating it on the old system in open pans are well known, and many ingenious plans li;t\' IHVII invented and to some extent worked for evaporating at lo\v temperatures ; but, on account of the improved plans being i-itlitT very much more costly or requiring much more skilled attention to work them, the greater part of the sugar produced is still made on the old and wasteful plan. Of all the contrivances fur evaporating at low temperatures the ordinary vacuum pan exhausted by pumps is at present the best, when carefully designed ; and in it under favourable circumstances very rapid evaporation can be produced at low temperatures. In the sugar-growing colonies however almost every circumstance is unfavourable for this mode of working ; the water required for condensing the vapour from the evaporating pan is warm, and consequently must be used in large quantities, thereby necessitating large pumps for its removal, and for exhausting the pan ; the pumps and motive power thus form together with the pan a very costly apparatus, which requires a considerable amount of skilled attention, often not obtainable, and frequent repairs. On the contrary, a vacuum pan exhausted by the steam jet exhauster in the manner shown in Figs. 15 and 16, Plate 29, becomes a very simple apparatus, only requiring a supply of steam at a moderate pressure for the jet A, which exhausts the vapour given off by the boiling solution of sugar or other liquid in the pan B ; and the steam and vapour together are then passed through the heating tubes D of the pan, thereby producing evaporation. The area of the steam jet is regulated by the hand-wheel C, the steam being supplied by the pipe E ; and the course of the current of steam and vapour is indicated by the arrows. By this arrange- ment the costly vacuum pumps and the steam-engine or other motive power are dispensed with, as well as the condenser and its supply of condensing water, the latter being in many places a consideration of vital importance ; and in their stead is sub- stituted the steam-jet exhauster, a comparatively cheap and simple apparatus, requiring little or no attention, and not liable to get out of order. 152 THE SCIENTIFIC PAPERS OF Experiments on this mode of evaporating have been so successful that a vacuum pan is now being constructed as above described, capable of evaporating 50 cubic feet of water per hour, in which it is estimated that a vacuum of from 18 to 20 inches of mercury will be maintained. The form of pan shown in Fig. 16 is the simplest arrangement in which the steam jet exhauster can be applied for the purpose ; but the exhauster can with equal advan- tage be applied in those cases where vacuum pans are worked on the systems known as double and triple effect. It has been successfully employed to exhaust a vacuum pan having a condenser placed high enough above the ground to discharge by gravitation against the vacuum the condensing water in which the vapour from the pan was condensed ; there was thus left only the air and a very small quantity of vapour to be removed by the exhauster, which in this case was a very small one, not using sufficient steam to produce evaporation. The steam-jet exhauster is further expected, on account of its cheapness and simplicity, to prove very useful in the colonies for draining the molasses from the sugar, by exhausting the air from below the perforated bottom of a strainer containing the undrained sugar, the pressure of the atmosphere then driving the syrup or molasses through the sugar and perforated bottom. By this means the crude and imperfect mode of draining by gravitation, and also the more elaborate but costly and troublesome centrifugal strainers, can be superseded with advantage. BLOWER FOE GAS-PRODUCERS. — A further application of the improved steam jet is to gas-producers for heating purposes. The author has had occasion to make numerous applications of the steam jet arranged as a blower for accelerating the distillation of fuel in his gas-producers, as shown in Figs. 17 and 18, Plate 30. The blower B is built into the side wall of the producer, and the combined current of air and steam delivered by it issues through an opening A into the space C underneath the fire-grate, which is closed by doors 1). The small proportion of steam that enters together with the air is just sufficient to assist beneficially in the production of the combustible gas, inasmuch as in passing through the incandescent fuel the steam becomes converted into hydrogen and carbonic oxide. The steam is admitted to the blower through the branch pipe E from the main steam pipe F, which supplies a WILLIAM SIEMENS, F.R.S. 153 number of blowers in a series of gas-producers. A valve e used, and that the gas production of each producer in con- suming small fuel is raised from l£ tons to 8 tons of gas per 24 hours ; while at the same time the quality of the gas is improved, owing to the generation of hydrogen from the steam which enters intermingled with the air. These applications of the improved steam jet suffice to illustrate its scope and value. Other useful applications will readily suggest themselves, where work may be accomplished by exhausting or compressing air or gases. In conclusion the author would remark that although the steam jet is not a new mechanical agent, and has been applied before for various purposes and in a variety of forms, yet the mechanical conditions under which it is capable of developing the greatest amount of useful effect have not previously been laid down or practically realised in such a way as to produce results at all comparable with those obtained from a steam-engine working an air-pump ; but this it is maintained a steam jet may do, if care be taken that the available elastic force is changed into onward motion of the combined jet, and again into onward pressure, with- out undue loss of effect by eddies or by development of sound or heat, which have constituted the principal results in the case of an ordinary steam jet. The PRESIDENT said he had been led to investigate the subject of the steam jet in consequence of having been engaged in con- structing a circuit of pneumatic despatch tube for the Central telegraph office in London ; the tube itself had cost £3000, and fully as much had been spent on the engine and air pump. As there was moreover great difficulty in finding room for this machinery in so crowded a locality, it had occurred to him that a more direct means of propelling the piston carriers through the tube would be a matter of some importance ; and in considering 154 THE SCIENTIFIC PAPERS OF the conditions of a steam jet he had been led to the conclusion that, if the elastic force of the steam could be all employed for giving velocity to its particles, and if each particle of steam so accelerated could be brought into direct and immediate contact with the air to be impelled, an average speed of the combined current could be obtained, which should represent nearly the whole of the elastic force originally existing in the steam. If this combined current were then sent through a long expanding mouth- piece or tube, enlarging gradually in a parabolic curve, so that the velocity of the current should be gradually converted into pressure by bringing the particles nearly to rest, it had appeared to him that very favourable results might be obtained ; and the experi- ments he had made had proved that these anticipations had been correct. There were some remarkable results connected with this steam jet. The quantity of work done by it, measured by the weight of air delivered per minute, was proportionate absolutely to the amount of surface contact between the steam jet and the air to be impelled, irrespective of the pressure of steam employed. Thus in discharging the combined current into the atmosphere, the same weight of air per minute would be thrown out with a steam pressure of 5 Ibs. as with GO Ibs., the only difference being that with the lower pressure of steam the limit of exhaustion or com- pression would be sooner reached than with the higher. The experiments also showed that the degree of exhaustion or com- pression capable of being produced by the steam jet, that is the difference of pressure between the air at the jet and that in the vessel from which the jet was exhausting or into which it was compressing the air, was exactly proportionate to the steam pressure ; so that with 100 Ibs. steam above the atmosphere the degree of exhaustion or compression attainable was double what it was with 50 Ibs. steam. A third result was that, in exhausting the air from any vessel by the steam jet, it took as long a period of time to exhaust the first 1 Ib. of pressure, from the atmospheric pressure of say 15 Ibs. down to 14 Ibs., as it did to reduce the pressure 1 Ib. in any lower part of the scale, say from 8 Ibs. to 7 Ibs. ; this was explained by the consideration that the weight of air, which had to be put into motion with such a velocity as would force it through the contracted opening at the base of the expanding .s/A' WILLIAM SIEMENS, F.R.S. 155 delivery tube, was the measure of the working capacity of the instrument. These were very distinctly marked characteristics of a good steam jet ; and if they were attended to in the construc- tion of the jet apparatus for any particular application, it would be found that very economical results could be realised for the steam expended. He exhibited a full-size specimen of one of the steam-jet ex- hausters employed to exhaust the pneumatic tube connecting the iclfirraph offices in London, so as to maintain a current of air flowing continuously through the tube in the same direction. Tin- tube formed a complete circuit, and the piston carriers, whether put in at the commencing station of the circuit or at any intermediate station, all travelled in the same direction ; the result was that a tube of only 3 inches diameter was sufficient for a great amount of work, because there might be ten or more carriers in the tube at a time, all flowing towards the end station, but capable of being intercepted and taken out at any intermediate station. In answer to various Speakei-s — The PRESIDENT replied that the expanding form of the delivery tube from the steam jet was of considerable importance, though not so much so in the case of air as where a denser fluid had to be dealt with, as in the water jet of the Giffard injector. From experiments that he had made with a parallel delivery tube, in comparison with the expanding form, he had found that, in exhausting a vessel to the extent of producing a vacuum of '20 inches of mercury, the expanding tube rendered the jet about 10 per cent, more effective than it was with the parallel tube ; but in exhausting to only a small extent, the greater density of the fluid would cause the expanding tube to be as much as 20 per cent, more effective than a parallel one. The form which he had adopted for the expanding delivery tube of the steam jet was a parabolic curve ; but the difference in effect between this and an ordinary straight cone, with the same areas of passage at the two extremities, would be immaterial. The mixing chamber, which had to be of a definite length in proportion to the breadth of the annular air passage, was made to diminish gradually in area, 156 THE SCIENTIFIC PAPERS OF somewhat in the form of a " vena contracta," the rate and extent of contraction being determined in each individual case according to the velocity of the combined issuing current. But the point of chief importance in the instrument was the mode of bringing the entering air into contact with the steam jet. As the working power of the jet was proportionate to the extent of surface contact between the steam and the air, the annular form of jet suggested itself as the most suitable ; and the thickness of the annular film of steam should be very small, about -gV^1 inch having been found by experiment to be the maximum thickness of film that was consistent with economical results. If the thickness of the jet were increased beyond this amount, the particles of steam inside the thickness of the jet would flow on at a greater rate than the outer particles forming the skin of the jet. the latter being retarded by contact with the air ; and eddies within the atmosphere of the steam itself would be the result. Again, if the steam jet were simply made to issue into a plain open tube, through which the air had to be propelled, the result would be very inconsiderable, because the eddies formed between the air and the steam would then attain their maximum amount ; the steam issuing with great velocity and the air being nearly stationary, the latter would not be so much impelled in a steady current as set in rotation and rolled forwards by the power represented by the difference of velocity between the two fluids. It was consequently requisite that the air should be accelerated as nearly to the full velocity as practicable before coming into actual contact with the steam ; and this was the most important point connected with the apparatus. The area of the air passages was therefore gradually contracted for some distance as they approached the issuing orifices ; and the combined areas of the central air aperture inside the steam jet and of the annular aperture outside the jet were made to be together rather less than the area of the issuing orifice at the outer extremity of the mixing chamber, through which the combined current issued ; this arrangement ensured the air attaining the full velocity of the combined jet, whereby the amount of eddies and the consequent loss of power were reduced to a minimum. The PRESIDENT considered that the suggested application of the A/A' \\-II.IJ.\M .S7/.M//..\'.V, I-.R.S. 157 D jet for removing dust from the casing of millstones daring the grinding might be attended with in><> larger rivets stood forward, and naturally would take nearly the whole of the strain that fell upon the plate. The other four rivets stood back to such an extent that, before they would receive any considerable portion of the strain, the two forward rivets would be loaded to such an extent as to cause a partial yielding of the metal, and, as they were near the edge, tearing action would set in. Now a material, however strong it might be, could be torn without much effort. Thus if a strip of india-rubber were nicked, it tore with little stress ; whereas if there was no nick, it would bear almost any amount of elongation. In like manner the mild steel had to be treated differently from iron ; and experiments like the present gave better information than any learned essays on the subject could possibly supply. When the strips of the same plate •were tested in the usual way, they stood the test as well as every other portion of the material supplied. The use of iron rivets had been advocated, and was still advo- cated by many, for riveting these mild steel plates together. He could not too strongly protest against that practice. It was utterly against nature to stick together material like this mild steel with another material, iron, which behaved quite differently as to elongation and yielding. Again, when iron rivets were used, the rivet-holes must necessarily be larger than they would need to be for steel rivets ; being larger they would be put a greater distance apart, and the distance practically chosen was the same as was in ordinary use for iron plates of 20 per cent, greater thickness. Thus the thinner plate was held together at points relatively further apart ; and the result was that the metal between hole and hole could not be so securely held as it should be, and tearing action set in. He was very glad to see that Mr. Boyd had resisted the temptation of using iron rivets, and had adopted steel riveting in these boilers. He did not quite agree with the author that punching neces- sarily diminished the strength of a steel plate something like 33 per cent. No doubt his experiments had been very carefully made, but there was a great difference between punching and punching. His belief was that on punching a cylindrical piece or " burr " out THE SCIENTIFIC PAPERS OF of that plate it would be found that this piece was not as thick as the plate, but on the contrary considerably thinner. What then had become of this metal ? It had not gone to increase the diameter of the burr, although its lower part might be a little bulged out in that way ; but while the punch was being driven into it that metal had accumulated somewhere in the plate. There was thus a ring of highly compressed material formed round the hole, and this compression caused the surrounding portion of the plate to be under high tension. The result must be that, if pressure was applied, the portion already under high tension received additional tension, and tearing action began. Hence the great loss of strength in punching. He held in his hands the results of some experiments, made with great care by Mr. James Riley at the Landore works, which proved precisely what he had stated. There however plates, which before punch- ing bore 29'33 tons per sq. in., bore after punching 30*7 tons per sq. in. without annealing. The reason of this anomaly was, the* die in these cases was made considerably larger than the punch, and thereby the compression was practically avoided.* Another kind of punch had lately been introduced from America, which was well worth the attention of the meeting. It was a helical punch, which, instead of driving out the metal before it, cut it out in a spiral form. This mode of punching he thought very pro- mising, and he believed by adopting such a method the weakening effect that had been experienced in punching thick plates would be entirely got over, without unduly increasing the size of the die. In punching thin plates the author found there was but very slight reduction of strength, and that the punched plate when annealed resumed its former strength exactly. It had also been found that by riming out a punched hole the strength of the metal was entirely restored : showing that the cause of weakness was in * Mr. J. GL Mair has since communicated to the Secretary the results of some experiments made on this point by Mr. Henry Sharp, of Bolton. Four pieces of \ in. steel plate, 2^ in. wide, were punched with an \± in. punch, but with a die g in. in two cases and f in. bare in the other two. The results were as under, showing 25 per cent, more strength for the greater clearance : — I in. die. f in. bare die. 1st experiment . . . 32 '30 25 '92 2nd experiment . . . 32 '85 26 '08 32 '5 tons per sq. in. 26 '0 tons per. sq. in. SIX WILLIAM SIEMENS, F.R.S. 173 immediate vicinity of the hole, and did not extend to any distance through the metal, which was in accordance with the explanation he had suggested. The author had added an important item of information with iv_rard to the staying of flat surfaces. The addition of the nuts to the stays showed a remarkable increase of strength, and he hoped that mode of staying would be generally adopted. It was a question however whether for flat stay-plates this very mild steel should be used ; it would probably be more advantageous to use for flat surfaces steel containing perhaps 0*4 per cent, of carbon ; they would then get a material of great stiffness as well as great strength, and still of sufficient ductility. Steel with about 0'4 per cent, of carbon would not indeed elongate 25 per cent, before breaking, but it would elongate probably 12 per cent. ; and in the case of a flat plate that ought to be sufficient. He might mention that lately he had witnessed two experiments made with a view of bursting a steel boiler. These were made at Swindon by Mr. Dean of the Great Western Railway ; and Mr. Parker, the Chief Surveyor at Lloyd's for the boiler department, was present at the second experiment. Both experiments failed, i.e., they could not burst the boiler ; and he believed it was impossible to burst a steel boiler. It might be expanded and the joints racked to the extent of introducing an amount of leakage that would prevent further accumulation of pressure ; but it would never be burst. That condition of things was certainly a satisfactory one. In the discussion of the Paper "ON A NEW REVERSING AND EXPANSIVE VALVE-GEAR," by Mr. DAVID JOY, DR. C. W. SIEMENS * said that, listening to the very excellent paper which had been brought before them, and to the observa- * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers 1880, pp. 444-445. 174 THE SCIENTIFIC PAPERS OF tions of the speakers who had taken part in the discussion, one result seemed to his mind to be quite certain, namely, that the link-motion was doomed. He must say he did not feel the same regret on that score which appeared to animate Mr. Head. The link-motion had no doubt been a way out of a difficulty ; but it was correct only within very narrow limits, and the moment those limits were exceeded it did not produce the expansive action desired. A motion had now been brought before them which challenged comparison with the best expansive gear that could be mentioned. There was a clean cut-off ; the steam was put on at once in ample quantity, and the exhaust also was opened promptly at the right time. There was also the means of adjusting the action so as to make the up-stroke and the down-stroke perfectly alike, which, as they all knew, was not the case with the link- motion. And, as Mr. Webb had beautifully illustrated by his locomotive, the new gear had the advantage of giving a large useful space on the main shaft for increasing the length of the bear- ings. These were very important advantages, which Mr. Joy might claim for his motion. But they had also been put in pos- session of two other motions, which seemed to be as perfect as Mr. Joy's. Still they need not regret that result. There were points of difference between the gears, though they all aimed at the same result, a very perfect cut-off and a perfect mode of re- versing the engine. The object was achieved by different mechanical details, all of which he considered were superior, both theoretically and practically, to the old link-motion. With the criticism offered by Mr. Boyd, in regard to a portion of Mr. Joy's motion, he thoroughly agreed. The slotted disc, which was turned into a different angular position, with the slide-block grinding up and down in the slot, was not, he thought, a desirable detail ; and he would recommend Mr. Joy to do away with it. He observed it had actually been done away with in one arrangement shown. All the friction was there reduced to the friction on the pins, which must be preferable to friction of sliding surfaces. With that exception Mr. Joy's motion appeared to him perfect, and one that would no doubt receive the most earnest attention of mechanical engineers. S7A WILLIAM SIEMENS, F.R.S. 175 In ////• ili*-i;*sion of (ha Paper "ON GAS-GENERATING FURNACES," By Mr. F. LIRMANN, Du. Si KM FA'S* said, Mr. Liirraann was so well known as a gentleman who had originated practical ideas which had been hiiLTt-ly used, that anything coming from him deserved much con- sideration. The gas-producer now advocated by Mr. Liirmann \v;i< l»ased, as might be supposed, upon a sound philosophical prin- ciple— that of concentrating heat as much as possible in the operation of converting the solid fuel into gas. He had, however, two criticisms to make on Mr. Liirmann's paper, the one regarding the historical record with which he prefaced his arguments, and the other as to the technical value of the particular arrangements proposed by him. It was now more than thirty years since he had constructed the first gas-producer applied to the regenerative gas furnace, and he might add, that the subject of fuel conversion had engaged his attention ever since. Under these circumstances he should have expected to find in the historical record of the author some allusion to his labours in this direction. In the years 1863 and 1864 he patented several varieties of gas-producers, in which the coal passed towards the fire-grate through retorts, in a vertical or inclined direction, which retorts were heated either by the gas resulting from the operation itself or from extraneous sources. Indeed, the hopper arrangement, described in the paper as Price's gas-producer, might, amongst others, have been taken from one of his specifications of that early date. He might further mention that in the year 1863 he brought a bill before Parliament to supply Birmingham with heating gas, and that the gas-producer then put forward comprised both the principle of re- tort-heating and that of the open grate for the final conversion of coke into carbonic oxide, whilst by another arrangement the coke was withdrawn from the apparatus to be used separately as breeze. This arrangement, he believed, was still in operation at Messrs. * Excerpt Journal of the Iron and Steel Institute, 1880, p. 583-585. 176 THE SCIENTIFIC PAPERS OF Russell & Co.'s tube works near Birmingham. He held in his hand the specifications of the two patents alluded to, and it might not be without interest to the Institute to learn exactly what was known and claimed regarding the proposed method of producing gas as early as 1863 and 18G4. In the patent of 18G3 it is said : " Thus, although we much prefer to make use of regenerators for producing the intense heat required, yet heating apparatus of different construction may be applied, and the form and construc- tion of the heated chambers, as well as the means adopted for charging and discharging them, may be greatly modified ; also the chambers or retorts may be arranged in a somewhat inclined position instead of being placed vertical," &c. ; and he claimed " constructing furnaces in which coal or other carbonaceous material is subjected, whilst descending gradually in upright recipients or retorts, to the action of intense heat resulting from the application of regenerators with reversal of currents, the result being either the total conversion of the carbonaceous matter into combustible gases when a grate is applied at the bottom of such recipients, or the production of both combustible gases and coke of superior quality, when admission of atmospheric air to the bottom of the recipient is prevented." And in 1864 the first two claims run as follows : " First, constructing apparatus for converting carbona- ceous matter into combustible gases, in which such carbonaceous matter is first caused to descend gradually through one or more vertical or inclined retorts, from the lower end of which it passes in a thick layer upon a fire-grate, the heated combustible gases resulting from the imperfect combustion of the fuel upon the latter being made to pass around or against the outer surface of the said retort or retorts. Second, constructing gas-producers (which are chiefly applicable for the conversion of binding coal into combustible gas) in such a manner that the fuel descends through an inverted funnel, acting more or less as a retort, upon a solid moderately-inclined plane supporting the column of fuel, such inclined plane having one or more openings at the top for the admission of atmospheric air, as well as for the introduction of bars to break up the masses of coke, whilst one or more other openings are provided at bottom for the removal of clinkers or ashes, and for the introduction of a further quantity of air or steam or both, in order to complete the conversion of the car- WJ 1.1.1 AM SIEMENS, F.R.S. 177 bonaceous matter, substantially as hereinbefore described." He made these quotations simply by way of addendum to the historical rrrord brought before them by the author, his personal interest in the matter having ceased \\ith the expiry of the patent through lapse of time. The reason for not persevering in the direction ndirated was due to the retort action being found too slow for the production of combustible gas in such quantities as were required for working large furnaces, and he expected that Mr. Liu-maun would be met with the same kind of difficulty when he attempted to give his gas-producers an extended application. His endeavours had since been directed to concentrate as much latent heat in the gas as possible, in order that it might travel, and t Ii-Telbre he had always used the spare heat for drawing up vapour, and to convert the water in this form into its two elements. In the form of producer now put forward, the enrichment of the gas was simply in the direction of obtaining a higher temperature, and this higher temperature could be utilized if the gas-producer was put into close connection with the furnace. But in the regenera- tive system that high heat was secured through the regenerators, and therefore was not required previously. In one form of the gas-producer, which was also largely used, a steam blast was employed, with a closed grate. He had since gone a step further in that direction, and he had obtained certainly a very remarkable result. ON THE USE OF COAL GAS AS A FUEL. BY DR. C. WILLIAM SIEMENS. DR. C. WILLIAM SIEMENS : * Mr. President, among the subjects suitable for discussion before this Society there is, perhaps, none more so than that of combustion, or rather that of the production of chemical energy, and its application. It has devolved upon to bring this subject before you, and although I should have * Excerpt Journal of the Society of Chemical Industry, 1881, pp. 39-46. VOL. I. N 178 THE SCIENTIFIC PAPERS OF preferred that the choice had fallen on a gentleman who could have given more time to the actual preparation of such a paper than I have been able to bestow upon it, yet having for nearly thirty years given much attention to the subject of combustion, and the utilization of gaseous fuel, it was perhaps natural thnt your President called upon me to open out the subject before this new Society. The fuel at our disposal, generally speaking, is coal, and in most applications coal, in its raw condition, is still used for the production of heat. I have put a table before you, showing the amount of heat energy residing in a pound of fuel. If that fuel is pure carbon, 14,544 units of heat are producible. If coke were used, and burnt entirely to carbonic acid, 12,500 heat units would be produced. If coal of the average quality is employed, 11,000 heat units may be obtained. But, if instead of using solid fuel we should employ gaseous fuel, we immediately jump to much higher figures. Olefiant gas gives in its combustion 21,344 heat units ; marsh gas, 23,500 ; and hydrogen, 62,000 units, or very nearly six times as much as raw coal. Then carbonic oxide, not counting the oxygen already taken up, but simply the carbon in the carbonic oxide, gives 10,100. These figures may serve to show the great advantage in the use of gaseous fuel ; and if by some means or other we could impart to the fuel as it is consumed the greatest possible power for the production of heat energy, it would be clearly to the advantage of the user, because not only does this better fuel produce for the same weight of material a greater result, but it produces that result with a smaller expendi- ture of oxygen, that is, with less draught. The principal reason why gaseous fuel, especially hydrogen, produces such a large amount of heat energy, consists in the heat energy already expended in expanding it to its volume, and the ultimate result, therefore, depends less upon combustion than it would do in the case of coal where a large proportion of the heat produced is expended in converting the solid into gaseous fuel to begin with. But gaseous fuel, when used instead of solid fuel, possesses several other advantages. It is much easier to produce perfect combustion in using gaseous than in using solid fuel. Solid fuel, when first heated, flies off to a great extent into products of distillation, and the supply of oxygen can hardly keep WILLIAM .S/A'.J/A.Y.s; F.R.S. 179 with such a sudden increase of production of gaa. The result is smoke, and smoke is waste, whichever way it is viewed. .Moreover, it is a public nuisance, and as such it should be done away with. Then, in using gaseous fuel, the supply can be kept constant, and when the supply of air is once regulated, it can be employed in the exact proportion to produce the maximum result. This is an important argument in favour of gaseous fuel. Then in •us fuel we have already a product of manufacture, and we have it free of ashes, and those drawbacks which attach to solid fuel, making disturbance and dirt not only in the atmosphere, but in works or dwellings where it is employed. Again, by the use of gaseous fuel, labour is saved to a very great extent. We have not to cany coal, but the fuel is supplied through tubes to the place where it is used, and the labour of producing the gas being concentrated labour, involves very much less expense than it would if solid fuel had to be dealt with. Lastly, gaseous fuel admits of the attainment of results such as cannot possibly be produced with solid fuel. You can heat gas to any degree almost within ordinary furnace temperatures before it enters into combustion, and I have shown by means of furnaces which I have been constructing for the last twenty years, that air can be heated to a very high temperature before entering into combustion with gas, and there is thus produced a compound, regenerative, cumulative action, which enables us to obtain by means of gaseous fuel the highest temperature which can be attained by combustion at all. You are all aware that the temperature attainable by combustion is limited by the point of dissociation, as Bunsen and St. Claire Deville have shown in their beautiful researches. I may mention that in applying a gas furnace for the fusion of steel on the open hearth, the point of dissociation is practically very nearly attained. Although this furnace is sufficiently well known by this time, I may just shortly refer to its leading details. It comprises si gas-producer which is presented in a somewhat novel form ; I shall refer to it again presently. The furnace itself consists of a furnace bed, and of brick chambers filled with refractory material piled up loosely so us to admit the circulation of air or gas through the same ; gas N 2 l8o THE SCIENTIFIC PAPERS OF from the gas-producer is directed upwards through one of these chambers, and cold air is directed upwards through the adjoining chamber. Both air and gas meet at the entrance of the combus- tion chamber, and if the brickwork contained in the two chambers is heated by any process, the air and gas flowing through it will also be heated to very nearly the temperature of the materials which impart that heat. They will therefore meet in combustion at a high platform, so to speak. If the temperature of the brick- work be at the upper surface, say 1000°, the air and gas will be heated practically to 1000° before they combine, and the result of that combustion must be a temperature of at least 1000° higher than it would have been if the gas had not been so heated. The products of combustion flow away at the other side through pas- sages, every alternate passage leading into one or other of the two remaining chambers, and in flowing downwards over the surfaces of the brickwork they impart heat to those surfaces, raising their upper layers to nearly the temperature of the products of combus- tion, which after depositing their heat, reach the chimney compara- tively cool. By reversing the direction of the gases, say every hour, or every half-hour, as the case may be, and admitting gas fuel at the place where one portion of the products of combustion left, and air at the point where the other portion of the products of combustion left, the currents of coal gas and air will pick up, so to speak, the heat which was kept there in deposit, and reach the point where they enter into combustion heated to a higher degree by another 1000° ; and the consequence of this combustion will be the attainment of a still higher degree of heat than was obtained in the previous operation ; and so on, and on, until either there is an equilibrium produced by the fusion of the materials to be heated, at which point, of course, the excess of heat will be absorbed in work done, or it will go on accumulating until com- bustion itself will cease. Such a point will be reached at about 2500° Cent., the temperature of dissociation, and in heating one of these furnaces up to the highest point which it would be safe to attain in them, the flame, which at one portion of the operation is a short white flame, becomes gradually extended into a long attenuated flame of somewhat bluish appearance, clearly showing that combustion is earned on under great difficulties. For any temperature exceeding these limits we should have to resort to S/fi WILLIAM SIEMENS,, F.R.S. l8l difU'ivnt means altogether, such as the electric arc, because com- bustion, however carried on, would not give us a higher tempera- ture, even if we found materials that would resist the heat. These, thru, are some of the advantages which may be claimed in favour of gaseous fuel. Fuel may be dealt with in two ways in order to produce gaseous fuel ; it may be placed in a retort, and the retort heated by the external application of heat in order to drive out the volatile con- st .imciits. This is the process, as you are aware, generally followed in gas-works. The use of gas for illuminating purposes dates from the end of the last century. It was in the year 1792 that Murdoch, of Soho, erected his gas- retort. After him Lampadius published, in 1801, his investigation, very crude according to our present ideas, on the subject of gas, and gas illumination, but it was not until 1815 that gas illumination came to be practically used, and it was applied first of all, I believe, in London. This mode of producing gas by heating a retort, gives rise to two prin- cipal products, the gas or gaseous fuel, and the residue, the car- bonaceous matter, or coke. Both these constituents are very suitable for heating purposes. Coke has this advantage over raw coal, that it burns without developing smoke, and it is, therefore, applicable for many purposes where this rapid development, or change of the solid fuel into gaseous constituents, would absolutely impede the operations to be performed, such as blast furnaces, or locomotive engines. The gaseous fuel produced in the retort is also applicable for heating purposes, but has hitherto been used chiefly as an illuminating agent. I shall presently refer to the working of a gas retort, with a view of showing that, although we treat the gas coming from the retort as illuminating gas, as an entity, it really consists of many constituents, and that the quality of the mixture of gas coming from such a retort at one portion of the process is very different from that which comes from it at other portions. If the purpose before us is the heating of a fur- nace, and our object is to obtain from the solid coal as much gaseous fuel as possible, then it would not be desirable to have resort to a retort. The retort process is a slow one, and the coke produced, although it can be used also as fuel, would be undesirable at works where no such fuel is required, where the only object is to heat furnaces for melting glass, for making steel, for heating 1 82 THE SCIENTIFIC PAPERS OF iron, or whatever it may be. For such purposes the whole of the solid coal ought to be converted into gaseous fuel, and that has been accomplished for many years. It is accomplished in the blast furnace, where the combustion of coke under the influence of an insufficient amount of blast gives rise to a product at the top, consisting, in a great measure, of carbonic oxide gas mixed with a large proportion of nitrogen, which necessarily comes in with the air at the bottom. It is due chiefly to Mr. Ebelmen, a French physicist of some distinction, that attention was called to these gases in the early part of the century, but no practical application was made of gas for a number of years, nor were the gases coming from the blast furnace practically utilized until within the last twenty-five years. In the year 1861, I, in connection with my brother Frederick, succeeded in the construction of a regenerative gas furnace in which gas is used resulting from the total destructive distillation of coal, and I now wish to place before you an apparatus of an improved character for effecting that purpose. The gas-producer which we have hitherto used was effective, so far as it goes, in producing a combustible gas, but it did not fulfil all the conditions necessary to produce this chemical operation to the best advan- tage. One of the essential conditions for the total conversion of coal into combustible gas is a maximum degree of heat at one portion of the process. Where air enters, or is forced into a mass of incandescent fuel, the temperature of that fuel is raised, and the result of perfect combustion is carbonic acid. In order to produce carbonic oxide, which is the gas fuel producible from the carbonaceous constituent of the coal, it is absolutely necessary that carbonic acid, or the result of perfect combustion, should be produced in the first instance, and only by passing this intensely heated carbonic acid over an additional mass of incandescent carbon will it take up another constituent of carbon, and con- stitute itself carbonic oxide ; unless the temperature is high enough, this reconversion, or backward conversion from carbonic acid into carbonic oxide, will be effected only partially and imperfectly. The apparatus, Plate 33, which I have lately tried, and which pro- mises to be a great improvement on the former arrangement, consists of a cylindrical chamber truncated towards the bottom, which is WILLIAM SIEMENS, F.R.S. 183 filled with coal through a large hopper at the top ; this iron casing is covered on the interior with a lining of refractory material, and in this lining passages are arranged all round for the exit of the ; a large opening at the bottom admits of the removal of ashes and clinkers that may be formed in the combustion of the fuel, and a blast, which by preference should be heated, is directed riirlit into the very heart of the mass of fuel. The result is a very high temperature in the centre of the mass, and no heat is lost at that point, which loss would interfere with the due conversion back into carbonic oxide. At the same time, water, which is admitted by a continual streamlet into a pan near the bottom, is evaporated, and currents of steam are directed or drawn into the apparatus, passing through the zone of highest temperature towards the centre of the mass. They there become converted by contact with the incandescent fuel into carbonic oxide, and hydrogen gas, which add greatly to the calorific effect of the gas produced. Much has been said of late years of water-gas, and one has sn 'ii statements in the papers calling attention to the enormous store of fuel we possess in the ocean ; but a very little considera- tion will show the utter fallacy of such a proposition, as getting actual heat energy from water, which is already the product of complete combustion. Water can only usefully assist in the operation of gas production if you have spare heat to expend. If in the gas-producer no water at all were admitted, you would obtain a current of carbonic oxide, mixed with the other products of distillation of the raw fuel that enters the apparatus ; and the heat that would result from this combustion, even after a portion of it had been expended in the backward reconversion of the carbonic acid into carbonic oxide, and in the work of distillation of the raw coal into hydro-carbons, would be sufficient to impart to the gas at the point of exit a temperature of about 1,000° F., or a little more. This heat must be considered as a loss, because if the gas had to be carried to any reasonable distance, this free heat would be dispersed before it reached the furnace, and it is with the view of utilising this heat, which would other- wise be lost, that water can be had recourse to advantageously. But it must be administered in judicious proportions. If too much water is admitted the chemical action which is intended to 1 84 . THE SCIENTIFIC PAPERS OF be carried into effect in the gas-producer would cease, and the temperature would never attain the degree necessary to convert carbonic acid back into carbonic oxide. There would result a poor vapoury gas, which on analysis would show a very large proportion of carbonic acid still present, and probably free oxygen, which never had combined at all. This is a point to which I have wished particularly to call the attention of this Society (which has for its object to combine strictly scientific investigation with its practical applications), viz., the degree to which water can be advantageously used for effecting this decom- position, and its re-combustion. When this process is properly conducted in the old form of producer, the result of the total combustion is a gas of moderate temperature, perhaps 400° F., found on analysis to contain of carbonic oxide 24 per cent., hydrogen 8 per cent., carburetted hydrogen 2 per cent., carbonic acid 4 per cent., nitrogen 61 per cent. ; whereas in a well-organised gas-producer of the new form, the proportions of hydrogen and carbonic oxide could be materially increased, and the amount of nitrogen diminished proportionately. I may also mention with regard to this form of producer, that the earthy constituents of the coal are fused, or brought into a semi- fused condition, and are carried down in that condition by the weight of the fuel itself ; the object being to produce this semi- fused mass of clinkers within the mass of the fuel without giving them the opportunity of attaching themselves to the furnace, and thus to save labour. Another matter I wish to call attention to is the supply of gas that can be carried to a distance. After all, gas produced by total distillation in the gas-producer can only serve at works where it can be used at once, but for the multifarious purposes of daily life, for small works, and for domestic purposes where heating gas will become from day to day used to a larger extent, there it is necessary to send through pipes a gas of a much richer character than that coming from a gas-producer. It must be a pure combustible gas, such as marsh gas, or hydro-carbons, or hydrogen. This may be produced in retorts of the ordinary kind, or, as I proposed eighteen •years ago, when I suggested the supply of heating gas to the Town Council of Birmingham, by the use of large vertical retorts heated by a regenerative furnace, and furnished with a supply of SIR WILLIAM SIEMENS, F.K.S. 185 water at the lower extremity, in order to get a very active distilla- tinn, irrespective of the illuminating quality of the gas produced. P.iu the (lill'uulty which presented itself was one rather of estab- lishment. It was proposed to build works simply for the purpose of supplying heating gas ; and although the Town Council of Birmingham went to Parliament for a Bill to empower them to carry out this suggestion, they lost their Bill in the Committee of tin ilouse of Lords. Since then the public desire for the use of heating gas has been gradually increasing, and another mode of supplying it has suggested itself to me. It may have been thought of by others, and it is one that recommends itself, I think, by its simplicity to your consideration. It consists in separating the produce of the distillation of coal in the gas retorts into two parts : one to be set aside for heating, and the other for illuminating pur- poses. The result of such a separation is illustrated by the diagram, Plate :;i, which is based on some experiments made many years ago by M. Ellissen, the Chemist of the Paris Gas Works, working in connection with M. Regnault, the great physicist. They wanted to determine by accurate observation and experiment what was the least time to be allowed for each distillation. Instead of carrying on the operation through six hours, they came to the conclusion that it should be hastened, and completed in four hours, and for this purpose the Paris Gas Works first adopted the regenerative gas furnace as a means of heating retorts, and they have used it very largely ever since. Through the kindness of M. Ellissen I have been able to construct this diagram, showing the quantity and the illuminating quality of the gas leaving the retorts at each portion of the four hours during which the opera- tion is carried on. The cross line shows the illuminating power of the gas at the different portions. The abscissae give the time, and each line represents a quarter of an hour, and the ordinates give the illuminating power on the curve and the quantity on the other curve. The diagram shows at once that during the first twenty-five minutes or half-an-hour, the gas coming from the retorts has a very low illuminating power. They are chiefly occluded gases, consisting in a great measure of marsh gas. At the end of the first half-hour, the maximum illuminating power is reached, and for about an hour and a half this high illuminating power is pretty wrell maintained. It then gradually diminishes, 1 86 THE SCIENTIFIC PAPERS OF until at the end of the fourth hour it is less than half what it was at the earlier portion of the process. Now, if the gas produced in the retort could be directed by a simple reversing valve into one main or the other the illuminating power would rise from 18| to 18 caudle-power, and produce thus all the advantages which the public now desire, a gas of increased illuminating power ; whereas the heating gas constituting the other half, or even two-thirds, of the total produce, would be all the better qualified for heating purposes than the gas which is now sent into our mains. It is well known that marsh gas produces a higher calorific effect weight for weight than olefiant gas. Therefore, if the marsh gas, and the hydrogen, which has still higher calorific power, could be supplied separately, we should get a better illuminating gas, and a better heating gas. It may be objected that this would involve the laying down of a separate set of mains ; but in answer to that, I contend that in many towns we have already two sets of mains, because at one time or another we have had opposing Gas Companies, each with their set of mains ; but even if they do not exist, the question of the supply of heating gas is such a large one, that the laying down of additional mains should not stand in the way. If gas heating is to come into general use, we shall soon require perhaps three or four times the amount of gas which can possibly be supplied through the existing mains. If at the same time such a great advantage can be realised as the production of a gas of a higher illuminating power, and with it a heating gas at lower cost, we should have an advantage every way. But with regard to the question of cost, of course, the public would be willing to pay a somewhat increased price for a gas of 40 or 50 per cent, increased illuminating power, whilst the heating gas, on the other hand, would not require the same amount of care and expense in purifying as is necessary for illuminating gas. Then for this Society the question has another important aspect. If by the supply of heating gas the total consumption can be vastly increased the bye-products would be increased in the same pro- portion, and these bye-products have now attained an im- portance only second to that of the value of the gas itself. Therefore, if by the carrying out of such a plan the total pro- duction of gas can be very greatly increased, an impulse would .S7A' WILUAM SIEMENS, F.R.S. 1 87 ivi'ii to chemical manufactures such us I need not specify i,* ihis Society. There are other questions which I should like to have touched upon, regarding certain applications of heating gas, and certain UB of intensifying illuminating gas, so as to bring it more niMi-ly up to the standard of brilliancy of its great rival, the electric light ; but this would, I fear, be travelling outside my subject, which was to bring before, the Society the question of gas as a lieu ting agent. Tin I 'resident (Professor Koscoe) : We have all listened with interest to this suggestive communication which Dr. Siemens has made to the Society. 1 feel sure that it is a subject in which every one takes an interest, and it has been treated in his masterly manner. I am sure it will not fail to please all the members who are present. The suggestions he makes are certainly bold enough, and let us hope they may receive that attention from corporations, and from the gas companies, which their importance and the originality of the suggestions warrant. I am sure all the members of the Society would wish to hear, if Dr. Siemens will consent to give us in a few words, the mode of application, which 1 see from some models he has here, he has already thought out. I think it does form a very important part of his communication — the method in which lie proposes to use the gases of low illuminating power for heating purposes, and with your consent, gentlemen, I would ask him to give us an account of the method which he proposes to employ before we begin the discussion. Dr. Siemens : I did not wish to extend my subject too much, but willingly comply with the desire expressed by the President, and will describe shortly two applications, one of heating gas, and the other of illuminating gas, I have had occasion to make lately, ;ui(l which have given very encouraging results. In using gaseous fuel in an ordinary h're-place, it becomes necessary to introduce some substance which shall become incandescent in order to radiate the heat into the apartment. We have substance of this t description in use in the ordinary gas-grates, such as pumice- stone, or other purely refractory material, but coke or anthracite naturally suggests itself also as a suitable substance for taking up heat and radiating it out ; it joins in the incandescence, and 1 88 THE SCIENTIFIC PAPERS OF through its owii slow combustion aids the gas, which per s& is at the present time at all events the more expensive fuel. If gas could be supplied at Is. a thousand feet, it would no longer be more expensive than coal, and the time will come, I believe, when we shall have good heating gas supplied to us at that price. Wherever gas fuel is used, there ought to be some means of accumulating the effect of heat — some mode of regeneration, and the question occupied my mind in my leisure hours, how could the regenerative principle be applied to an ordinary open fire-grate ? After some time the idea occurred to me, that in taking advantage of the conducting power for heat of some metals, I might be able to pick up heat at the back of the fire-grate, and bring it down to a system of surfaces below the fire-grate, in order there to communicate it to currents of air supporting combustion in front of the grate. Such an action is carried out in the grate of which I have a model here, Plate 35. It has the ordinary fire-bars, to the bottom- most one of which an inclined plate is attached, but instead of the ordinary horizontal grate, an angular casting of iron with ribs projecting from its lower surface supports the fuel. In front of this casting, and behind the lower grate-bar, a gas-pipe is fixed, having a limited number, (from 8 to 12) of gas orifices, of about one-sixteenth of an inch diameter. The gas issuing from these openings towards the back of the pipe, gives rise to flames percola- ting through the coke oranthracite, or other similar substances which fill the grate. Each gas flame in percolating up through the coke produces very much the appearance of an ordinary coal fire in its best condition, and the coke in front of the grate soon becomes incandescent, giving out a very considerable amount of radiant heat. When this point has been reached, the gas may be nearly altogether turned off, as the glow of heat will be maintained almost entirely by the hot air currents which by this time set in, and produce intense combustion in front of the grate. I have, I think, fourteen such grates in my office and house, including all the principal rooms, and I have succeeded gradually in winning the lady portion of the household over in favour of the improvement. At first they said it was a dead fire, and you could not poke it, but gradually even the housemaids, who at first thought it was an abomination, have come round. They see that it gives them less S/A' WILLIAM SIEMENS, F.R.S. 189 t n>u I ile ; that in lighting it is very agreeable to turn the gas on or off as needful, and to be able to keep up the fire for half a day without touching it. Many friends when they have come into the room have said, "What a magnificent fire." The cost also I have been able to ascertain by this time. For tin- first quarter of the present year, in the five large grates, including the drawing-room, my own study, and the dining-room, where a fire is maintained nearly the whole day, the consumption of gas amounted per grate to 6,HOO cubic feet, being of the value of one guinea, or of one ton of coal when at its cheapest in London. I am quite sure I have saved more than a ton of coal in each grate, even after debiting myself with the consumption of coke, which amounts to about one-third the consumption of coal. Taking it all in all, it is a cheap fire, and certainly it is perfectly smokeless. I am glad to say that several of the leading grate- builders have taken up the construction of this grate, and I believe at this present moment there are several hundreds of them in actual use. I have adopted the same principle for intensifying the light of an ordinary argand gas-burner, Plate 35. Through the centre of the burner a stem of copper projects, which is bulged out cup-like, at its upper extremity, and is connected at its lower extremity with a cylindrical box of copper, of high conductive power. The cylindrical vessel is perforated all over, and round it ten layers of copper-wire gauze are wound. The bottom also is closed by ten discs of wire gauze. The burner is mounted in the ordinary w.ay with a glass chimney, but at the point of the flame the bulged portion of the rod, filled up with fire-clay, gathers up heat, and conducts it downwards to the wire gauze, whilst the current of air is drawn in by the flame itself, and is heated in its transit through the wire gauze, to a temperature of from about 500° to 700° Fahr. By this simple arrangement the intensity of the gas flame can be very nearly doubled. In fact, according to one experiment, it was rather more than doubled, measured photometrically ; and at the same time a flame of much whiter character is obtained. TJie President: Do you remember what is the illuminating power of such a burner ? Dr. Siemens : In using ordinary gas we get from this burner 190 THE SCIENTIFIC PAPERS OP about 25 candles. I should mention that my brother, Frederick Siemens, has worked independently on this same subject, and pro- duced a burner which has been tried lately by some of the gas authorities, and has given an economy superior even to what I have stated. But the construction of my brother's burner is essentially different, the gas flame being drawn downward through heating apparatus. The President : Like Faraday's ? Faraday arranged gas-burners of that kind. Dr. Siemens : I am not acquainted with Faraday's arrangement, but although my brother has obtained very excellent results, I think that the. plan I described is certainly a more simple arrange- ment, and for ordinary applications commends itself on that account. I should have mentioned that, in order to prevent the oxidation of the copper conductor, and also in order to have a reflecting surface, I have covered the copper conductor with a very thin coating of enamel or platinum. In 1he discussion of the Paper "ON THE COMBINATION SYSTEM OF STEAM HEATING FOR TOWNS AND VILLAGES," By CAPT. DOUGLAS GALTON, The CHAIBJIAN (DE. C. W. SIEMENS),* in proposing a vote of thanks to Capt. Douglas Galton, said this question was not a new one in the abstract, for heating by steam had been carried out to his knowledge forty years ago. But there was a novelty in the proposal to generate steam in large volumes, at high pressure, at certain centres ; and to send it at that high pressure for miles under the streets. It was also perhaps a novelty to divide steam by regulating and stopping valves, and supply it to individual * Excerpt Journal of the Society of Arts, Vol. XXX. 1881-1882, pp. 93-94. WILLIAM SIEMENS, F.R.S. 191 houses, so that it might be used for tho various purposes men- tiuiu-d. The great question which presented itself was, would such a pipe be trustworthy ; could it be laid and maintained for this purpose without danger and without trouble. The paper described an elaborate method of insulating the pipe to prevent Mve loss by radiation, and from the figures given it seemed to have been very successful ; but it appeared to him doubtful whether, in our streets, a pipe so swelled out by insulators, and logs of wood, and planks, could be laid. The space below our streets was already so fully occupied, that the establishment of such pipes would present very great difficulties. As Sir Frederick Brain well remarked, if ,^hey wanted to bring heat into houses, there was another means already established, and in full opera- tion ; and from a little calculation he had just made, he found that a cubic foot of coal-gas brought with it about 750 heat units, which would be about the same amount as would be supplied by 8j cubic feet of steam, at a pressure of 6 atmospheres. The ques- tion, therefore, would reduce itself to this, whether the one pipe or the other could be maintained with the least expense. He, for one, must adhere, for the present, to the opinion that it would be easier to supply gas than steam. The paper spoke of various modes in which steam heat could be used, and the radiator was alluded to, but he did not think that apparatus was very happily named. A steam-heated surface in a room no doubt radiated heat, but not under the same conditions as a fire-place. Probably, nine- tenths of the heat given off from that hot surface would be given off to circulating currents of air, which would pass again and again through this radiator, and a very small portion would pass by radiation into the room. The rays from such a low source of heat would hardly be felt, as radiant heat, at any sensible distance from the source. Now, he looked upon an open fire-place not only as a thing endeared to them by long habit, but he attributed to it very high sanitary qualities. The open fire-place communicated absolutely no heat to the air of the room, because air being a per- fectly transparent medium, the rays of heat passed clean through it. It gave heat only by heating the walls, ceiling, and furniture ; and here was the great advantage of the open fire. If the air in the room were hotter than the walls, condensation would take place on them, and mildew and fermentation of various kinds 192 THE SCIENTIFIC PAPERS OF would be engendered ; whereas if the air were cooler than the walls, the latter must be absolutely dry. That was the great advantage of the open fire, and it endeared it to them, though many did not know exactly where and how the comfort arose. The Americans were very ingenious, but he would not take their word with regard to the comfort of their rooms ; when he was there he suffered severely from the closeness of the atmosphere of the dwellings, and when he travelled at night in the sleeping-cars he was obliged to get up four or five times and step out on the foot-board to get thoroughly cool. The only explanation he could offer was that the attendants were black men, whose standard seemed to be the interior of Africa. But although he could not agree absolutely with the proposal, yet the question of doing away with the smoke and nuisance which now resulted from open fire-places was so important, that any suggestion, backed by a considerable amount of experience was welcome ; and Captain Galton well deserved their thanks for the able manner in which he had brought the subject forward. In the discussion of the Paper "ON AIR REFRIGERATING MACHINERY AND ITS APPLICATIONS," By JOSEPH JAMES COLEMAN, F.I.C., F.C.S., &c., DR. SIEMENS * said the question that had been brought before the Institution was one of considerable engineering and public importance, and he was glad to see it brought forward in such a clear and efficient manner. The subject was not one of recent date, but had occupied the minds of many men for a considerable number of years. The author had been good enough to mention his name in connection with a proposal which he had made twenty - * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Vol. LXVIII. 1882, pp. 176-186. ir/I./.fAM X/EMENS, F.R.S. 193 five years ago to the effect of superadding to the simple play of .so jiu nips — the compressing and the re-expanding pump — an intercli;ui'_ror of temperature. That suggestion, as it presented to him, was published only in a provisional specification of a patent which had never been specified finally ; but more thiiii that had been accomplished, and perhaps it might interest the members to know exactly what had been done. Dr. Gorrie, an American, had patented and brought to England a certain scheme, which had been taken up by Mr. Wollastou Blake and a fr\\ other gentlemen in London, who erected plant which was perfect in all its details. The engine had a 25-inch cylinder and 5 feet stroke ; the compressing and re-expanding pumps were made by James Watt & Co., and had been erected somewhere in the north of London ; but when it came to be tried it was impossible to get a depression of temperature exceeding 20° Fahrenheit. That being the case, after several ineffectual attempts to improve the result, he was asked to examine the machine and report to the proprietors. He had lost sight of the report, but Mr. Wollaston Blake had sent him a copy with the drawings, and suggestions which ho had made for improving the efficiency of the engine, and lese would be appended to his remarks (see p. 195 et seq.~) The eport was of some interest, as it went very fully into the principles underlying the question of refrigeration, and the causes of the ion-realisation of those results which should have been effected. It seemed curious that, from the & priori examination and calcula- tions which he made, he had come to the conclusion that the jmperature could not be depressed more than 20° by the machine, that when that reduction of temperature was reached the loss of affect would exactly balance the beneficial result; and the actual trial jrroborated that statement. The author had. perhaps, hardly given lira credit for the labour which he had spent upon the subject. He id not only devised the temperature interchanges, which was the most essential feature in the whole process, and without which no ufficient results could be obtained, but he had fully recognised the antagonistic effect of aqueous vapour in the air dealt with. "he loss of effect " by throttled passages " he had given at LO'08 HP. That required some explanation. Dr. Gorrie evidently wished to avail himself of the expansive force of the compressed and cooled gases before they were discharged ag lin ; but he did VOL. i. o IQ4 THE SCIENTIFIC PAPERS OF not conceive that the whole effect of the machine depended upon the heat (utilized negatively) in that final expansion ; and in order to be sure, as he thought, doling out as it were the com- pressed air to the expanding cylinder, he introduced a throttle- valve into the compressed and cooled air ; and instructions were given to wiredraw that valve as much as possible on the sup- position that after all the safe plan of gaining refrigeration would be to expand air through the throttle-valve, that was through a contracted orifice. Dr. Siemens showed that contraction was the worst thing that could happen — that by merely expanding air without exacting work from it, no depression of temperature would ensue. By friction and useless agitation of the fluid, the loss was 3 HP., by condensation of vapour, TOO HP. That, of course, was a fruitful source of loss. If the air was compressed and then not sufficiently refrigerated, the vapour which it con* tained would, on re-expansion and final cooling in the expansive cylinder, not only condense, but be converted into ice. The vapour which went in as steam would come out as ice, and the whole of the latent heat taken up in that double process of con- version was entirely lost. That loss in some of the earlier attempts was fully equal to the whole useful effects that could be expected. But the greatest loss of all was incurred in allowing the cold air to leave the apparatus at the minimum temperature. Dr. Siemens suggested that a current exchanger should be supplied ; that the cold air, after it had done its negative work, so to speak, should pass up through spaces surrounding a number of vertical tubes, and that the compressed air should pass through the tubes themselves in the opposite direction, and exchange temperatures. In that way 1\ HP. could be saved. It was shown in the report that a very economical result might be obtained by observing these precautions. Attached to the report were diagrams taken from the three cylinders, and a sketch showing the kind of apparatus which was then proposed, and which, he thought, in all material points was similar to the machine brought before the members by the author of the paper. There was, however, one point in which he still dissented from the knowledge and experience of the present day. He had stated in the report that as ice-making was really negative work, there could be no absolute limit to the effect to be produced by heat in that direction. It was true that SfK WJLLIAAf SIE.\fENS, F.R.S. 195 great men like Dr. Clausius, Sir William Thomson, and Dr. Joule, had established a certain equivalent, an equivalent which was perfectly true if the heat generated in the mechanical process of t-< impression were treated as waste. But by means of the re- trciit-rator it was possible to recover, at any rate, a large proportion df the heat so produced at the minimum temperature attained in run pressing the air. The ice produced was, therefore, only i-viilcnce of a transfer of heat from the fresh water to air or water raised to a high temperature. And in this respect the operation of freezing differed very essentially from that of power-producing, when a given amount of heat must absolutely disappear. The report might perhaps be interesting, as it gave the particulars of the views which he then entertained, and of the theoretical conclusion at which he arrived — a conclusion which, he had little doubt, though it was not now fully admitted, would be admitted before the subject was done with. The paper dealt with the question as it stood at the present day in a very able and proper manner, and the applications which would flow from a cheap and ready mode of lucing temperature to any desirable point could not be easily overrated. tBPORT OX THE PERFORMANCE OF NEWTON'S PATENT REFRIGE- RATING APPARATUS, WITH SUGGESTIONS FOR IMPROVING THE SAME. Having examined your apparatus for the artificial production of ; on your premises at Camden Town on the 8th inst, and having examined carefully into the principles involved, and into the rases of its present lack of success, I have to report thereon as allows : — " Description. — The apparatus consists of a horizontal condens- ing steam-engine of 32 inches diameter of cylinder, of 5 feet Bngth of stroke, in excellent condition, by Messrs. James Watt id Co., which imparts motion to a crank-shaft with two Iditional cranks, which are connected with the pistons of two air cylinders of 4 feet 6 inches stroke, and of 21 inches and 19 inches diameter respectively. The piston rods of the air cylinders are carried horizontally through the cylinder bottoms, and are each of o 2 196 THE SCIENTIFIC PAPERS OF them attached to a second piston 4 inches in diameter, working in the barrels of double-acting pumps, which inject at each stroke their fluid contents into one extremity and the other of their respective air cylinders. The larger air cylinder (of 21 inches diameter) compresses atmospheric air into an upright receiver, where it is allowed to separate from the injected water, the water issuing from the bottom through a ball-tap, and the comparatively dry air proceeding through a pipe leading from the tap into a larger horizontal receiver or reservoir, which is provided with a mercurial pressure-gauge indicating 55 Ibs. effective pressure per square inch when the apparatus is at work. "A copper pipe (of 3 inches diameter, and provided with a stop- valve) leads from the receiver to the second air cylinder of 19 inches diameter, wherein the compressed and cooled air is allowed to expand again down to atmospheric pressure, and being mixed in the expanding cylinder with a spray of injected brine (by means of the second injection pump) it is expelled into a large cistern containing about 500 gallons of brine. The injected brine here subsides, and the expanded air escapes freely into the atmo- sphere. It appears from records of experiments made on the 28th and 29th of April, and on the 13th of May last, that the water injected into the compressing cylinder was raised uniformly from 2^° to 3° Fahr. in temperature, whereas the brine in the cistern (500 gallons) fell gradually in temperature from 2° to 3° per hour at first, but diminishing gradually, as the temperature descended gradu- ally below that of the atmosphere, until it reached the temperature of 18'5°, which appears to be the lowest degree ever attained. The speed of the main shaft was, during the first-named experiment, twenty revolutions per minute, when the injected water was raised 3°, and the brine in the cistern reduced only 2° per hour at the commencement of operations, and during the second experiment the speed varied from fourteen to sixteen revolutions per minute, when the injection water was raised only 2^°, whereas the brine in the cistern was lowered 3° Fahr. per hour, until it descended corre- spondingly below atmospheric temperature. The water to be frozen had been filled into cans of copper and dipped into the brine, after the greatest depression of temperature had been attained, which caused a rise of temperature from 18'5° to 22° or 23°. .V7A' \V1LUAM SIEMENS, F.R.S. 197 " When I examined the apparatus I found the speed to average fifteen revolutions per minute, and the following are the mean ;tvs and horse-power indicated upon the three cylinders, viz.: — MEAN HORSE PBESSUBE. POWER. The steam cylinder according to data obtained from Mr. Blake . . 8'8 Ibs. 32 Comiiressing cylinder . . . . 26'75 „ 37'85 Expanding cylinder with injection . 18*25 ., 2T1 Kxpanding cylinder without injec- tion 14-22 „ 16-5 " Theory. — Before entering into a consideration of the merits and defects of the apparatus in its actual condition, it will be of advantage to establish generally the principles whereon its effect depends. The heat which it is purposed to abstract from the water is communicated to expanding air, or, in the language of modern science, is converted into mechanical effect, and it can be proved philosophically that a caloric engine may be devised which derives its power from the latent heat of water in causing it to congeal. In fact, the heat communicated by the injected solution to the expanding air is a source of power to the machine, which would yield both effective power and ice but for the compressing cylinder, which in the arrangement described has to be worked by an engine. The power expended in compressing the air produces, however, its equivalent of heat, which heat would be sufficient, in a philosophically perfect arrangement, to reproduce the power necessarily expended by the engine, and a surplus of effective power proportionate to the heat abstracted from the water would be realised. " This view of the principle involved in your machine is novel, I believe, and somewhat startling ; but I am confident it will be acquiesced in by those conversant with the dynamic theory of heat, and although the conditions of the ideal machine will probably never be realised, it is important for our purpose to know that the production of ice does not necessarily involve an expenditure of power. " Starting, then, with the admission that the heat produced in 198 THE SCIENTIFIC PAPERS OF the compressing cylinder is practically unavoidable, the question arises, — how great is the necessary expenditure of engine-power, or, in other words, the difference between the power absorbed in the compressing cylinder and the power obtained in the expanding cylinder ? The difference of power arises in consequence of the abstraction of heat from the compressed air, and is directly pro- portionate to the number of degrees of heat abstracted or generated in compression and afterwards lost in expansion. The quantity of heat lost in the expanding cylinder is, however, proportionate to the power produced in expansion, and is entirely independent of the limits of expansion which, as has just been shown, determines the degree or quality of cold produced. It follows that low rates of compression and expansion of the air are favourable to the production of cold with the least expenditure of engine-power, and I find by calculation that the power value of a given amount of heat abstracted (or cold produced) increases in the ratios of the squares of the number of degrees of reduction of temperature, re- quired. " It is therefore highly advantageous to compress and expand large volumes of air to a moderate extent, consistent with the requisite energy of action of the machine. "Adhering for the present to the rate of compression obtained in working your apparatus, namely 55 Ibs. per square inch effective pressure, the following result might be obtained if no incidental losses of any kind were obtained, and taking the speed at 15 revo- lutions per minute. H.P. indicated in compressing cylinder „ ,, expanding cylinder engine .... Units of heat produced in compression minute ....... Injection water raised in compression cylinder Units of heat produced in expansion Ice produced per hour from water of 60° 600 gallons of water cooled per hour The diameter of expanding cylinder Lo be . per 35-0 25-2 9'8 1,500 2-5° 10-80 381 Ibs. 10-8° 17| ins. In comparing these results with those actually obtained, it will SIR WILLIAM SIEMENS, F.R.S. 199 be observed tho compressing cylinder did its work remarkably well, whereas the duty obtained from the expanding cylinder falls manifestly short of the results indicated by theory. It was necessary then to inquire carefully into the causes operating a.u'ainst the performance of the expanding or freezing apparatus, and the following are the results of that enquiry : — " 1. The power developed in the expanding cylinder should be •_'.")•!' H.P., whereas only 16*5 H.P. was actually indicated (when no solution was injected) owing to — "a. A great loss of pressure between the cylinder and the receiver. " b. Excessive expansion beneath the atmospheric line, which involves a loss of power on the return stroke. " c. Imperfect adjustment of the admission valves. "2. When solution was injected the indicated power rose to 21*15 H.P., or G'93 H.P. higher than before, which excess of power may to a great extent be fictitious, being caused by the penetration of the solution into the indicator, but it proves that considerable force must be expended in forcing and agitating the solution, and all the power so spent will produce its equivalent of heat and must be deducted, besides the power lost in friction of piston, from the indicated 16'5 H.P. in estimating the refrigerating effect to be produced. " 3. The compressed air being cooled by injection of cold water, it will certainly be saturated with vapour, which vapour will be condensed and converted into ice during expansion, and produce a white fog pervading the expanded air. " The quantity of vapour so condensed and congealed, supposing the temperature of the compressed air in the reservoir to be 68° Fahrenheit, amounts to O'OG Ib. per minute, yielding about 1330 units of heat, which represents a loss = 1'9 H.P. " 4. The expanded air leaves the apparatus at the temperature of the cistern, or say at 20°, which is 6 8° -20° = 48° below the temperature at which it entered the compressing cylinder, which represents a loss of effect = 312 units = 7'25 H.P. at least. " 5. The cistern containing the solution, the expanding cylinder, the pump and the connecting pipes, present an aggregate surface 200 THE SCIENTIFIC -PAPERS OF of about 200 superficial feet of heat-absorbing surface 6 5° -20° = 45° cooler than the surrounding atmosphere on an ordinary summer's day. The machinery especially being ill-protected, and of a dark colour, I estimate the loss of effect from this source at about 3'6 H.P., assuming that the covering prevents two-thirds of the radiation which would take place if the surface were unpro- tected. Assuming that the solution in the cylinder has been reduced to 20° Fahrenheit, the total losses are as follows : — By throttled passages, &c. ,, agitation and friction ,, condensation of vapour ,, cold air leaving cistern . ., absorption of heat from the atmo- sphere see paragraph 1 2 say „ 3 4 H. P. 10-08 3-00 Total loss . Total power to be obtained 3-60 25-83 25-2 It follows that when the temperature of the cistern is reduced to 20°, the losses of cold produced equal or actually exceed the power of the apparatus of producing the same, which result is corroborated sufficiently well by the experience obtained, although it has been the result of independent calculation as regards para- graphs 1, 3 and 4, but only assumed as regards paragraphs 2 and 5, which, however, are the less important. " The next question is whether, and to what extent, these different sources of loss can be obviated ; and I will at once proceed to describe the fresh arrangements I propose for your adoption, and which are illustrated by the sketch shown on Plate 36. " The proposed expanding and freezing apparatus consist of a cylinder of cast iron of 17 inches diameter, instead of 19 inches, and 4 feet 6 inches stroke. The pipes and valves connected with this cylinder to have a sectional area of not less than 15 square inches (instead of 7 square inches), and no stop-valve to be introduced. The admission valves to cut off at one-fourth part of the stroke. The expanding cylinder is immersed in the cistern containing the freezing solution, and the expanded air issues from .s/A' WILLIAM SIEMENS, F.R.S. 2OI the cylinder into chambers a, a, forming the inner sides of the cistern, which chambers are perforated towards the bottom to allow the air to bubble through the solution. The cistern to be about 10 feet long, by 5 feet broad, by 2 feet 6 inches deep. The t \|i;itided air issues from the cistern into the atmosphere through a series of vertical tubes contained in a cylindrical air-tight chamber (C) through which the compressed air circulates on its way to the cylinder. The compressed air enters the annular chamber through a pipe &, and issues into the tube chamber (('), through a number of holes in order to distribute it uniformly. It then descends gradually, and effects an interchange of temperature with the expanded air within the tubes, which latter issues at the top at nearly the temperature of the compressed air on entering, whereas the compressed air reaches the expanding cylinder nearly at the temperature of the cold cistern, or below the freezing point. The annular chamber d, serves to collect the cold compressed air at the bottom, and to supply it to the admission valves e and /, by means of pipes not shown. The tube in the centre of the chamber C is of about 9 inches diameter, and contains a cylindrical vessel, g, filled with water, which enters the same from above, and is withdrawn at the bottom in a cooled condition to fill the former for the production of ice. The tube surface required is about 200 superficial feet. "The advantages obtained by this exchange of temperatures are very important. The compressed air is reduced below freezing point before it reaches the expanding cylinder, and the aqueous vapour it contained is at the same time condensed upon the tubes. Indeed the lower the temperature of the cistern descends, the more will the compressed air be reduced in temperature, and the cold produced will accumulate in intensity to any desired degree. Both injection pumps and one of the large air receivers will be dispensed with, for it makes no difference at what temperature the compressed air enters the exchanging apparatus. I should recommend, however, to retain the injection pump of the com- pressing cylinder till the efficacy of the new apparatus has been proved by experiment. "This new apparatus would reduce the different losses of refrigerating effect in the following proportions, according to my estimation, viz. : — 202 THE SCIENTIFIC PAPERS 01' Probable loss expressed in H.P. 1. By throttled air passages .... say 2 '5 2. „ agitation and friction of piston . . . . 1>5 3. „ condensation of vapour in expanding cylinder . O'o 4. ,, cold air escaping ....... 2'5 5. ,, heat absorbed by radiation .... 2*0 9-0 Gross power of expansion ... . . 25'2 Leaves effective refrigerating power . . .16*2 which is capable of producing 258 Ibs. of ice per hour. " The production of ice may, however, be increased 25 per cent, in working the apparatus at the rate of twenty revolutions per minute, which the increased passages, &c., admit of. It is hardly necessary to draw your attention to the gain of engine power which the proposed alterations are calculated to effect. In order to reduce the engine power required to its proper limit, I should propose considerable modifications in the general arrange- ment of the apparatus, consisting chiefly in attaching the three pistons upon one rod, in accelerating the speed of the pistons, and in compressing the air to only about 30 Ibs. per square inch. " COST. An apparatus so constructed would be considerably less complicated and costly than our present apparatus. The ex- panding cylinder might be made of cast iron, the two injection pumps and one air reservoir would be suppressed, and in their stead the comparatively cheap exchanger of temperatures or reciprocator be added. The engine and moving gear would, moreover, be greatly diminished. The proposed alterations in the existing apparatus would not cost above £200 (I consider), taking into account the value of materials of the present expanding cylinder and injection pumps. London, 28th July, 1857. Signed, C. W. SIEMENS. To WOLLASTON BLAKE, Esq., F.E.S. &c. Mr. David Thomson said he had been much interested in the paper, the theoretical part of which he thought was quite correct. Dr. Siemens had thrown some doubt upon the formula as given in S/A' ll'/LL/AM SIEMENS, J-'.N.S. 203 the paper, p. 147 ; Mr. Thomson had the honour of laying this formula before the Institution some years ago, when Mr. Kirk's paper mi the Mechanical Production of Cold was read and discussed. At that time Dr. Siemens mentioned that the formula was due to Clausius, but Mr. Thomson had deduced it from Rankine's works. Dr. Siemens observed that Clausius and Rankine worked independently and simultaneously at the same question, and arrived at the same conclusion. He did not doubt the correct- ness of the formula put forward by those eminent mathematicians find physicists, but he doubted its applicability under all con- ceivable circumstances to the question under consideration. In the discussion of the Paper "ON THE THEORY OF THE GAS-ENGINE," By DUGALD CLERK, DR. SIEMENS * said that one part of the paper dealt with matters regarding the mechanical arrangement of gas-engines, and the other with a theoretical question, that of the law of com- bustion. He would refer to the theoretical part first, because the author appeared to attach great importance to it, and as Dr. Siemens had from time to time given a great amount of con- sideration to the action of negative combustion or dissociation, it might be of some interest to the members to see how far his views fell in with those set forth by the author. It was well known that by combustion no unlimited degree of temperature could be attained. Thus, in a furnace worked at very high tem- perature the fuel was not completely burned when it came in contact with the oxygen of the heated or non-heated air. The moment a certain comparatively high temperature was reached * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Vol. LXIX. Session 1881-82, pp. 251-4. 204 THE SCIENTIFIC PAPERS OF the carbon refused to take up oxygen, or the hydrogen refused to take oxygen, and what had been called by Bunsen, and shortly after him, by St. Claire Deville, dissociation, arose. The point of dissociation was not a fixed one ; partial dissociation came into play at a comparatively low temperature, and went on increasing at a higher temperature in very much the same ratio as vapour density increased with temperature. Thus, if aqueous vapour were passed through a tube at a sufficient temperature the whole of the vapour would be dissociated, and the oxygen and the hydrogen would be separated. It was true if these gases were left to themselves they would, the moment the tem- perature lowered, again associate or burn ; but if precautions were taken to cool them rapidly after they had attained that high temperature they would be found as a mixture of oxygen and hydrogen simply. The author had stated that the law which governed these actions was not well known and required research, but Dr. Siemens would like to know whether he was aware of the researches of St. Claire Deville on the subject. It might be that the determinations of St. Claire Deville were not quite correct, but in the meantime they might be regarded as being so. He found that at atmospheric pressure the point of half dissociation of aqueous vapour arose at a temperature of 2,800° Centigrade, and that of complete dissociation at a much higher temperature. Taking that law as determined by the French philosopher, it did seem reasonable to suppose that when a mixture of hydrogen and oxygen, with or without a mixture of nitrogen, exploded, the point was reached beyond which the temperature did not increase, and, according to the author, that point was 1,500° Centigrade. If such a temperature was reached in the working cylinder complete combustion would not take place immediately, but only partial combustion would occur, which would go on as the temperature diminished by absorption into the cylinder or by expansion, and that combustion would be completed only in the course of the stroke. In that way the action which had been described with reference to the diagrams was reasonable enough. With regard to the mechanical arrangement of gas-engines, the author distin- guished between three types. In the first, the mixture of gas and air drawn in at atmospheric pressure was exploded. In the second, with which the author had connected Dr. Siemens's name WILLIAM SIEMENS, F.R.S. 205 ostliat of the first proposer, the combustion was produced gradually ; the gases were ignited as they flowed into the heating cylinder. In the third type, the gases, after being compressed and mixed, admitted into the working cylinder, and suddenly exploded. With reference to the early engine which Dr. Siemens constructed in 1860, Plate 87, the author had stated that it combined other rl. 'incuts, which were entirely wanting in the gas-engines of the present day. The gas-engine of the present day, taking either of the three types, was, in his opinion, in the condition of the steam-engine at the time of Newcomen. The fuel was burnt in a cylinder which it was attempted to keep cold by passing water over it, and it was easy to conceive that the heat so generated, was only partly utilised for maintaining the state of expansion of the heated gases, the cold sides of the cylinder taking a good half of it away at once, thus causing a great loss. Then there was another palj >uble loss in these engines. After expansion had taken place, after half the heat had been wasted in heating a cylinder which was intended to be kept cool in order to allow the piston to move, the gases were discharged at a temperature of 1,000°, or in the best types about 700°. That amount of heat, representing in one case one-half and in the other two-thirds of the total heat gene- rated, was thrown away. This was heat which could be saved and made useful. Instead of commencing the combustion at a tem- perature of 60°, if the heat of the outgoing gases were transferred to the incoming gases, combustion might commence at a tempera- ture of nearly 1,000°, and the result would be a very great economy. In the engine which he constructed in 1860 all those points were fully taken into account. The combustion of the gases took place in a cylinder without working a piston, and in a cylinder that could be maintained hot, and the gases, after having complete expansive action, communicated their heat by means of a regenerator to the incoming gases before explosion took place. Although the engine was not worked with ordinary gas used for illumination, but by a cheaper kind made in a gas-producer, he then thought that a gas-engine constructed on that principle would prove to be the nearest approach to the theoretical limits which could never be exceeded, but which might exceed the limits of the steam-engine four or five fold. The engine promised to give very good results, but about the same time he began to give his 206 SCIENTIFIC PAPERS. attention to the production of intense heat in furnaces, and having to make his choice between the two subjects, he selected the furnace and the metallurgic process leading out of it ; and that was why the engine had remained where it was for so long a time. But now the time had come when there was a greater demand for engines of a smaller kind to do their best in houses and in small works, and when marine engineers especially had become fully alive to the importance of more economical arrangements. He therefore looked upon the question before the Institution as one of first importance to engineers, and he hoped that it would be well discussed. METALLURGY. METALLURGY. "ON THE REGENERATIVE GAS FURNACE AS APPLIED TO THE MANUFACTURE OF CAST STEEL." [A Lecture delivered before Hit Fellows of the Cliemical Society, May 7th, 1868.] By C. W. SIEMENS,* F.R.S., Mem. Inst. C.E. IN responding to your call to deliver a lecture to your Society, on a subject of applied chemistry, I feel that I have undertaken a very responsible task, a responsibility which is only balanced by the honorary distinction conferred by your call. It is a hopeful sign of the advancement of science that your Society puts itself into intellectual communication with en- gineers and others, whose mission it is to apply and practise that pure science cultivated within your body. It would be pre- sumptuous on my part to reason with you upon a purely chemical subject, for although many years ago I had the advantage of re- ceiving instruction f romWohler and Himly, I can in no way lay claim to be a chemist of the present day. Yet I can safely affirm that of all the instructions I received in early life, there is none that has been a more useful guide to me in my professional pursuits. The subject to which I wish to call your attention this evening is one that has occupied my mind for many years, and which I hope may engage your interest, involving as it does the generation of intense heat by means essentially differing from those in general use, and the application of that heat to the production of cast steel in large masses, and directly from the ore or scrap metal. * Excerpt Journal of the Chemical Society, 1868, pp. 279-310. VOL. I. P 2IO THE SCIENTIFIC PAPERS OF The regenerative gas furnace, which is the joint production of my brother, Frederick Siemens, and myself, is already known through its application to nearly all those branches of industry in which furnace heat is employed. It was described by Faraday, to the members of the Royal Institution, in the last public lecture delivered by that great philosopher in 1862, and has since been the subject of several publications. I need not, therefore, bring before you all the features of this mode of producing intense heat for the various purposes to which it has been applied, but shall confine myself to its description as applied only to the production of cast steel in large masses, which is the principal subject of my present communication. NATURE OF STEEL. — Before proceeding with this description I shall briefly remark upon the nature of steel and the methods by which it has hitherto been produced. STEEL. — Steel is generally regarded as a compound of iron and carbon, possessing the remarkable quality of becoming exceedingly hard when heated and suddenly cooled. The proportion of carbon determines the degree of hardness of which the steel is capable, or what is termed its temper. The following table of the percentage of carbon in steel suited to different purposes, is prepared from analyses made in my laboratory by Mr. A. Willis, unless another authority is men- tioned. Description. Carbon per cent. Authority. Wootz . ' . . . . 1-34 T. H. Henry Steel for flat files . . . . T2 A.Willis „ for turning tools . TO „ ,, (Huntsman's) for cutters .1*0 „ ., for cutters .... '9 „ „ for chisels .... "75 „ Die steel (welding) ... '74 „ Double shear steel .... '7 ,, Welding steel .... '68 „ Quarry drills *64 ,, Mason's tools ... '6 „ Ramrods '6 ., Common steel for stamping . '42 .S7A' WILLIAM SIEMENS, l-.R.S. 21 I Description. for magnets containing tungsten . „ spades . . . . „ hammers . Bessemer steel for rails . . . Homogeneous metal armour plates Vi ry mild steel from open hearth furnace Sample before Spiegel was applied Bessemer iron (pure) . Carbon per cent. Authority. •4 •32 •3 •25 to •: •23 •18 •05 trace A. Willis various Percy A. Willis Abel Cast-steel containing less than 0*3 per cent, of carbon is no longer capable of being hardened, and should be classed rather as homogeneous or melted iron than as steel, while on the other hand an excess of carbon above 1'4 per cent, again deprives the metal of the quality of taking a temper, and it must then be regarded as approaching in character rather to white cast-iron. It is, however, a contested question between chemists whether the presence of a third substance may not be necessary to produce steel. Fre*my, in his celebrated controversy with M. Caron before the French Academy, maintains that nitrogen or cyanogen is a necessary constituent of steel ; the investigations of other chemists appear to confirm this theory, and the old Sheffield practice of mixing leather and other animal substances with the charcoal used in the converting furnace would also seem to corroborate it. M. Fremy's theory probably admits of great extension, and it may be that we should regard steel as a triple combination of iron with carbon and with another substance, taken from a series comprising nitrogen, sulphur, phosphorus, silicon, manganese, tungsten, titanium, tin, silver, and probably many other elementary bodies, each of which entering, in an exceedingly small proportion, into combination with the iron and carbon is capable of imparting to the steel distinctive physical properties. NITROGEN. — Nitrogen has been found invariably in the stee produced by the ordinary processes. SULPHUR AND PHOSPHORUS. — Sulphur and phosphorus are commonly regarded as the worst enemies to steel, the one render- ing it " red-short," or incapable of being forged, and the other P 2 212 THE SCIENTIFIC PAPERS OF " cold-short," or brittle at ordinary temperatures. It is owing to the presence of these impurities in nearly all British irons, that the highest qualities of tool steel are still made entirely from Swedish or other charcoal-iron of high quality, produced from the purest ores. If phosphorus exists in steel in quantities exceeding O'l per cent., its presence is indicated on breaking the sample, by peculiarly bright and distinct faces of crystallisation on the fractured surface, but the steel admits of being forged and welded, and though somewhat brittle when cold, it is remarkable for hardness. It would, therefore, not be safe to maintain that phosphorus in small quantities is objectionable in steel under all circumstances. Steel containing above 0'2 per cent, of sulphur breaks under the hammer at a low red heat, and is, therefore, only applicable to the production of steel castings : for this purpose the presence of a small amount of sulphur is unquestionably a positive advantage, imparting increased fluidity to the molten metal and toughness to the casting when cold. This effect is so well understood in Sweden as regards cast-iron, that in casting ordnance sulphur is added to the metal. MANGANESE. — Manganese possesses the remarkable property of counteracting to a great extent the effect of sulphur (or red- shortness) in steel. Its application for this purpose is due to Josiah Marshall Heath (1839), and must be classed among, the most important discoveries in modern times ; for it is only in consequence of the addition of manganese (in the form of oxide, mixed with carbon) to the steel melted in pots, that the Sheffield melters have been enabled to use English puddled iron for the commoner qualities of steel in place of the purer and more costly Swedish iron ; and again it is only in consequence of the addition (by Mushet) of manganese in the form of ferro-manganese or spwgeleisen to the liquid bath produced in the Bessemer converter that the better qualities of English pig-iron have been made avail- able for the production of malleable Bessemer metal. It is dis- tressing to think that the author of this invaluable discovery was deprived of the fruits of his labour by an unjust combination among the manufacturers chiefly benefited by him, who contested the validity of Heath's patents upon trivial grounds, relying for their success upon their financial power to crush his unquestion- able claims. The specific chemical action of manganese has never -S7A' WILLIAM .S7AM//;.V\, I-.R.S. 213 been clearly demonstrated. It is certain that only traces of metallic manganese are ever found in cast-steel, and that the bulk of the manganese added is found combined with oxygen, silica, and alumina, in the form of slag ; yet it follows, from experiments which I have had occasion to make, that on adding manganese to a bath of liquid steel in an open reverberatory furnace, its beneficial action ceases if the metal is retained in the furnace, exposed to the flame for any length of time, say more than half an hour. This is the case quite independently of any sensible reduction in the pro- portion of carbon in the steel, and indicates that the effect of manganese is not due to the removal of sulphur or other substances with which it may enter into combination, but it is inseparable from the presence of metallic manganese in the steel, in however small a quantity. A further confirmation of the view, that the addition of manganese removes no impurity from the steel, is supplied by the fact, that if cast-steel from English iron which has been rendered perfectly malleable at a red-heat, by the ad- dition of manganese, is re-melted ivitlwut adding manganese, it becomes as red-short as ever. According to Parry, the presence of manganese in sensible quantity in steel tends to render it brittle when cold. SILICON. — Silicon in small quantity seems to increase the hard- ness of steel without taking away from its malleability or tough- ness when cold, and the presence of a trace of silicon appears to have the singular effect of preventing that violent evolution of gas from fluid steel at the moment of solidification, which renders the ingot so frequently unsound. Steel containing above 0'5 per cent, of silicon breaks up under the hammer if heated above low redness. TITANIUM, &c. — The effect of titanium, tin, arsenic, silver, and other metals upon steel, is stated to produce increased Itardmss, but I have not myself made any experiments upon this subject, nor been able to find very reliable observations of others. TUNGSTEN has a very remarkable effect upon steel, first ob- served by Dr. Werner Siemens, in 1853, in increasing its power of retaining magnetism when hardened. Being specially interested in this question, I have determined, by careful experiments, the extent of the increase ; and the practical result is, that whereas a horse-shoe magnet of ordinary steel, weighing 2 Ibs., is con- 214 THE SCIENTIFIC PAPERS OF sidered of good quality when it bears seven times its own weight, and the famous Haarlem magnet of the same weight, supports about 13 times its weight, I am now able to produce a similar horse-shoe magnet carrying 20 times its weight, suspended from its armature. The chief difficulty besetting experiments on the effects of these various admixtures upon the quality of steel, consists in the unavoidable presence of other substances in variable propor- tions ; but the effects of these other substances could be eliminated if the experiments were accompanied by exhaustive analyses, and it is impossible to over-estimate the advantages that would result from such a course. PROCESSES. — Dr. Percy, in his truly invaluable metallurgical work, has made us acquainted with the various known processes for obtaining steel which have been followed from the earliest times ; but no method of producing steel can be considered admissible at the present day which does not pass the metal through the condition of entire liquefaction, for it is only by fusion that foreign admixtures can be thoroughly separated, and that flaws and fissures can be avoided ; inasmuch, however, as the steel obtained by tiiem may be subsequently fused, I shall briefly refer to them. The principal processes of this class are : — 1. The direct process of making steel, or steely iron, from the ore in the Catalan forge, by employing a large excess of charcoal. The steel is obtained without fusion in the form of a ball of spongy metal, and is drawn out into bars. 2. The cementation process, in which bar-iron is converted into steel by prolonged contact at a comparatively low temperature either with liquid cast-iron, as formerly practised in Styria and elsewhere,* or with crushed charcoal — a method extensively em- ployed in Sheffield at the present day for the manufacture of steel for railway and carriage springs, and for the production of bar-steel from Swedish iron, which, when subsequently melted in pots, makes the finest quality of steel for tools and cutlery. 3. The decarburization process, in which steel is made from cast-iron by the removal of part of the carbon in the puddling * Percy, Metallurgy, II. 790, 807. A7A' WILLIAM .S7A-.J//:.\.s, l-.R.S. 215 furnace, or by the partial application of any of the older methods nf decarburetting cast iron in an open In-aith in direct contact \\ith the fuel. A modified form of the decarhuri/ution process has ••'•(vntly introduced to some extent by Messrs. Heaton and Hariri-raves. They remove the carbon of the pig-iron by the action of oxydizing salts, principally nitrate of soda, and either fuse the crude metal obtained, producing cast steel, or work it up into blooms under the hammer. The Bessemer process, now so well known, is also a method of producing steel by the decarbonization of cast iron : but it presents a vast advantage over those just named, in the fact that the steel is obtained in the liquid state, and may be cast, free from flaws, into homogeneous ingots of any size. As Bessemer steel is produced much more cheaply than the cast steel obtained by any other process yet extensively in use, its introduction has opened out a vast field for the application of steel where iron alone could formerly be thought of. Thus many parts of steam and other machinery, railway plant, boiler-plates, and even rails, are now made of Bessemer steel, and are found to be cheaper in the end when made of that material rather than when made of iron, although their absolute cost is fully twice as great. CAST STEEL. — The remaining methods of producing cast steel, are those in which it is obtained by the fusion either of steel already made by other processes, or of its component materials, iron or iron-ore, on the one hand, and carbon, either as charcoal or already combined in the form of cast iron, on the other. The oldest known steel of high quality, the Indian Wootz, is obtained by the fusion of compact iron and carbonaceous sub- stances in small crucibles, but it is only in the course of the last century that the manufacture of cast-steel was first introduced in Europe. Reaumur states, in his work on the conversion of forged iron into steel, published in 1722, that he had succeeded in producing steel by the fusion together of cast and wrought iron in a common forge ; but steel melting was first practically carried out in the latter half of the century by Huntsman, of Sheffield ; the process he employed, consisting in " the fusion in closed crucibles of steel already made by cementation in cJiarcoal" is still universally in use for the production of the finest qualities of steel for tools and 2l6 THE SCIENTIFIC PAPERS OF cutlery. The Hindoo process has, however, been revived within the last twenty years, by Heath, Price and Nicholson, Gentle Brown, Attwood, and others, and large quantities of steel are now made in Sheffield and elsewhere, by the fusion of puddled iron or puddled steel with charcoal, or with pure pig-iron (Acadian or Spiegeleisen), in such proportions as to form steel of the required quality. The Uchatius process is somewhat similar to these in principle ; it consists in effecting the partial decarburization of granulated pig-iron by fusing it in contact with iron-ore, but the temper obtained is said to be irregular, and, together with the process just mentioned, it labours under the disadvantage of involving the expensive operation of fusion in pots. OPEN HEARTH. — Some method of effecting the fusion of steel more cheaply than in crucibles, as well as in larger masses, has long been a desideratum. Heath, the discoverer of the beneficial action of manganese, was the first (in 1845) to conceive that cast- steel might be produced in large quantities by fusing wrought and cast-iron together upon the open hearth of a reverberatory furnace. The modus operandi he proposed, consisted in melting pig-metal in a cupola, and running it into the heated furnace. The wrought-iron was introduced into another part of the furnace, forming a bank between the bath of fluid metal and the chimney, to be there heated by the waste heat of the flame, previously to its being pushed forward into the liquid in order to be dissolved. Fearing the effect of the ashes from a common fire-place, Heath proposed to heat his furnace by jets of gas, and there is every probability that his experiments would have been crowned with success, if he had possessed the means of imparting to his flame the intensity of heat and, at the same time, the absence of cutting draught, which are essentially necessary. Since the date of Heath's patent, the fusion of steel in an open furnace has formed the subject of an extensive series of experiments, by Sudre, in France. The experiments of M. Sudre were made at the Monta- taire Iron Works, at the expense of the Emperor of the French, and were superintended, on his behalf, by three members of the French Institute ; MM. Sainte-Claire Deville, Treuille de Beau- lieu, Colonel of Artillery, and Caron, Captain of Artillery, who have made an able report on the subject, showing that it is just possible to raise the heat of an ordinary furnace by means of a A/A' WILLIAM .sy/-;.i//-;.VA, /-'.A-.A. 217 fan -I (last, sufficiently to effect the fusion of tool-steel upon the op.'ii hearth in protecting the metal by a layer of glass, but that the rapid destruction of the furnace, the cost of fuel, and other diilk'iilties attending the operation, were such as to render the process, commercially, of doubtful value. RKCKNKKATIVI: (IAS FURNACE. — The regenerative gas furnace is so manifestly suitable for the operation of melting steel, both in pots and on the open hearth, that my attention was directed from the first towards this object. The early experiments conducted by my brother and myself at Sheffield failed, however, partly on account of certain irregularities, arising from defects in the furnace which have since been removed, but chiefly in consequence of the want of determination on the part of the manufacturers and their workmen to persevere with us to the attainment of the proposed results. ATTWOOD. — In 1862, Mr. Charles Attwood took a licence to apply the regenerative gas furnace to the melting of steel upon the open hearth in connection with certain chemical processes or mixtures of his own. I supplied the design of a furnace which answered the purpose, except that the quality of steel produced was not such as Mr. Attwood desired. This circumstance decided him to carry out his process in closed pots heated in the same furnace. LE CHATELIER. — In 1863, my friend, M. Le Chatelier, Inge- nieur en Chef des Mines, elaborated a process for producing steel from cast-iron by puddling, and melting the hot puddled blooms in a bath of cast-iron prepared in a regenerative gas furnace, upon a bed of 'bauxite, of the following composition : — Silica 13 to 17 per cent. Alumina GO to 65 „ Peroxide of iron . . . . 4 to 8 „ Water in combination . . . 15 to 17 ,, This material presents the advantage of being exceedingly in- fusible and of containing no materials that could impart hurtful ingredients to the steel. A furnace of great heating power was constructed by Messrs. Boigue, Rambour and Co., at their works near Montlu9on, in France, under my superintendence, and would 2l8 THE SCIENTIFIC PAPERS OF certainly have accomplished the desired object if the company had displayed the least determination to succeed. The furnace-bottom of bauxite did not succeed, as it was not solidified by the heat, and rose to the surface of the liquid bath, — but this defect was soon rectified by the substitution of a white sand bottom. Through some carelessness, however, the covering arch of the furnace was damaged by excess of heat ; and this slight accident, which proved nothing except an ample sufficiency of heating power, sufficed to deter the company from pressing on to the attainment of that success which was so nearly within their reach. In the meantime I had granted a licence to Messrs. Eraile and Pierre Martin, of the Sireuil Works, to melt steel, both in pots and on the open hearth, and a furnace was erected by them in 1864 which was chiefly intended for a heating furnace, but was at the same time constructed of such materials (Dinas brick) and in such a form as to be also applicable for melting steel. With this furnace, which was really less suitable than those previously erected, MM. Martin have succeeded in producing cast-steel of good quality and of various tempers, ard their pro- duce was awarded a gold medal at the great French Exhibition of last year. MM. Martin have since patented various arrangements of their own, such as the employment of particular fluxes to cover the surface of the molten metal, the application of a separate furnace for heating the iron before charging it into the melting furnace, and the employment of particular brands of cast and wrought-iron, which may be useful under special circumstances but which form no essential part of the general solution of the problem. Having been so often disappointed by the indifference of manufacturers and the antagonism of their workmen, I deter- mined, in 1865, to erect experimental or " Sample Steel Works " of my own at Birmingham, for the purpose of maturing the details of these processes, before inviting manufacturers to adopt them. The first furnace erected at these works, is one for melt- ing the higher qualities of steel in closed pots, and contains 16 pots of the usual capacity. The second, erected in 1867, is an open bath furnace, capable of melting a charge of 24 cwt. of steel every 6 hours. Although these works have been carried on under every disadvantage, inasmuch as I had to educate a set of men \M' WILLIAM SIEMENS, F.R.S. 2ig capable of managing steel furnaces), the result has been most beneficial, in affording me an opportunity of working out the details of processes for producing cast-steel from scrap-iron of tn-dinary quality and also directly from the ore, and in proving these results to others. I shall now proceed to describe the construction and working ot the regenerative gas furnaces (similar to those at Birmingham) wlurh are now at work, or in course of erection, in this country and abroad for the production of cast-steel, both by the old method of fusion in pots, and by the new system of making cast-steel on a large scale and on an open furnace bed, from scrap-iron and from the ore. The regenerative gas furnace consists of two essential parts : The gas producer, in which the coal or other fuel used is con- verted into a combustible gas ; and The furnace, with its " regenerators " or chambers for storing the waste heat of the flame, and giving it up to the in-coming air and gas. Any combustible gas might be burned in the regenerative furnace ; I have used ordinary lighting gas very successfully on a small laboratory scale, but it is far too costly to be employed in larger furnaces, and the only gas generally available is that gene- rated by the complete volatilisation of coal, wood, or other fuel, with admission of air in a special " gas producer." Any descrip* tion of carbonaceous matter may be worked in a suitable gas producer, and will afford gas sufficiently good for the supply of even those furnaces in which the highest heat is required. Coal is the fuel chiefly used for gas furnaces in England ; small coke has been employed in some cases, as in gas-works, where it is to be had at a cheap rate ; wood is used in France, Bohemia, and Spain ; sawdust in Sweden, furnishing gas for welding and other high-heat furnaces ; lignite in various parts of Germany ; and peat in Italy and elsewhere ; this last being applicable with the greatest relative advantage. Plate 38 represents a gas producer suitable for burning non- caking slack. In form it is a rectangular fire-brick chamber, one side of which, B, is inclined at an angle of from 45° to 60°, and is pro- vided with a grate, C, at its foot. The fuel is filled in at the top 220 THE SCIENTIFIC PAPERS OF of the incline at A, and falls in a thick bed upon the grate. Air is admitted at the grate, and as it rises slowly through the ignited mass, the carbonic acid, first formed by the combination of the oxygen with the carbon of the fuel, takes up an additional equiva- lent of carbon, forming carbonic oxide, which diluted by the inert nitrogen of the air and by a little unreduced carbonic acid, and mixed with the gases and vapours distilled from the raw fuel during its gradual descent towards the grate, is led off by the gas flue to the furnace. The ashes and clinkers that accumulate on the grate are removed at intervals of one or two days. The composition of the gas varies with the nature of the fuel used, and the management of the gas producer. That of the gas from the producers at the Plate Glass Works, St. Gobain, France, burning a mixture of f caking coal and \ non-caking coal, is as follows, by an analysis dated July, 1865 : — VOLUMES. Carbonic oxide . 23"7 Hydrogen . . . . . . . . 8'0 Carburetted hydrogen . . < . .2*2 Carbonic acid 4'1 Nitrogen ..... ... 61'5 Oxygen 0'4 99-9 The trace of oxygen present is no doubt due to carelessness in collecting the gas, or to the leakage of air into the flue, and allowing for this, the corrected analysis will stand as under : — VOLUMES. Carbonic oxide 24'2 \ Hydrogen 8'2 / 34'6 Carburetted hydrogen . . . 2'2 ] Carbonic acid . . . . . 4'2 •vr-i. fi . > f G5'4 Nitrogen (>1 lOO'O Only the first three of these constituents, say 35 per cent, of the whole, are of any use as fuel, the nitrogen and carbonic acid present only diluting the gas. It is the presence of this large proportion of inert gases, which must be heated to the full \/A> WILLIAM SIEMENS, F.R.S. 221 temperature of the flame, that renders it so difficult to maintain a high heat by gas of this description burned in the ordinary way. In u>ing such gas in a regenerative furnace the presence of so large an amount of nitrogen is not objectionable, as the heat it ies off' is given up again to the air and gas coming in. The gas as it passes off from the fuel contains also more or less aqueous vapour, which is got rid of by cooling it, with some tar and other impurities, and a small quantity of suspended soot and dust. Any air drawing in unburned through a hole in the mass of fuel, reduces the value of the gas, by burning the carbonic oxide again to carbonic acid. To prevent the indraught of air in this way at the side of the grate, I have found it very advantageous to set the side walls of the gas producer back, forming a broad step, about nine or ten inches above the grate ; any air creeping up along the wall is thus thrown into the mass of fuel and completely burned. The effect of this feature in the form of the producer on the quality of the gas has been very striking. Three-tenths of the total heat of combustion of solid carbon are evolved in burning it to carbonic oxide ; but in the gas producer, a small portion only of "this heat is really lost, because it is in a great measure taken up and utilized in distilling the tar and hydrocarbon gases from the raw fuel ; and it may be still further economised, especially in burning a fuel, such as coke or anthra- cite, which contains little or no volatile matter, by introducing a regulated supply of steam with the air entering at the grate. This is effected very simply by keeping the ash-pit always wet. The steam is decomposed by the ignited coke, and its constituents, hydrogen and oxygen, are rearranged as a mixture of hydrogen and carbonic oxide, with a small variable proportion of carbonic acid. Each cubic foot of steam produces nearly two cubic feet of the mixed gases, which, being free from nitrogen have great heating power and form a valuable addition to the gas. The proportion of steam that can be advantageously introduced into the gas pro- ducer, is, however, limited, as it tends to cool the fire, and if this is at too low a heat, much carbonic acid is produced instead of carbonic oxide, causing waste of fuel. From the high temperature of the gas, as it rises from the fuel (1,000° F. to 1,300° F.), and from its comparatively low specific gravity, it is considerably lighter than atmospheric air, and 222 THE SCIENTIFIC PAPERS OF ascends into the upper part of the producer with a slight outward pressure. It is necessary to maintain this pressure through the whole length of the gas flue, in order to ensure a free supply of gas to the furnaces, and to prevent its deterioration in the flue, through the indraught of air at crevices in the brickwork. The slight loss of gas by leakage, which results from a pressure in the flue, is of no moment, as it ceases entirely in the course of a day or two, when the crevices become closed by tar and soot. Where the furnace stands so much higher than the gas producer, that the flue may be made to rise considerably, the required plenum of pressure is at once obtained ; but more frequently the furnaces and gas producers are placed nearly on the same level, and some special arrangement is necessary to maintain the pressure in the flue. The most simple contrivance for this purpose is the " elevated cooling tube." The hot gas is carried up by a brick stack to a height of eight or ten feet above the top of the gas producer, and is led through a horizontal sheet-iron cooling tube, J, of not less than 60 square feet of surface per gas producer, from which it passes down either directly to the furnace, or into an underground brick flue. The gas rising from the producer at a temperature of about 1100° F., is cooled as it passes along the overhead tube, and the descending column is consequently denser and heavier than the ascending column of the same length, and continually over-balances it. The system forms, in fact, a syphon in which the two limbs are of equal length, but the one is filled with a heavier fluid than the other. The height of cooling tube required to produce as great a pressure in the flue as would be obtained by placing the gas producers, say ten feet deeper in the ground, may be readily calculated. The temperature of the gas as it rises from the pro- ducers has been taken as 1,100° F., and we may assume that it is cooled in the overhead tube to 100° F., an extent of cooling very easily attained. The calculated specific gravity, referred to hydrogen, of the gas of which I have quoted the analysis, being 13*14, we obtain the following data : — LB. Weight of the gas per cube foot at 1,100° F. = -022 100° F. = -061 Weight of atmospheric air per cube foot at 60° F. = -076 S/K WILLIAM SIEMENS, F.R.S. 22$ ami from these we have, on the one hand, the increase of pressure J.:T loot of height, in a flue rising directly from the gas producer, = -on; — •( '!'•_' = M).H ll>. per square foot; and on the other hand, tip- excess of pressure at the foot of the downtake from the cooling tube, over that at the same level in the flue, leading up from the gas producer (for each foot in height of the cooling tub.-) = -OG1 — '022 = -039 Ib. per square foot. The height of the cooling tube above the level of the flue that will be sufficient to produce the required pressure, equal to 10 feet of heated gas column, is therefore '. - . 10 ft. = 13' 10", or say 14 feet. 'OoJ This method of obtaining a pressure in the gas-flue by cooling the gas, has been objected to as throwing away heat that might be employed to more advantage in the furnace, but this is not the case, because the action of a regenerator is such, that the initial temperature of the gases to be heated has no effect on the final temperature, and only renders the cooling of the hotter fluid more or less complete. The only result, therefore, of working the furnace with gas of high temperature is to increase the heat of the waste gases passing off by the chimney flue. The complete cooling of the gas results, on the other hand, in the great advantage of condensing the steam that it always carries with it from the gas producer ; and in the case of iron and steel furnaces, in burning wet fuel, it is absolutely necessary to cool the gas very thoroughly, in order to get rid of the large amount of steam that it contains which, if allowed to pass on to the furnace would oxidise the metal. There is, undoubtedly, a certain waste of heat, which might be utilized by surrounding the cooling tube with a boiler, or by otherwise economising the heat it gives off, as, for instance, in drying the fuel ; but the saving to be effected is not very great, for as 100 volumes of the gas require for combustion about 130 volumes of air, including 20 per cent, above that theoretically required, the heat given off in cooling the gas 1,000° is no more than would be lost in discharging the products of the complete combustion of the fuel, at a temperature 435° in excess of the actual temperature of 200°, and this loss is greatly diminished if a richer gas is obtained. In erecting a number of gas producers and furnaces, I generally 224 THE SCIENTIFIC PAPERS OF prefer to group the producers together, leading the gas from all into one main flue, from which the several furnaces draw their supplies. The advantages of this are saving of labour and con- venience of management, from the gas producers being all close together, and greater regularity in working, as the furnaces are seldom all shut off at once ; nor is it likely that all will require at the same time an exceptional amount of gas. From the fact that the gas producers may be at any distance from the furnaces that they supply, if they are only at a lower level, it would be perfectly practicable to erect them in the very coal mine itself, burning the slack and waste coal in situ (in place of leaving it in the workings as is now often done), and distribut- ing the gas by culverts to the works in the neighbourhood, instead of carrying the coal to the different works and establishing special gas producers at each. In rising to the mouth of the pit, the gas would acquire sufficient pressure to send it through several miles of culvert. In the regenerative furnace the gas and air employed are sepa- rately heated by the waste heat of the flame, by means of what are termed "regenerators," placed beneath the furnace. These are four chambers, filled with fire-bricks, stacked loosely together, so as to expose as much surface as possible ; the waste gases from the flame are drawn down through two of the regenerators, and heat- ing the upper rows of bricks to a temperature little short of that in the furnace itself, pass successively over cooler and cooler sur- faces and escape, at length, to the chimney flue nearly cold. The current of hot gases is continued down through these two regene- rators until a considerable depth of brickwork, near the top, is uniformly heated to a temperature nearly equal to that of the entering gas, the heat of the lower portion decreasing gradually downwards, at a rate depending on the velocity of the current, and the size and arrangement of the bricks. The direction of the draught is then reversed ; the current of flame or hot waste gases is employed to heat up the second pair of regenerators ; and the gas and air entering the furnace are passed in the opposite direc- tion through the first pair, and coming into contact, in the first instance, with the cooler brickwork below, are gradually heated as they ascend, until, at some distance from the top, they attain a temperature nearly equal to the initial heat of the waste gases, .s/A' WILLIAM SIEMENS, F.R.S. 22$ ami, passing up into the furnace, meet and at once ignite, pro- '1 iii-ing a strong flame, which, after passing through the heating- chamber, is drawn down through the second pair of regenerators to the chimney-flue. The temperature attained by the ascending gas and air remains nearly constant, until the uppermost courses of the regenerator brickwork begin sensibly to cool ; but by this time the other two regenerators are sufficiently heated, and the draught is again reversed, the stream of waste gases being turned down through the first pair of regenerators, re-heating them in turn, and the gas and air which enter the furnace being passed up the second. By thus reversing the direction of the draught at regular inter- vals, nearly all the heat is retained in the furnace that would othenvise be carried off by the products of combustion, the tem- perature in the chimney-flue rarely exceeding 300° Fahr., whatever may be the heat in the furnace. The proportion of heat carried off in an ordinary furnace by the products of combustion is gene- rally far greater than that which can be utilized, as all the heat of the flame below the temperature of the work to be heated is abso- lutely lost. The economy of fuel effected in the regenerative gas furnace, by removing this source of loss, and making all the heat of the waste gases, however low its intensity, contribute to raise the temperature of the flame, amounts in average practice to fully 50 per cent, on the quantity used in an ordinary furnace, and the saving is greater the higher the heat at which the furnace is worked. In addition to this economy in the amount of fuel used, a much cheaper quality may generally be burned in the gas pro- ducer than could be used in a furnace working at the same heat, and in which the fuel is burned directly upon the grate in the ordinary way. When the heat of the furnace is not abstracted continually by cold materials charged into it, the temperature necessarily increases after each reversal, as only a very small fraction of the heat gene- rated is carried off by the waste gases. The gas and air, in rising through the regenerators, are heated to a temperature nearly equal to that at which the flame had been passing down, and when they meet and burn in the furnace the heat of combustion is added to that carried up from the regenerators, and the flame is necessarily lotter than before, and raises the second pair of regenerators to VOL. I. Q 226 THE SCIENTIFIC PAPERS OF a higher heat. On again reversing, this higher heat is communi- cated to the gas and air passing in, and a still hotter flame is the result. The temperature that may be attained in this way by the gradual accumulation of heat in the furnace and in the upper part of the regenerators appears to be quite unlimited, and the heat at which a suitably designed furnace can be worked is limited in practice only by the difficulty of finding a material sufficiently refractory of which it can be built. Welsh Dinas brick, consisting of nearly pure silica,* is the only material, of those practically available on a large scale, that I have found to resist the intense heat at which steel-melting furnaces are worked ; but though it withstands perfectly the temperature required for the fusion of the mildest steel, even this is melted easily if the furnace is pushed to a still higher heat. As the gas flame is quite free from the suspended dust which is always carried over from the fuel by the keen draught of an ordinary furnace, the brickwork exposed to it is not fluxed on the surface and gradually cut away, but fails, if at all, only from abso- lute softening and fusion throughout its mass. A Stourbridge brick, for example, exposed for a few hours to the heat of the steel-melting furnace, remains quite sharp on the edges, and is little altered even in colour ; but it is so thoroughly softened by the intense heat, that on attempting to take it out,, the tongs press into it and almost meet, and it is often pulled in two, the half-fused material drawing out in long strings. It results from this perfect purity of the flame, that where the heat is not suffi- cient to effect the absolute fusion of the bricks employed, the length of time is almost unlimited during which a gas furnace will work without repairs. * Analysis of Dinas " clay " from Pont-Neath, Vaughan, Vale of Neath (Percy's Metallurgy, Vol. I. p. 237). Silica . Alumina . Protoxide of iron Lime Potass and soda Water combined 98-31 0-72 0-18 0-22 0-14 0-35 99-92 The " clay " is mixed with 1 per cen\ of lime in making the bricks. SfK WILLIAAf SIEMENS, F.R.S. 227 Another advantage in employing the fuel in the manageable f<>rm of gas is that the rate of combustion may be regulated at ire to produce an active heating flame of any length, from little more than two feet, as in the pot steel-melting furnaces, to thirty feet in the largest furnaces for the fusion of plate glass ; and the most intense heat may be thrown exactly upon the charge, the ends of the furnace and the apertures through which the gas and air are introduced being actually protected from the heat by the currents of unburned and comparatively cool gases flowing through them, and only mixing and burning at the very point at \\hirh the heat is required, and where it is taken up at once by the materials to be fused or heated. This is of especial importance in the case of those furnaces in which a very intense heat is employed. The amount of brickwork required in the regenerators to absorb the waste heat of a given furnace is a matter of simple calculation. The products of the complete combustion of one pound of coal have a capacity for heat equal to that of nearly 17 pounds of fire- brick,* and (in reversing every hour) 17 pounds of regenerator * Taking the analysis by Vaux of the celebrated ten-yard coal of South Stafford- shire (Watts' Dictionary of Chemistry, i. 1081), the exact calculation is as follows : — Composition of the coal. Carbon . 7857 Hydrogen Sulphur Nitrogen ( ixy- Ash •0529 •0039 Oxygen required. 2-0952 0-4232 0-0039 •0184 •1288 . . less . . •0103 net oxygen required 1 -0000 20 per cent, excess Total Oxygen Corresponding Nitrogen . . 9 '6 16 Nitrogen in the fuel . . -018 2-5223 0-1288 2-3935 0-4787 2-8721 Total Nitrogen . . 9 -634 Oases produced from 1 Ib. of coal. Carbonic acid = 2'881 Water (Steam) = 0'476 Sulphurous acid = 0'004 Oxygen in excess = 0 "479 Nitrogen = 9 '634 Specific heats. •217 •480 •154 •218 •244 Equivalent weight of water. •625 •228 •001 •104 2-350 Total equivalent weight of water .... 3 '308 ,, ,, firebrick (sp. heat = 0-2). 16-540 Q 2 228 THE SCIENTIFIC PAPERS OF brickwork at each end of the furnace per pound of coal burned in the gas-producer per hour would be theoretically sufficient to absorb the waste heat, if the whole mass of the regenerator were uniformly heated at each reversal to the full temperature of the flame, and then completely cooled by the gases coming in ; but in practice by far the larger part of the depth of regenerator chequer-work is required to effect the gradual cooling of the products of combustion, and only a small portion near the top, perhaps a fourth of the whole mass, is heated uniformly to the full temperature of the flame ; the heat of the lower portion decreasing gradually downwards nearly to the bottom. Three or four times as much brickwork is thus required in the regenerators, as is equal in capacity for heat to the products of combustion. The best size and arrangement of the bricks is determined by the consideration of the extent of opening required between them to give a free passage to the air and gas, and by the rule, deduced from my experiments on the action of regenerators in 1851-2,* that a surface of six square feet is necessary in the regenerator to take up the heat of the products of combustion of one pound of coal in an hour. By placing the regenerators vertically and heating them from the top, the heating and cooling actions are made much more uniform throughout than when the draught is in any other direction, as the hot descending current on the one hand passes down most freely through the coolest part of the mass, while the ascending current of air or gas to be heated, rises chiefly through that part which happens to be hottest, and cools it to an equality with the rest. The regenerators should be always at a lower level than the heating chamber ; as the gas and air are then forced into the furnace by the draught of the heated regenerators, and it may be worked to its full power, either with an outward pressure in the heating chamber, so that the flame blows out on opening the doors or with the pressure in the chamber just balanced, the flame some- times blowing out a little, and sometimes drawing in. The out- ward pressure of the flame prevents that chilling of the furnace, * Proceedings of the Institution of Civil Engineers, 1852-3, page 571, " On the Conversion of Heat into Mechanical Effect. " SfX WILLIAM SIEMENS, F.R.S. 22$ and injury to the brickwork, from the in-draught of cold air through crevices, which is otherwise unavoidable in any furnace worked without blast. The action of the furnace is regulated by the chimney damper, and by valves governing the supply of gas and air, and the draught is reversed by cast-iron reversing valves, on the principle of the common four-way cock. FUSION OF STEEL IN CRUCIBLES. — In the application of the system to the fusion of steel in closed pots or crucibles, the melting-chamber, containing generally 24 pots, is constructed in the form of a long trench, 8 feet 6 inches wide at the bottom, and gathered in to under 2 feet at the top. The sides of the melting- chamber are arched both horizontally and vertically, to keep them from sinking together in working, and the work is strengthened by cross walls at intervals. The pots are set in a double row along the centre of the melting-chamber, and the flame passes from side to side, the gas and air from the regenerators being intro- duced alternately from one side and from the other, opposite to each pair of pots. The melting-chamber is closed above by loose firebrick covers, which are drawn partly off in succession by means of a lever suspended from a pulley above the furnace, when the pots are to be charged or drawn out. The pots stand in a bed of finely-ground coke-dust, resting on iron plates. The coke-dust burns away only very slowly, if it is made of hard coke and finely ground, and it presents the great advantage of remaining always in the form of a loose dry powder, in which the pots stand firmly, while every other material that I have tried either softens at the intense heat, or sets after a time into a hard, uneven mass, in which the pots do not stand well. The process of melting carried out in this form of gas furnace is the same in all respects as that in the small air furnaces or melting-holes fired with coke which are commonly employed, but a great saving is effected in the cost of fuel, and in the number of crucibles required. The ordinary consumption of hard coke, costing 22s. per ton in Sheffield, is between three and four tons per ton of steel fused, while in the gas furnace the same work may be done by the expenditure of 15 to 20 cwt. of common coal slack (worth only 5s. to Ss. per ton), at a cost that is of only 5s. against 75s. per ton 230 THE SCIENTIFIC PAPERS OF of steel melted. There is a further saving in the number of crucibles required, as they may be used in the gas furnace four or five, and sometimes even ten times, while in furnaces heated by coke, two or three casts are as much as are ever obtained. The lining of the furnace lasts at least 15 to 20 weeks without repair (in working day and night), while 4 to 5 weeks is the longest duration of the ordinary coke-fired holes. FUSION OF STEEL ON THE OPEN BED.— The furnace employed for the fusion of steel on the open bed is similar in shape to a reheating or puddling furnace ; the direction of the flame is from end to end ; and the regenerators are placed transversely below ihe bed, which is supported on iron plates, kept cool by a current of air. The air enters beneath the bed plates in front, and escapes by two ventilating shafts at the back of the furnace near the ends. This cooling of the bed is very necessary to keep the slag or melted metal from finding its way through into the regenerator chambers. The upper part of the furnace is built entirely of Dinas brick. There are three doors in the front of the furnace, one in the centre immediately over the tap-hole, and two near the bridges, through which the bed can be repaired when necessary, and ingot ends or other heavy scraps may be charged in. Sloping shoots are provided at the back of the furnace, through which long bars, such as old rails, may be conveniently charged, and beneath these are openings for charging the pig-iron. The upper end of the shoots is on a level with an elevated charging platform behind the furnace. The bottom of the furnace is formed of silicious sand, which answers exceedingly well if properly selected and treated. Instead of putting moist sand into the cold furnace, as is usually done in preparing the bottoms of furnaces for heating or melting iron or copper, I dry the sand, and introduce it into the hot furnace, in layers of about 1" thickness. The heat of the furnace must be sufficient to fuse the surface of each layer, that is to say, it must rather exceed a welding heat to begin with, and rise to a full steel-melting heat at the end of the operation, in order to impart additional solidity to the uppermost layers. Care must be taken that the surface of the bath assumes the form of a, shallow basin, being deepest- near the tap-hole. Some white sands, such as S/R WILLIAM SIEMENS, F,R.S. 231 from Gornal, near Birmingham, will set under these circum- stances into a hard impervious crust, capable of surviving from L'<) to 80 charges of liquid steel, without requiring material repairs. If no natural sand of proper quality is available, white sand, such as Fontainebleau sand, may be mixed intimately with about 25 per cent, of common red sand, to obtain the same results. In tapping the furnace, the loose sand near the tapping-hole is removed, when the lower surface of the hard crust will be reached. The lowest point of this surface is thereupon pierced by means of a pointed bar, upon the withdrawal of which the fluid metal runs out from the hottest and deepest portion of the bath into the ladle in front of the furnace. M. Le Chatelier now proposes to mix the natural Bauxite, of which the bottom of the experimental furnace at the works of MM. Boignes, Ilambourg and Co., near MontluQon was first made, with about 1 per cent, of chloride of calcium dissolved in water, to calcine the mixture, and to form it into moulded masses of highly refractory material. A hard bottom being thus prepared, and the heat of the furnace being raised to whiteness, it is ready to receive the materials to be melted. If these materials consist of bar iron, or of old iron and steel rails, they are cut into lengths of about six feet, and are intro- duced into the furnace through slanting hoppers from the elevated platform at the back, so that their ends rest upon the sand bottom forming the bath. If the capacity of the furnace is such, that charges of 3 tons can be formed, about 6 cwt. of grey pig-iron is introduced through the ports or short hoppers, below the main charging-hoppers before-mentioned. As soon as a bath of pig metal is formed, the heated ends of the rails or bars begin to dissolve, causing the bars gradually to descend. By partially closing the mouths of the charging-hoppers, a regulated quantity of flame is allowed to escape from the furnace, in order to heat the descending bars of metal previous to their entry into the melting-chamber, the object being to maintain the high temperature of the furnace, notwithstanding the constant introduction of cold metal. The escaping products of combustion, which are thus withdrawn from 232 THE SCIENTIFIC PAPERS OF the regenerators, are a positive gain to the heat of the furnace, because, having been in contact with comparatively cold metal, they would be at a heat inferior to that of the upper portions of the regenerators, and would therefore only lower their tempera- tures. As the bars sink in the hoppers by their gravity, they are followed up by additional bars until the metal charged amounts to about three tons, all of which will be rendered fluid within about four hours from the time of commencing the charge. The metallic bath is tested from time to time by the introduction of a bar through one of the front doors of the furnace, and if the bath should become thick before the end of the operation, although the heat has been maintained, it will be necessary to introduce an additional quantity of pig-metal. All the metal being liquid, a sample is taken out by means of a small iron ladle, and plunged into cold water while still red-hot. In breaking this sample upon an anvil, the temper and quality of the metal may be fairly judged. Its fracture should be bright and crystalline, betokening a very small proportion of carbon (not exceeding '1 per cent.), and the metal should be tough and malleable, notwithstanding its sudden refrigeration. From 5 to 8 per cent, of Spiegeleisen (containing not less than 9 per cent, of manganese) is there- upon charged through the side openings upon the bank of the furnace, and allowed to melt down into the bath, which is then stirred and made ready for tapping in the manner before described. The amount of carbon introduced with the Spiegeleisen deter- mines the temper of the steel produced, the manganese being necessary to prevent redshortness, unless Swedish or Styrian iron is used. When old iron rails or scrap of inferior quality are charged, the addition of manganese does not suffice to effect the necessary purification of the steel produced ; but the perfectly liquid con- dition of the bath, together with the unlimited time available for chemical reaction, offer extraordinary advantages for the introduc- tion of such materials as may be found to combine with sulphur, phosphorus, silicon, or arsenic, which are the usual antagonists to be dealt with. The experiments which I have been able to institute in this WILLIAM SIEMENS, F.R.S. 233 direction, are by no means complete ; — nevertheless, I have ob- tained most beneficial results from the introduction into the bath of lithariM', in conjunction with oxidising salts containing strong bases, such as the alkaline nitrates, chromates, chlorates, stannates, titanates, &c. The choice of the reagents and the quantity to be employed depend, naturally, upon the quality and quantity of objectionable matter to be removed. By the aid of the process just described, it will be possible to convert old iron rails into steel rails of sufficiently good quality at a cost scarcely exceeding that of re-rolling them into fresh iron rails. The non-expensive nature of the process may be judged by the fact that extremely little labour is required in conducting it ; that the loss of metal does not exceed from 5 to G per cent., and that from 10 to 12 cwt. of coal suffices to produce a ton of cast steel. ORE. — Although I have succeeded in producing malleable steel from ordinary English iron by this process, it would be unreason- able to expect steel of really high quality, in using those materials which are already contaminated in the blast-furnace ; and I am sanguine in the expectation of producing cast steel superior in quality, and at a low cost, directly from the better description of ores, such as the hematites, magnetic oxides, and the spathic carbonates. My experiments in this direction extend over several years ; and last year I sent a few bars of steel produced from hematite ore, to the French Exhibition, which had stood a high test in Kirkcaldy's machine. A " grand prix " was awarded for this and other applications of the regenerative gas furnaces. Having tried various modifications of the furnace, I have arrived at a form of apparatus (Plates 89 and 40) not dissimilar to the one just described. The furnace and tapping arrangements are, indeed, the same, except that for the slanting hoppers, vertical hoppers over the middle of the bath are substituted, in which the ore gradually descends. Each hopper is formed of a cast-iron pipe, supporting a clay-pipe which is attached to it by means of a bayonet-joint, and reaches down into the furnace, while the cast-iron pipe rests with its flange on the charging platform. 234 -THE SCIENTIFIC PAPERS OF A fire space is provided surrounding each hopper, through which flame ascends from the furnace, and is allowed to escape in regulated quantities near the upper extremity of the retort, the* object being to heat the latter and the ore contained in it to a red heat. A wrought-iron pipe descends into each hopper from a general gas-tube above, through which a current of ordinary pro- ducer gas is forced in amongst the heated ore. The propulsion of the gas is effected most conveniently by means of a steam-jei in the gas-tube leading from the main gas-channel to the top of the furnace, care being taken to effect a total condensation of the steam by passing the gas finally through a small scrubber, in which water trickles over pieces of coke. In this way the gas is at the same time purified from sulphurous acid, the sulphur of which might otherwise combine with the reduced ore. The furnace is charged in the following manner : — The hoppers and gas-pipes being placed in position, about \ cwt. of charcoal is charged through each hopper to form a basis for the ore with which these are afterwards filled. About 10 cwt. of pig-metal is charged through the ports at the back or front of the furnace, which, upon being melted, forms a metallic bath below the hoppers. In the meantime, the ore in the lower parts of the hoppers, being heated in an atmosphere of reducing gas, has become partially reduced into metal sponge, which, in reaching the metallic bath, is readily dissolved in it, making room for the descent of the superincumbent ore, which is likewise reduced in its descent and dissolved in due course, fresh ore being continually supplied on the charging platform. The dissolution of the reduced ore proceeds with extraordinary rapidity, but is practically limited by the time necessary to effect the reduction of the ore in the hopper which occupies several hours. It is, however, not essential that the ore should be thoroughly reduced before reaching the bath, because the carbon contained in the cast metal serves also to complete the operation. I prefer to employ a mixture of hematite and spathic ore, containing the elements for forming a fusible slag, which will accumulate on the surface of the metallic bath, and may be from time to time removed through the centre door. If the ore con- SfK WILLIAM SIEMENS, F.R.S. 235 any silica, it is necessary to add some lime or other fluxing mat' rials, but it is desirable to employ ores containing little gan^ue, in order not to encumber the furnace with slag, reserving the poorer ores for the blast furnace. The ore should, moreover* be in pieces ranging from the size of a pea to that of a walnut, in order to be pervious to the reducing gases. If ores in the form of powder are employed, it is necessary to mix them with about 10 per cent, by weight of light carbonaceous materials, such as dry peat, wood, or charcoal. The metallic bath having sufficiently increased in the course of from three to four hours, the supply of ore is stopped, and that contained in the hoppers is allowed to sink. Before the hoppers are empty, a false cover of cast iron, lined with clay at its under side, is introduced, being suspended from above by a strong wire, in order to prevent the access of flame to the interior of the empty hoppers. Charcoal and ore are filled in upon the top of this false cover, and, on cutting the wire, afterwards form the commence- ment of the succeeding charge. When all the ore has disappeared, the metallic bath is tested as before described in reference to the melting of scrap. If it should be partially solidified, cast iron is added to re-establish complete liquefaction ; but if, on the other hand, the bath con- tains an excess of carbon, oxidising agents may be added as before described, in requisite proportion. From 5 to 8 per cent, of spiegeleisen is then added, and the furnace is tapped as already described. The quality of the steel produced is chiefly dependent upon the quality of the ore, but considering that ores of great freedom from sulphur, phosphorus, or arsenic can be had in large quantities, this process contains all the elements for producing steel of high quality. Having tried a variety of ores, I do not attach much im- portance to their precise composition, so long as they are comparatively free from gaugue, and from sulphur and phos- phorus, the heat being sufficient to reduce the most refrac- tory. My experience is, however, as yet limited to experimental working. I hoped to have been in a position to have given you the temperature of this furnace, as determined by an electric resistance 236 THE SCIENTIFIC PAPERS OF pyrometer, which I have constructed for this purpose, but have not yet been able to obtain satisfactory results, owing to the destruction of the coil of platinum wire, which has to be exposed to the heat. My efforts were baffled moreover by the fact, interesting in itself, that platinum wire produced by fusion in Deville's furnace, does not increase in electrical resistance with increase of temperature in the same ratio as that produced by the old process, owing probably to the presence of carbon or other alloy in fractional quantities. Avoiding the use of fused platinum wire, I have measured temperatures by electrical resistance up to a full welding heat, which I estimate at 1,600° C. = 2,900° F. ; and in judging the heat of the steel-melting furnace by comparison of effects, I should put it at not less than 2,200° C. = 4,000° F. The effect of this degree of heat may be judged by the following : — An ingot of rather hard cast-steel, weighing 6 cwt., was intro- duced into the furnace to be incorporated with the bath of steel. The ingot was nearly cold, and was allowed to remain fifteen minutes upon the bank before it was pushed into the bath, where it was completely dissolved in fifteen minutes, the time occupied in heating and melting the ingot being thirty minutes. A cube of wrought metal of nearly 8 inches, weighing 130 Ibs., was also introduced cold into the furnace, and allowed to remain upon the bank during ten minutes to be heated externally to whiteness, before being pushed into the metallic bath, when twelve minutes sufficed to render it completely liquid. It must be borne in mind that these results are produced without a strong draught, the flame being indeed so mild, as not to oxidise the unprotected metal, which can be maintained for several hours as liquid steel in the furnace without adding carbon in any form. It may be matter for surprise, that the material composing the furnace can be made to resist such a heat, and it must be admitted that best Dinas brick is the only brick capable of resisting for four to five weeks, by which time the thickness of the arch is reduced to about 2 inches, by the absolute fusion of the inner surface ; but this excessive heat is confined to the heated chamber only, the regenerators being at such a moderate heat, that the S/A WILLIAM SIEMENS, F.R.S. 237 chequerwork will stand for months, and the arches for years, of constant working. In conclusion, I wish to express to you my sense of the dispro- portion that exists between the magnitude of the task I have brought before you, and my ability to accomplish it in all its rami- fications. It may be granted that the regenerative gas furnace itself has passed beyond its experimental stage, but much has yet to be done in working out the applications of the system to the useful arts, and the modifications and improvements in processes which it frequently involves. Much, also, has yet to be done before the method of producing cast steel, in one direct process from the ore, can take its place as the recognised system of making steel on a large scale from the purer iron ores, a position that I firmly believe it will assume, sooner or later. It is my earnest hope that, in bringing the subject before your Society, I may induce some of its members to forward this result, by taking up particular branches of the scientific inquiries upon which I have only been able to touch lightly in my present communication. I have much pleasure in acknowledging the assistance I have received in working out this subject from Mr. William Hackney, my principal superin- tendent, and Mr. Willis, the chemist in charge at my experi- mental works. ON PUDDLING IRON, BY C. W. SIEMENS, F.R.S. [Paper read before the Chemical and Mechanical Sections of tlic British Association at Norwich, 1868, and ordered to be printed in extenso among the Reports.] * NOTWITHSTANDING the recent introduction of cast steel for structural purposes, the production of wrought iron (and puddled steel) by the puddling process ranks among the most important branches of British manufacture, representing an annual produc- * Excerpt Journal of the British Association, 1868, pp. 58-71. 238 THE SCIENTIFIC PAPERS OF tion exceeding one and a half millions of tons, and a money value of about nine millions sterling. Notwithstanding its great national importance and the in- teresting chemical problems involved, the puddling process has received less scientific attention than other processes of more recent origin and inferior importance, owing probably to the mis- taken sentiment that a time-honoured practice implies perfect adaptation of the best means to the end and leaves little scope for improvement. The scanty scientific literature on the subject "will be found in Dr. Percy's important work on iron and steel. Messrs. Grace, Calvert and Richard Johnson, of Manchester,* have supplied most valuable information by a series of analyses of the contents of a puddling furnace, during the different stages of the process. These prove that the molten pig metal is mixed intimately, in the first place, either with a molten portion of the oxides (or Fettling) which form the lining or protecting covering to the cast-iron tray of the puddling chamber, or with a proportion of oxide of iron in the form of hammer slag or red ore thrown in expressly with the charge ; that the silicon is first separated from the iron ; that the carbon only leaves the iron during the " boil " or period of ebullition ; and that the sulphur and phosphorus separate last of all while the metal is " coming to nature." The investigations by Price and Nicholson, and by M. Lan, confirm these results, from which Dr. Percy draws some important general conclusions, which have only to be followed up and supple- * "Phil. Mag.," Sept. 1857. The following Table, from Messrs. Calvert and Johnson's Paper, includes the chief results of their investigations : — Time. Carbon. Silicon. Pig iron charged Sample No. 1 12 12-40 2-275 2-726 2-720 0-915 2. . 1-0 2-905 0-197 3 . . 1-5 2-444 0-194 4. . 1-20 2-305 0-182 5 . . 1-35 1-647 0-183 6 . 1-40 1-206 0-163 7 . . 1-45 0-963 0-163 8 . 1-50 0-772 0-168 Puddled bar 9 0-296 0-120 Wire iron 10 . ... 0-111 0-088 5Y/? WILLIAM SIEMENS, J-.K.S. 239 mented by some additional chemical facts and observations, in to render the puddling process perfectly intelligible, and to into relief the defective manner in which it is at present put into practice, involving, as it does, great loss of metal, waste of fuel, and of human labour, and an imperfect separation of the two hurtful ingredients, sulphur and phosphorus. SILICON. — In forming (by means of the rabble) an intimate mechanical mixture between the fluid cast metal and the cinder, the silicon contained in the iron is brought into intimate contact with metallic oxide, and is rapidly attacked, being found afterwards in the cinder in the form of silicic acid (combined with oxide of iron). The heat of the furnace is always kept low during this stage of the process, and the flame is maintained as reducing as possible. CARBON. — The disappearance of the carbon from the metal is accompanied by the appearance of violent ebullition and the evolution of carbonic oxide, which rises in innumerable bubbles to the surface of the bath, and burns (in an ordinary puddling furnace) with the blue flame peculiar to that gas. In puddling in a regenerative gas furnace this blue flame cannot be observed, because the flame of this furnace is strictly neutral, and there is no free oxygen present to burn the carbonic oxide rising from the fluid mass, a circumstance which by itself explains the superior results obtained from the gas furnace. It is popularly believed that the oxygen acting upon the silicon and carbon of the metal is derived directly from the flame, which should, on that account, be made to contain an excess of oxygen, but the very appearance of the process proves that the combination between the carbon and oxygen does not take place on the surface, but throughout the body of the fluid mass, and must be attributed to reaction of the carbon upon the fluid cinder in separating from it metallic iron ; while as the removal of the silicon is still more rapid, and is effected under a reducing flame, there is strong evidence that it also is oxidized rather by the oxygen of the cinder than by the flame.* But it has been argued that, although the reaction takes place below the surface, the oxygen may, nevertheless, be derived from * At page 258 is appended a Table showing the comparative quantities of carbon in various kinds of iron and steel. 240 THE SCIENTIFIC PAPERS OP the flame, which may oxidize the iron on the surface, forming an oxide or cinder, which is then transferred to the carbon at the bottom, in consequence of the general agitation of the mass. This view I am, however, in a position to disprove by my recent experience in melting cast steel upon the open flame bed of a furnace, having invariably observed that no oxidation of the unprotected fluid metal takes place so long as it contains carbon in however slight a proportion. But being desirous to ascertain by positive proof, what is the behaviour of silicon, and carbon, in fluid cast iron, when contact with the atmosphere, or the flame of the furnace, is strictly prevented ; I instituted the following experiment at my Sample Steel Works, at Birmingham : — Ten cwts. of Acadian pig metal, and one cwt. of broken glass, were charged upon the bed of a regenerative gas furnace (usually employed for melting steel upon the open hearth). The bed of this furnace was formed of pure silicious sand, and one object in view was to ascertain whether any reaction takes place between silica and fluid cast metal, it being generally supposed that metallic silicon is produced under such circum- stances by the reducing action of the carbon in the metal upon the silica or silicates present. The cast metal employed in this experiment was Acadian pig, containing silicon, 1*5 per cent. ; carbon, 4*0 per cent. In the course of an hour, the metal and glass were completely melted. A sample was taken out, containing silicon, 1-08 per cent. ; , ( 0'6 per cent, combined carbon, carbon, 2-90 per cent. | 2.3 ^ ^.^ At the end of the second hour, another sample was taken out and tested, the result being silicon, '96 per cent. ; carbon, 2*40 per cent., combined. The physical condition of the metal had now undergone a decided change. The carbon having wholly combined with the iron, rendered it extremely hard. The amount of silicon having steadily diminished, these results prove that no silicon is taken up ly fluid cast metal in contact with silica or silicates. The reduction of the amount of silicon in the metal might be accounted for by the presence of minute quantities of oxides of S/A' U'lI.UAM SIEMENS, F.R.S. 241 iron, produced in melting the pig metal, which oxides were now innvased by the addition of hematite ore in small doses. At the end of the third hour, another sample was taken, containing silicon, '76 per cent. ; carbon, 2*4 per cent, combined, the metal being extremely hard, as before. Additional doses of red ore were added gradually without agitating the bath, and the effect upon the fluid metal was observed from time to time. At the end of the fifth hour, the samples taken from the fluid bath assumed a decidedly mild temper ; when the addition of ore was stopped, and exactly six hours after being charged, the metal was tapped and run into ingots ; it now contained silicon, 0*046 per cent. ; carbon, '25 per cent., thus both the silicon and the carbon had been almost entirely removed from the pig metal by mere contact with metallic oxide under a protecting glass covering. The quantity of red ore added to the bath amounted to two hundredweight, and the weight of metal tapped to ten hundred- weight, five pounds, being slightly in excess of the weight of pig metal charged. But the pig metal had contained 1/5 per cent, of silicon, and 4 per cent, of carbon, or a combined total of 5*5 per cent., whereas the final metal contained collectively only *296 of silicon and carbon, showing a gain of metal of 5'5 - '296 = 5*204 per cent., or including the five pounds of increased weight, a total gain of 5*7 per cent, of metallic iron. Supported by these observations, I venture to assert that tJte removal of the silicon and carbon from the pig iron in the ordinary inuldlinij or " boiling " process is due entirely to the action of the fluid ojcide of iron present, and thai an equivalent amount of metallic iron is reduced and added to the bath, which gain, however, is generally and unnecessarily lost again in the subsequent stages of the process. The relative quantity of metal thus produced from the fluid cinder admits of being accurately determined. The cinder may be taken to consist of Fe3 0* (this being the fusible combination of peroxide and protoxide), together with more or less tribasic silicate (3FeO, SiO3), which may be regarded as a neutral admixture, not affecting the argument, and silicic acid or silica is represented by Si O3, from which it follows that for every four atoms of silicon leaving the metal, nine atoms of VOL. i. n 242 THE SCIENTIFIC PAPERS OF metallic iron are set free, and taking the atomic weights of iron = 28, and of silicon 22'5, it follows that for every 4 x 22-5 = 90'0 grains of silicon abstracted from the metal, 9x28 = 252 grains of metallic iron are liberated from the cinder. Carbonic oxide, again, being represented by C 0, and the cinder by Fe3 O4, it follows that for every four atoms of carbon removed from the metal, three atoms of iron are liberated ; and taking into account the atomic weights of carbon = G and of iron = 28, it follows that for every G x 4 = 24 grains of carbon oxidized, 28 x 8 = 84 grains of metallic iron are added to the bath. Assuming ordinary forge pig, after being remelted in the puddling furnace, to contain about 3 per cent, of carbon and 2 per cent, of silicon, it follows from the foregoing that in removing this silicon 'W3 x 2 = 5'6 per cent., and in removing the carbon ff x 8 = 10' 5 per cent, of metallic iron is added to the bath, making a total increase of 5'G + 10'5 - 5 = ll'l per cent., or a charge of 420 Ibs. of forge pig metal, ought to yield 4G6 Ibs. of wrought metal, whereas from an ordinary puddling furnace the actual yield would generally amount to only 370 Ibs. (or 12 per cent, less than the charge), showing a difference of 96 Ibs. between the theoretical and actual yield in each charge. This difference, amounting to fully 20 per cent., is due to the enormous waste by oxidation to which the iron is exposed after it has been " brought to nature " (by the removal of the carbon) ; when it is in the form of a granular or spongy metallic mass and during the process of forming it into balls. So great a waste of metal by oxidation seems at first sight almost incredible, but considering the extent of surface exposed in the finely divided puddled mass, it is not at all exceptional, and is in fact almost unavoidable in a furnace of the ordinary construction, maintained as a puddling furnace is, at a welding heat. Many attempts have been made, for example by Chenot, Clay, Renton, and others, to produce iron directly from the purer ores, by reducing the ore in the first instance to a metallic sponge, and balling up this sponge, which is a loose porous mass, somewhat similar to spongy puddled iron, on the bed of a furnace, but all these attempts have failed, simply on account of the great waste of iron, a waste amounting to from 25 to 50 per cent., in balling up the sponge. Indeed, the loss in an ordinary puddling furnace would probably be greater S/A' WILLIAM SIEMENS, F.R.S. 243 than -jit per cent, if the metal were not partly protected from the Hunif by the bath of cinder in which it lies ; for in one instance in which the cinder accidentally ran out of a puddling furnace during the balling up of the charge, leaving the iron exposed to the flame, I found the yield reduced from the average of 413 Ibs. down to 370 Ibs., showing an increased waste of 43 Ibs., or over 10 per cent., due to the more complete exposure of the metal to the oxidizing action of the flame. In order to realize the theoretical result, a sufficient amount of oxides must have been supplied to effect the oxidation of the silicon and carbon of the pig iron, and to form a tribasic silicate of iron (3 Fe 0, Si O3) with the silicic acid produced. The amount of oxide required may be readily ascertained. In taking the expression, Fe3 O4, the atomic weight of which is 3 x 28 + 4 x 8 = 116, while that of the three atoms of iron alone is 8 x 28 = 84, it follows that VV x 4G = G3'5 Ibs. of cinder or oxide of iron are requisite to produce the 4G Ibs. of reduced iron which were added to the bath. There must, however, remain a sufficient quantity of fluid cinder in the bath to form, with the silicon (extracted from the iron), a tribasic silicate of iron, or about 60 Ibs., making in all 1 24 Ibs. of fettling which would have to be added for each charge, a quantity which is generally exceeded in practice notwithstanding the inferior results universally obtained. There remain for our consideration the sulphur and phos- phorus, which being generally contained in English forge pig in the proportion of from '2 to 'G per cent, each, can hardly affect the foregoing quantitative results, although they are of great importance as affecting the quality of the metal produced. It has been suggested by Percy that the separation of these ingredients may be due to liquation. This I understand to mean that the crystals of metallic iron, which form throughout the ailing mass when the metal " comes to nature," exclude foreign substances in the same way that the ice formed upon sea water excludes the salt, and yields sweet water when re-melted. According to this view, pig metal of inferior quality will really yield iron almost chemically pure, to which foreign ingredients are again added by mechanical admixture with the surrounding cinder, or semi-reduced metal. It may be safely inferred that the freedom of the metal from R 2 244 THE SCIENTIFIC PAPERS OP impurities thus taken up will mainly depend upon the temperature, which should be high, in order to ensure the perfect fluidity and complete separation of the cinder. The following was the result of an analysis of an inferior English pig iron before and after being puddled : — PIG METAL. Sulphur Phosphorus . . . Silicon Iron and Carbon (by difference) . . . •08 1-16 1'97 96-79 100-00 PUDDLED BAB. Sulphur Phosphorus . Silicon Iron (by difference) •017 •237 •200 99-546 100-000 showing the extent to which foreign matters are actually removed by the process of puddling. These analyses were made a few days since by Mr. A. Willis in my laboratory at Birmingham. Led by these chemical considerations, and by practical attention to the subject, extending over several years, I am brought to the conclusion that Ihe process of puddling, as practised at present, is extreme!// "wasteful in iron and fuel, immensely laborious, and .yielding a metal only imperfectly separated from its impurities.^ How nearly we shall be able to approach the results indicated by the chemical reasoning here adopted, I am not prepared to say, but that much can be accomplished by the means actually at our doors is proved by the result of the working of a puddling fur- nace erected eighteen months since to my designs by the Bolton Steel and Iron Company in Lancashire. This furnace consists of a puddling chamber of very nearly the ordinary form, which is heated however by means of a regenerative gas furnace, a system of which the principle is now sufficiently well established to render a very detailed description here un- necessary. The general arrangement of the furnace is shown in the accom- panying illustrations. It consists of two essential parts : The gas-producer, in which the coal or other fuel is converted into a combustible gas ; and The furnace, with its " regenerators " or chambers for storing WILLIAM SIEMENS, F.R.S. 245 the waste heat of the flame, and giving it up to the in-coming air •us. The gas-producer is shown in Plate 41, Fig. 1 ; it is a rectangular irk chamber, one side of which, B, is inclined at an angle of in mi •!."> to GO0, and is provided with a grate, C, at its foot. The fuel, which may be of any description, such as coal, coke, lignite, peat, or even sawdust, is filled in through a hopper, A, at the top of the incline, and falls in a thick bed upon the grate. Air is admitted at the grate, and in burning, its oxygen unites with the carbon of the fuel, forming carbonic acid gas, which rises slowly through the ignited mass, taking up an additional equivalent of carbon, and thus forming carbonic oxide. The heat thus produced distils off carburetted hydrogen and other gases and vapours from the fuel as it descends gradually towards the grate, and the car- bonic oxide already named diluted by the inert nitrogen of the air and by any small quantity of unreduced carbonic acid, and mixed with these gases and vapours distilled from the raw fuel, is finally led off by the gas flue to the furnace. The ashes and clinkers that accumulate in the grate are removed at intervals of one or two days. E is a pipe for the purpose of supplying a little water to the ash pit, to be decomposed as it evaporates and comes in contact with the incandescent fuel, thus forming some hydrogen and carl ionic oxide, which serve to enrich the gas ; G is a small plug hole by which the state of the fire may be inspected, and the fuel moved by a bar if necessary ; and D is a sliding damper by which the gas-producer may be shut off at any time from the flue. It is necessary to maintain a slight outward pressure through the whole length of the gas flue leading to the furnaces, in order to prevent the burning of the gas in the flue through the indraught of air at crevices in the brickwork. Where the furnaces stand much higher than the gas-producers, the required pressure is at once obtained ; but more frequently the furnaces and gas-producers are placed nearly on the same level, and some special arrangement is necessary to maintain the pressure in the flue. The most simple contrivance for this purpose is the " elevated cooling tube." The hot gas is carried up by a brick stack, H, to a height of eight or ten feet above the top of the gas- producer, and is led through a horizontal sheet-iron cooling tube, 246 THE SCIENTIFIC PAPERS OP J, (Fig. 1), from which it passes down either directly to the furnace, or into an underground brick flue. The gas rising from the producer at a temperature of about 1000° Fahr., is cooled as it passes along the overhead tube, and the descending column is consequently denser and heavier than the ascending column of the same length, and continually over- balances it. The system forms, in fact, a syphon in which the two limbs are of equal length, but the one is filled with a heavier gaseous fluid than the other. In erecting a number of gas-producers and furnaces I generally prefer to group the producers together, leading the gas from all into one main flue, from which the several furnaces draw their supplies. The puddling furnace, proper, is shown in Plate 41, Fig. 2, and Plate 42, Figs. 3 and 4. Fig. 2 is a sectional plan, and Fig. 3 is a front elevation of the furnace, showing the gas reversing valve and flues in section. Fig. 4, is a longitudinal section. The peculiarity of the regenerative gas furnace, as applied either to puddling, or to any other process in which a high heat is required, consists in the utilization in the furnace of nearly the whole of the heat of combustion of the fuel, by heating the entering gas and air by means of the waste heat of the products of combustion, after they have left the furnace, and are of no further use for the operation being carried on. The waste heat is, so to speak, intercepted on its passage to the chimney, by means of masses of fire-brick stacked in an open or loose manner in certain chambers, called " Regenerator chambers," C, E, E1, Cl, (Fig. 3). On first lighting the furnace the gas pr.sses in through the gas regulating valve, B, (Fig. 2), and the gas reversing valve, B1, and is led into the flue, M, and thence into the bottom of the regenerator chamber, C, (Fig. 3) ; while the air enters through a corresponding " air reversing valve," behind the valve B1, and passes thence through the flue, N, into the regenerator chamber, E. The currents of gas and air, both quite cold, rise separately through the regenerator chambers, C and E, and pass up through the gas and air flues respectively, into the furnace above, where they meet and are lighted, burning and producing a .s/A' WILLIAM SIEMENS, F.R.S. 247 moderate heat. The products of combustion pass away through a similar set of flues at the other end of the furnace into the regenerator chambers, C1, El, and thence through the flues, M1, N ' , and through the gas and air reversing valves, into the chimney flue, 0. The waste heat is thus deposited in the upper courses of open lire-brick work filling the chambers, C1, E1, so heating them up, while the lower portion, and the chimney flue, are still quite cool ; then after about an hour, the reversing valves, B1, (through which the air and gas are admitted to the furnace) are reversed, by means of the levers, P, and the air and gas enter through those regenerator chambers, E1, C1, that have just been heated by the waste products of combustion, and in passing up through the open brickwork they become heated, and then on meeting and entering into combustion in the furnace, D, D, they produce a very high temperature, probably 500° Fahr. higher than when admitted cold ; the waste heat from such higher temperature of combustion heating up the previously cold regenerator chambers, < . K, to a correspondingly higher heat. After about an hour's work the reversing valves, B1, are again reversed, and the air and gas enter the first pair of regenerator chambers, C, E, but which are now very hot, and therefore the air and gas become very hot, and enter the furnace in this state, meeting and entering into combustion, and thus producing a still higher temperature, probably 500° higher still, and again heating the second pair of regenerator chambers, C1, E1, so much higher, which enables them to again heat the air and gas to a still higher degree, when the valves, B1, are again reversed. Thus an accumulation of heat and an acces- sion of temperature is obtained, step by step, so to speak, until the furnace is as hot as is required ; for unless cold materials are put in to be heated, and thus abstract heat, the temperature rises as long as the furnace holds together, and the supply of gas and air is continued. The heat is at the same time so thoroughly abstracted from the products of combustion by the regenerators that the chimney flue remains always quite cool. The command of the temperature of the furnace and of the quality of the flame is rendered complete by means of the gas and air regulating valves shown at B in Fig. 2, and by the chimney damper. These are adjusted to any required extent of opening by the notched rods, Q , R, and S, (Fig. 2,) respectively, so that having the power of 248 THE SCIENTIFIC PAPERS OF producing as high a temperature as can be desired, there is also the power of varying it according to the requirements in each case. The bed of the furnace, D, D, is of the ordinary construction, formed of iron plates, and is provided with water bridges at the ends, as shown, to protect the " fettling," (or oxide of iron used for lining the furnace) from being melted away. The overflow from one of the water bridges is led into a sheet-iron tank below the bed, and then away. The evaporation from this tank keeps the bottom plates cool and preserves the cinder covering them from melting off, and the steam is carried away by a draught of air entering through two holes I, I, (Fig. 3), below the tap hole, and passing off by small ventilating shafts at the back of the furnace. A heating chamber, H, is arranged at each end of the furnace, in which the charge of pig iron may be heated to redness before it is introduced into the puddling chamber, D, D. The advantages of this furnace, for puddling, arc that the heat can be raised to an almost unlimited degree ; that the flame can be made at will oxidizing, neutral, or reducing, without interfering with the temperature ; that in-draughts of air and cutting flames are avoided ; and that the gas fuel is free from ashes, dust, and other impurities, which are carried into an ordinary puddling furnace from the grate. In this last respect the new furnace presents the same advantages as puddling with wood. The following tables give the working results which were obtained from this furnace, as compared with the results obtained at the same time in an ordinary furnace from the same pig (the ordinary forge mixture) : SIR WILLIAM SIEMENS, l-.R.S. 249 TABLE I. REGENERATIVE GAS FURNACE. l>:it,-. Not. of BMta, Time charged. First Ball out. If eta] charged. Yield. 1867. FIHST SHIFT. n.s. iks. May 27 1 .V2.~, 6-32 410 392 2 8-48 7'BO 433 3'.l<; 3 8-8 '.HI 4:50 410 4 '.)•!.-, 10-7 I:.':. 426 .") 10-20 11-22 126 430 6 11-40 12-46 412 412 SECOND SHIFT. May 27 1 1-48 2-47 428 410 2 2-:.0 3-47 420 414 3 3-56 (•:,:; 426 418 4 5-0 <;-3 432 417 5 6-5 7-12 425 407 6 7-20 8-15 420 422 THIRD SHIFT. May 27 1 9-1U 10-15 423 414 2 10-25 11-30 422 412 3 11-3.-) 12-40 420 420 4 12-45 2-0 430 410 5 2-10 3-10 424 418 6 3-16 4-20 420 400 FIEST SHIFT. May 28 1 5-38 6-45 423 402 2 6-50 8-0 422 400 3 8-6 9-8 430 390 4 9-15 10-28 426 407 5 10-35 11-45 426 420 6 11-68 1-8 430 416 SECOND SHIFT. May 28 1 2-0 3-1 422 422 2 3-6 4-0 424 415 3 4-5 5-18 423 424 4 B-28 6-27 4i?3 415 5 fi-33 7-46 427 420 6 7-49 8-50 490 406 THIRD SHIFT. May 28 1 10-0 11-20 420 424 2 11-25 11-33 420 410 3 12-40 1-45 423 412 . 4 1-50 2-58 425 420 5 3-13 4-20 430 418 6 4-30 5-35 422 426 Cwt. qrs. Ibs. Total charge 130 1 2 „ yield 132 3 7 Being at the rate of . . . 20 2 2 of pig iron per ton of puddled bar. 250 THE SCIENTIFIC PAPERS OF TABLE II. ORDINARY FURNACE. Date. Time. Weight of Metal charged. Weight of Puddled Bar produced. Ibs. 1867, ,C T3 424 May 17 o 2 425 405 «H d, 430 £ 430 v £ 438 43 If 3 416 -u m 456 §8 oo 410 J3 "* 432 | M . § 426 pe*« S M 420 "S ° 422 a ^ 03 0) 450 H 410 1V.D Mean charge 484 „ yield 426 or 22 cwt. 2 qrs. 20 Ibs. of pig iron per ton of puddled bar. It will be observed that the ordinary furnace received charges of 484 Ibs. each, and yielded on an average 426 Ibs., representing a loss of 12 per cent., whereas the gas furnace received charges averaging 424 Ibs., and yielded 413 Ibs., representing a loss of less than 2'6 per cent. It is important to observe, moreover, that the gas furnace turned out eighteen heats in three shifts per twenty-four hours, instead of only twelve heats per twenty-four hours, which was the limit of production in the ordinary furnace. This rate of working was attained without the employment of any arrangement for heating the pig iron before charging it into the furnace, the heating chambers at the ends not having been used. The adoption of the plan of heating the metal beforehand, a system already extensively in use both in this country and on the Continent, effects a further saving of ten to fifteen minutes in the time required for working each charge, as well as a considerable economy in fuel. The quality of the iron produced from the gas furnace was A/A' WILLIAM SIEMENS, F.R.S. 251 proved decidedly superior to that from the ordinary furnace, being what is technically called " best best " in the one, and " best" in (lit; other case, from the same pig. The economy of fuel was also greatly in favour of the gas furnace, but could not be accurately ascertained because some mill furnaces were worked from the same set of producers. Still, judging from the experience of several years, in the working of regenerative gas furnaces as re-heating or mill furnaces, and as glass furnaces, the saving of fuel in puddling cannot be less than 40 to 50 per cent, in quantity, while a much cheaper quality may be used. The consumption of " fettling " was, however, greater in the gas furnace, and the superior yield was naturally attributed by the forge managers to that cause, although the writer held a different opinion. The gas furnace, however, had not been provided with water bridges, these were subsequently added, and the furnace put to work again in February last, since which time it has been worked continuously. The result of the water bridges has been that the amount of "fettling" required is reduced to an ordinary proportion, the average quantity of red ore used being l)2'G Ibs. per charge, be- sides the usual allowance of bull dog, while the yield per charge of 483*3 Ibs. of grey forge pig has been increased to 485 Ibs. of puddled bar, as shown by the following return of a series of eighty consecutive charges in June last : TABLE 111. EEGENERATIVE GAS FURNACE. Date. No. of Heats. Total Charges and Yields. j ^ ^ Ibs. cwt. qrs. Ibs. Ibs. June, 1868 80 Pig iron charged .38,668 = 345 1 0 4S.S-3 Puddled bar returned . 38,808 = 346 1 25 186 Red ore for "fettling" 7,406=66 014 92-6 proving that the yield of puddled bar slightly exceeds the charge of pig metal (representing a saving of fully 12 per cent, over the ordinary furnace), while the superiority of quality in favour of the gas furnace is fully maintained. It is also worthy of remark that these results are obtained regu- 252 THE SCIENTIFIC PAPERS OF larly by the ordinary puddlers of the works, and that no repairs have been necessary to the gas puddling furnace since November last, the roof being reported to be still in excellent condition. In these investigations I have confined myself to the puddling of ordinary English forge pig in order to avoid confusion, but it is self-evident that the same reasoning also applies in a modified degree to white pig metal or refined metal, the use of which I should not, however, advocate. WATER BRIDGES. — Regarding the water bridges, I was desirous to ascertain the expenditure of heat at which the saving of "fettling" and greater ease of working was effected. The water passing through the bridges was accordingly measured by Mr. W. Hackney (who has also furnished me with the other working data) and found to amount to 25 Ibs. per minute, heated 40° Fahr. This represents 60,000 units of heat per hour, or a consumption not exceeding 8 Ibs. to 10 Ibs. of solid fuel per hour, an expenditure very much exceeded by the advantages obtained where water or cooling cisterns are available. The labour of the puddler and of his underhand being very much shortened and facilitated by means of the furnace, I should strongly recommend the introduction of three working shifts of 8 hours each per 24 hours, each shift representing the usual number of heats, by which arrangement both the employer and the employed would be materially benefited. The labour of the puddler may be further reduced with advantage by the introduction of the mechanical " Rabble " which has already made considerable progress on the Continent. By working in this manner, a regenerative gas puddling furnace of ordinary dimensions would produce an annual yield of about 940 tons of bar iron, of superior quality, from the same weight of grey pig metal and the ordinary proportion of " fettling." In conclusion, I may state that a considerable number of these puddling furnaces have been erected by me abroad, and that, in this country, they are also being taken up by the Monkbridge Iron Co., Leeds, and a few other enterprising firms. The construction of these furnaces has been still further improved lately by the application of horizontal regenerators, to save deep excavations, and by other arrangements whereby the first cost is diminished and the working of the furnace facilitated. .S/A' WILLIAM SIEMENS, b.R.S. 253 TABLE IV. K.VTAQE OP CAKUON AND SILICON CONTAINED IN VARIOUS KINDS or CA-T AND WROUGHT IKON AND STKKL. Description. Carlxm. Silicon. Authority. per cent. per cent. :i (New Jersey, U.S.) . 6-900 0-100 II«'iiry. ,. (German) . . . . 5-440 0-179 Schafhautl. „ (MtUen) .... 4-H23 ()-!l'.)7 l-'ivMjnius. i pig iron (Danncmora, Sweden) . 4-809 0-176 Henry. (iivv pig iron, No. 1 (Tow Law) . . 2-708 4-414 Riley. Uivy pig iron, No. 1 (Acadian Iron Co.) 3-500 4-840 Tookey. Grey foundry pig iron, No. 1 (Ne- 1 therton, South Staffordshire) . / 3-07 1-48 ( Woolwich ( Arsenal. Ditto Ditto, No. 2, ditto. . . 3-04 1-27 » Grey forge pig iron, ditto 3-12 i-i6 »» Forge pig iron, ditto . . . 3-03 0-83 » Strong forge pig iron ditto 2-81 0-57 » Grey pig iron (Dowlais) . . . . 3-14 2-16 Riley. Mottled ditto, ditto 2-95 1-96 <» White ditto, ditto .... 2-84 1-21 n Mottled pig iron (Wellingborough) 2-10 2-11 ( Woolwich \ Arsenal. White pig iron (Bloenavon) . . . 2-31 Ml Percy. Refined iron (Bromford, a. Stafford- \ shire ) 3-070 0-630 Dick. Puddled steel, hard (Kbnigshiitte) . . 1-380 •006 Brauns. Ditto ditto, mild (South Wales) •501 •106 Parry. Cast steel, Wootz 1-34 Henry. , for flat files. 1-2 A. Willis. , (Huntsman's) for cutters . 1-0 ! , for chisels .... •75 . . . , die steel (welding) . . . •74 , double shear steel •7 quarry drills . . . . •64 masons' tools •6 • . • , spades •32 , railway tyres •32 to -27 . • . . rails •26 to -24 , plates for ships . •25 Various. , very mild . . . \ , (melted on open hearth) / •18 A. Willis. Hard bar iron (South Wales) . . . •410 •080 Schafhautl. „ „ (Kloster, Sweden) . •386 •252 Henry. (Russia) . . . . •340 Trace » ,, ., },.... •272 •062 >t Boiler plates (Russell's Hall, South \ •i 'ii i .111 Staffordshire) . . . . j" iyu Jlvv » Armour plates (Weardale Iron Co.) 1 too steely J •170 •110 Percy. Bar iron (Lb'fsta, Sweden) 087 •115 Henry. „ (Gysinge, Sweden) . •087 •066 )> „ (Osteriiy, Sweden) •054 •028 ii Armour plates (Beale & Co.) •044 •174 Percy. ,. „ (Thames Iron Co.) . •033 •160 ii .. „ (Low Moor) . •016 •122 Tookey. 254 THE SCIENTIFIC PAPERS OF MR. SIEMENS said he quite agreed with most of the remarks that had been made. Mr. Bram well's way of putting the loss of iron was quite correct, and if ever the puddling process was brought to an absolute state of perfection the saving would in some cases be 20 per cent, instead of only 12 per cent, as at present. Undoubtedly what was saved in weight, was due to the improved chemical action, as named by Mr. Hawksley and Mr. Mallet, and he was glad to find that his explanation of the theory of puddling was so readily appreciated, both by chemists, in Section B, where his paper had also been read, and by engineers. In working it out he admitted at once that he had had the benefit of special advantages, by being able to exclude nearly all free oxygen whilst he was working with a very high temperature, much higher indeed than usual. In answer to Mr. Mallet's remark as to the use of the new furnace for other metals, he might say it was now being used for zinc, lead, and other ores, with great success. He was happy to be able to relieve Mr. Jones's mind of the impression that the furnace cost £3,000 ; the cost of a pair of puddling furnaces and their gas producers was £450, or £225 per puddling furnace complete. Caking coal, brown coal, free burning coal, and peat, &c., &c., had been in daily use for years in the gas producers with excellent effect, indeed the arrangement offered a means of utilising for operations requiring high temperatures, several descriptions of fuel that had never been used for the purpose before. He certainly did not heat the boilers in a mill with the waste heat from the puddling furnaces, simply because he had no " waste heat " to throw away ; all he made he used, and for the highest or best paying purposes. With regard to the last objection that had been raised, he was happy to say he had not found any diffi- culty with the workmen, they had, in fact, after a few days' work at the furnace, taken to it very well indeed ; he was sorry to say that it was with the masters only that he had any trouble, and he simply mentioned it as the contrary had been stated, but without the intention of finding fault with ironmasters, who would no doubt soon see that what was chemically right, and practicable, must also prove remunerative to themselves. He would only add one word in explanation of the quality A/A' WILUAM SIEMENS, F.R.S. 255 obtained, in reference to the remarks made by Mr. Cowper, Mr. Kolm, and Mr. Hackney ; Mr. Kohn said the silicon might burn out on the surface of the melted metal, but he thought that tin- experiments he had produced clearly indicated that both the silicon and the carbon in the cast metal were oxidized by the oxygen contained in the fettling. He begged to say that he had not the slightest idea of suggesting that pig iron containing large quantities of silicon was preferable ; he preferred the best, as every ironmaster did, but had given the effects of a furnace on a bad sample of iron as a severe test of its powers. There was no doubt that the practical improvement in the quality of the iron produced in his furnace was due, as Mr. Cowper had stated, partly to a mechanical cause and partly to a chemical one, for the purer flame of the furnace did far less injury to the iron, and the higher temperature at which the metal was balled up without being burned, caused the cinder to be so much more fluid, as to run out better from the iron when squeezed, hammered, or rolled, thus excluding more thoroughly those bad welds, " blacks " and " greys," so plentiful in ordinary iron. In the discussion of the Paper, and the Supplementary Paper, "ON THE FURTHER UTILISATION OF THE WASTE GAS FROM BLAST FURNACES, AND THE ECONOMY OF COKE DUE TO INCREASED CAPACITY OF FURNACE," by MR. CHAELES COCHRANE, of Dudley, MR. C. W. SIEMENS* said he had listened with great pleasure to the paper, combining as it did practical experience with theo- retical considerations ; and as regarded the chemical part of the question the arguments advanced seemed to be based upon correct * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers, 1869, pp. 33-36, 39, 42-43, 62-68. 256 THE SCIENTIFIC PAPERS OF chemical proportions, although there was one of the • conclusions arrived at that he could not agree with. In reference to the plan of closing in the charging hopper at the furnace top with the additional covering now described, there could be no doubt that a saving of gas must be thereby effected ; and although at first glance it might be thought that the amount of this saving would not be anything material, as the time that the furnace top was open on each occasion of charging seemed only momentary, it appeared from actual observation that this time of opening really amounted altogether to as much as 1-1 6th of the whole time of working of the furnace, representing a loss of l-16th of all the gas evolved from the furnace. At the same time this loss was attended with the additional objection of interruption in the flow of gas to the boiler fires and hot-blast stoves where it was employed for heating purposes ; and it was a decided advan- tage that these interruptions were now entirely obviated by the double closing of the furnace top. With regard to the theoretical minimum consumption of 1\ cwt. of coke in the blast furnace for the reduction of 1 ton of iron from the ore, it was certainly true that, with an ironstone containing 40 per cent, of iron, 6| cwt. of carbon would suffice to reduce 1 ton of iron from the ore by combining with the oxygen con- tained in the ore, and 1 cwt. of carbon in addition would be more than sufficient for the carbonisation of the iron, making the 1\ cwt. of carbon per ton of iron ; but he did not see that sufficient heat could then be produced by the combustion of that reduced quantity of carbon in the furnace. Moreover he did not consider that it would be possible in practice to attain to this theoretical minimum consumption of coke by any addition to the height of the blast furnace. A small additional amount of heat might indeed be absorbed from the waste gas by raising the furnaces still higher than at present, but this process could not go on indefinitely, and there would still be a certain surplus of heat that would escape ; because the combustion of coke by atmos- pheric oxygen that was necessary to effect the fusion of a given quantity of reduced ore at a high temperature must always leave a certain margin of heat available for reducing and heating the incoming ore. Moreover as the incoming ore was limited in quantity and possessed only a limited capacity for heat, it followed SIR WILLIAM SIEMENS, F.R.S. 257 that even if it were a perfect conductor of heat and presented an unlimited extent of surface for absorbing the heat from the gas, thnv would still be a certain amount of heat that would escape at the furnace top ; and in increasing the height of the furnace, a neutral point would speedily be reached, beyond which no further increase of height would produce any further absorption of heat, for the reason that the quantity of ore charged could not on the average exceed the quantity of ore smelted during the same interval of time, and its relative capacity for heat could not be increased by an augmentation of heat-absorbing surface. The saving consequent upon increased capacity of the blast furnace would continue to increase until a certain minimum consumption of fuel was reached, but this would not be the theoretical minimum assigned by chemical calculations. The ore could not do more than take up a certain amount of heat from the gas ; and sup- posing that its capacity for heat were sufficient to reduce the temperature of the gas down to 500° or 400°, that would be the temperature at which the gas must then escape; and no further saving would be possible. If the relative quantity of ore that could be charged into the furnace were indefinitely great, then indeed the escaping gas could be cooled down as low as the temperature of the external atmosphere ; but inasmuch as the quantity of ore charged into the furnace top was the same as the quantity smelted in the lower part of the furnace, this ore could not absorb more than a certain maximum quantity of heat, and all the surplus heat in the waste gas must escape. There was also the further question whether with anything like such a small proportion of coke a sufficient temperature could be obtained in the furnace to ensure the perfect fusion of the ore : for this pur- pose an infinitely high temperature of blast would be requisite, but with a blast at only 1000° temperature it would certainly be impossible to attain to anything like the theoretical minimum consumption, which left no margin at all of extra carbon for pro- ducing the heat required for smelting the ore ; and it must be borne in mind that the mere transfer of oxygen from the ore to the carbon was not attended by any evolution of heat, but by an absolute absorption of heat. Mr. C. W. Siemens did not understand how the temperature of VOL. i. s 258 THE SCIENTIFIC PAPERS OF the escaping gas could be independent of the rate of driving of the furnace, unless an excess of heat-absorbing surface had been provided ; because with a greater rate of driving, a given extent of surface would then be called upon to absorb a greater quantity of heat in the same time. When the extent of cooling surface of the materials was so proportioned as to reduce the temperature of the escaping gas to a certain degree, short of the ultimate attain- able point, only a small further quantity of waste heat would be absorbed by passing a greater quantity of gas over the same amount of surface in the same time, and the consequence would be that the gas would escape hotter ; just as, in the case of a steam boiler, a small extent of boiler surface caused a hot chimney. This question however was independent of the chemical advantages that might be obtained by hard driving. Mr. C. "W. Siemens thought the illustration suggested of the firebrick regenerator in the hot-blast stoves was not a parallel case, because the area of cooling surface of the firebrick in the regenerator was practically unlimited, on account of the means afforded of reversing the direction of the current through the regenerator as often as desired, whereby the points of maximum and minimum heat might virtually be separated by any distance required. There was no means of taking up a greater quantity of heat from the escaping gas in the blast furnace, because there was only a limited quantity of material, which was heated by a fixed quantity of gas ;• for although in any particular quarter of an hour it might be possible to fill in more material than corre- sponded to the average rate of smelting, yet in the course of a week the total quantity of ore put in was exactly the quantity smelted ; and for absorbing the extra heat generated in smelt- ing 1 cwt. of ore at the bottom of the furnace it was not possible by any means whatever to add more than 1 cwt. of fresh ore at the furnace top, with the proportionate quantity of the other materials. Mr. C. W. Siemens remarked that at the previous meeting, while appreciating the value of the facts brought forward in the paper then read, he had been unable to agree with the conclusion WILLIAM SIEMENS, F.R.S. 259 arrived at as to the quantity of coke that should be sufficient for smelting a ton of iron in a blast furnace having a capacity carried to the ultimate limits then indicated. The 7i cwts. of coke per ton of iron, which had been originally named as the theoretical minimum consumption, represented no more than the carbon necessary for combining chemically with the peroxide of iron or i ah- i ued ore, and for carbonising the reduced metal so as to bring it into the state of ordinary pig iron ; and the idea that it would be theoretically possible, by any increase in the capacity of the blast furnace, to bring down the consumption of coke to that amount, arose from the error of taking a simple arithmetical progression to represent the saving of coke consequent upon successive additions to the size of the furnace. In the supple- mentary paper now read however, an amended calculation had been offered, by taking into account the reduced capital, that is the reduced quantity of coke in the larger furnaces, upon which the percentage of saving had to be estimated ; so that the same percentage of saving, out of a total consumption which was diminished by each successive addition to the capacity of the furnace, represented a less and less absolute saving as the size of the furnace was increased. In this way, considering only the question of abstracting the heat from the escaping gas, the result now arrived at had been that 17'9 cwts. of coke per ton of iron was the limit of minimum consumption that could be attained by simply adding to the height of the furnace, ftb account however had been taken of the chemical work that had to be constantly performed within the blast furnace ; and moreover the additional quantity of heat that could be taken up from the gas by merely adding more material in the furnace top would be found, he considered, to be a very small amount. For although he had shown that, by means of the regenerative system, with a quantity of cooling material relatively very much smaller than was con- tained in a blast-furnace top, it was quite practicable to take up the heat from the outgoing current down to within 20° or 30° of the incoming draught, yet this was only the case so long as the two opposite currents were equal in the amount of their total capacity for heat ; but if the current passing in one direction through the regenerator had a different total capacity for heat from that passing in the opposite direction, then whatever extent s 2 260 THE SCIENTIFIC PAPERS OF was given to the cooling material or regenerator, equilibrium would never be established, and it would not be possible to cool down the escaping current to the temperature of the entering draught ; or, applying this argument to the case of the blast furnace, it would not be possible to cool down the escaping gas to the temperature at which the fresh materials were charged into the furnace, owing to the inferior total capacity for heat of the latter. With regard to the amount of chemical work which was required to be performed in a blast furnace for smelting a ton of iron, he had made a calculation, the results of which it might be interest- ing to compare with those that had been arrived at by adapting to the Cleveland furnaces the investigations of the foreign writers referred to, whose researches upon the subject he had not previ- ously been acquainted with. In the case of Cleveland ironstone containing 40 per cent, of metallic iron in the calcined ore, the iron being in the state of peroxide had 17 per cent, of oxygen combined with it, and the remaining 43 per cent, of the ore would be silica. To fuse this 43 per cent, of silica, which was equal to 21| cwts. per ton of iron made, 7 cwts. of calcined limestone would theoretically be required, but in reality he believed 8 or 9 cwts. of limestone was the quantity generally added in the Cleve- land district ; these would take up about 2| per cent, of iron, giving a total of about 31 cwts. of cinder per ton of iron made. The 17 per cent, of oxygen combined with the 40 per cent, of iron in the ore was equivalent to 8'50 cwts. of oxygen per ton of iron, and this would require 5 '31 cwts. of carbon to produce the mixture of f ths carbonic oxide and ^th carbonic acid which he believed actually resulted from the chemical reactions in the furnace ; for although it had been calculated in the paper that the proportions in which these two gases passed off at the furnace top were about frds carbonic oxide to |rd carbonic acid, he thought the difference should be allowed for the amount of carbonic acid evolved from the limestone, and that there would therefore be no material error in assuming the result of the combustion to be -f-ths carbonic oxide and ^-th carbonic acid. The heat necessary to be produced in the blast furnace was therefore that required for performing the three distinct opera- tions of melting the iron itself, melting the cinder accompanying S/A WILLIAM SIEMENS, F.R.S. 26 1 the iron, and generating into a gaseous form the fixed oxygen in the ore and the fixed carbon in the coke, so as to allow of their chemical combination taking place. Considering first the heat n in i red for melting the iron — taking the total heat developed in funning carbonic oxide as 4000 Fahr. units, and in forming car- bonic acid 14,000 units — the combustion of 1 Ib. of carbon into the mixture of -Jths carbonic oxide and |th carbonic acid would develope 6000 Fahr. units of heat ; and therefore— taking the specific heat of iron at 0*12 in comparison with water, and assuming the temperature to which the melted metal was heated (including its latent heat) to amount to 4000° Fahr. — it would be „ . . , 20x4000x0-12 found that to melt 1 ton of iron required — 1*60 6000 cwts. of carbon. This estimate was evidently on the safe side, as no account was taken in it of the further heat necessary for keep- ing the iron melted in the hearth till casting time, which would have raised the quantity of carbon nearer to the estimate of 2*70 cwts. given by Mr. Bell. The 1*60 cwts, received a satis- factory confirmation from actual results which he had obtained in the working of cupolas, showing that the calculation was sub- stantially correct. Next with regard to the cinder, taking its specific heat at 0'20, which he believed was below the mark, and assuming the total heat for melting it to be the same as that for iron, namely 4000° Fahr., it would be found that the melting of 31 cwts. of cinder per ton of iron made would require 31 x 4000 x 0-20 = 4.13 cwtg Qf carbon In reference to the third 6000 supply of heat required in the blast furnace — for transforming into a gaseous state the fixed oxygen in the ore and the fixed carbon in the coke — it must not be overlooked that in the combi- nation of carbon with oxygen, heat was only evolved in conse- quence of a reduction of volume occurring, and in proportion to the extent of that reduction of volume. But this could only take place when both bodies were already in a gaseous state ; and accordingly by the combination of solid carbon with gaseous oxygen in the proportion of one equivalent of each, producing carbonic oxide, the amount of sensible heat evolved (4000 units) •was less than half of that (10,000 units) which was further developed when a second equivalent of oxygen entered into com- 262 THE SCIENTIFIC PAPERS OF bination with the gaseous carbonic oxide so as to form carbonic acid ; because more than half of the total heat developed in the formation of the carbonic oxide (6000 out of 10,000 units) was rendered latent by the solid carbon having first to be volatilised before it could combine with the oxygen. The absorption of latent heat was necessarily still greater when the fixed oxygen in the ore had to be made to enter into combination with the fixed carbon in the coke, because a supply of heat had first to be absorbed sufficient for volatilising both the fixed oxygen and the solid carbon ; and he had found practically that, where a mixture of ore and carbon was exposed in a close retort to the heat of a furnace, it was necessary to supply a large amount of heat in order to bring about a combination of the elements. In the com- bination of the 8'50 cwts. of oxygen of the ore in the blast furnace with the 5'31 cwts. of carbon of the fuel, two processes of opposite effect had to take place : on the one hand, the combustion of the carbon into the final mixture of |-ths carbonic oxide and ^th car- bonic acid, developing 6000 Fahr. units of heat per Ib. of carbon, would give a total of 5'31 x 112 x 6000 = 3,568,320 units of heat developed ; but on the other hand, the volatilisation and separation from the iron of the fixed oxygen of the ore required the absorp- tion as latent heat of, he believed, not less than 6000 Fahr. units of heat per Ib. of oxygen, and the total absorption of heat thus occasioned would amount to 8'50 x 112 x 6000 = 5,712,000 units of heat absorbed. The difference 2,143,680 units, being an excess of heat absorbed, required therefore to be compensated by an extra consumption of 2'143'68Q = 357 Ibs. or 3'19 cwts. of carbon. 6000 These three amounts added together gave 1'60 + 4'13 + 3'19 = 8'92 cwts. of carbon, to which had to be added the 7 '43 cwts. required for chemical combination with the oxygen in the ore and for carbonising the pig metal, making 16'35 cwts. of pure carbon. A further addition was required of 10 per cent, or 1'63 cwts. for ashes and water in the coke actually employed in the blast fur- naces ; and also another 10 per cent, or T63 cwts. for effecting the calcination of the limestone and completing that of the ore, and to allow for vaporising the moisture in the materials and for loss by radiation. The total amount was thus brought up to 19' 61 cwts. as the theoretical minimum consumption of coke SfK WILLIAM SIEMENS, F.R.^ 263. necessary for the smelting of ono ton of iron. The complets con- Kiiiii|itiini was therefore as follows : — Cwte. Melting tin; iron 1'Ou Melting the cinder 4'18 Meat rendered latent by reduction of the ore 3'19 Carbon for combining with oxygen in ore and for carbonising pig metal . . 7'43 16-35 Ashes and water in the coke, 10 per cent. . . 1'63 Calcining the limestone, &c., 10 per cent. . . l'G3 Total quantity of coke required . . 19-61 cwts. In this calculation he had left out of consideration on the one hand the heat that was carried off from the furnace by the escaping gas, and on the other hand the heat brought into the furnace by the hot blast entering at 1000° Fahr. ; but on comparing these two quantities of heat it would be found that they balanced each other very nearly indeed. For the 8"9 2 cwts. of carbon made up by the first three items in the foregoing estimate would require, in order to produce blast-furnace gas consisting of fths carbonic oxide and |th carbonic acid, 14' 2 7 cwts. of oxygen, which would be contained in 62*04 cwts. of atmospheric air entering as hot blast ; while on the other hand the gas escaping at the furnace top would contain the whole of these 8'92 cwts. of carbon and 62'04 cwts. of air, together with the 8'50 cwts. of oxygen existing in the ore and the 5'31 cwts. of carbon supplied into the furnace to combine with it, making altogether 84'77 cwts. of gas, to which had to be added about 10 per cent, or 8*47 cwts. of carbonic acid and vapour of water generated from the limestone and other materials, thus making up a total weight of 93'24 cwts. of gas escaping from the furnace top, in the form of carbonic oxide, carbonic acid, and nitrogen mixed together. Assuming the tem- perature of this escaping gas to be 600° Fahr. and the specific heat of the mixture to be the same as that of air or 0*267, the total quantity of heat thus carried off from the furnace would be 93-24 x 112 x 600 x 0'267 = 1,672,949 units of heat per ton of iron made ; and at the same time the heat brought into the furnace 264 THE SCIENTIFIC PAPERS OF by the 62'04 cwts. of hot blast at 1000° Fahr. would be 62'04 x 112x1000x0-267 = 1,855,244 units of heat, leaving a small excess of 182,295 units of heat brought in by the blast per ton of iron made, which was probably not more than would cover the loss of heat by radiation from the furnace. The actual work done in one of the Cleveland blast furnaces represented therefore a consumption of between 19 and 20 cwts. of coke per ton of iron made, supposing the ironstone to contain only 40 per cent, of iron when calcined, and the blast to be delivered into the furnace at a temperature not exceeding 1000° ; and under these conditions he believed no blast furnace could be constructed to work with less than that quantity of coke, although with richer ores and higher temperatures of blast there would of course be a considerable margin for further economy in consumption of coke. Practically speaking he thought that 22 cwts. of coke per ton of iron made would be the best result that would be obtained under these circumstances ; and this would be independent of the capacity of the furnace, which might be increased indefinitely without improving upon this estimated minimum consumption. In the discussion of the Paper " ON THE DEVELOPMENT OF HEAT, AND ITS APPRO- PRIATION IN BLAST FURNACES OF DIFFERENT DIMENSIONS," by I. LOWTHIAN BELL, ME. C. W. SIEMENS,* who was received with applause, said : I have listened with great interest to this paper, which, founded on practical information, deals with blast furnaces as an economi- cal question. I think, in all operations, we should endeavour to look at the ultimate results we might possibly obtain, and * Excerpt Journal of the Iron and Steel Institute, 1869-70. pp. 124-125 and 220-222. WILLIAM SIEMENS, F.K.S. 265 then try, in practice, to approach these results by the best means we can think of. The question of the chemical economy of the blast furnace was discussed, as Mr. Bell will remember, at Bir- mingham, some time ago ; and, in arguing the point, I disagreed with some of the speakers on the great results which might be expected from the mere increase of capacity. I could not see that this capacity, when it had attained a certain limit, could be bene- ficial as a mere absorber of heat in order to increase materially the economy of the furnace. I am glad to see Mr. Bell's elaborate investigations on the subject have caused him to take the view he has explained to us. At the discussion in Birmingham I ventured to state the minimum consumption of coke in a blast furnace in dealing with ore of a certain chemical composition. Mr. Bell, in giving the results of his investigations, based partly upon theoreti- cal grounds, comes to a conclusion — and although the two inves- tigations are totally distinct, for we view the question from different points of view — the results we arrive at are the same within a fraction. I came to the conclusion that the minimum quantity in smelting Cleveland ore would be 21 cwts., and Mr. Bell's calculation comes to within 1 cwt. of that figure. This coincidence of result is, I think, the best proof that can be brought forward of the correctness of that view of the case. At this meeting we have had the whole question much more thoroughly brought before us, and I think the paper will remain a standard paper on the subject. Mr. Bell made one very valuable suggestion with regard to the carbonization of iron in the blast furnace. He has discovered that iron ore absorbs carbon, and the amount of absorption pro- bably rules the " number " of the pig metal produced. That is a new view of the question and a very interesting one. I, myself, have great belief in that view ; it will serve to explain many apparent anomalies. The next question — that of hot blast — I am not so well prepared to agree with him. No doubt Mr. Bell has viewed the question very maturely, and I hesitate to differ from him with regard to results. But still, in viewing the question from a different point, I would come to a conclusion different from that of Mr. Bell, and probably, on comparing the ways, the result that we will arrive at may, perhaps, in some degree modify the figures placed before us at this meeting. Mr. Bell shows that by increasing the blast beyond the ordinary limits of 600°, it 266 THE SCIENTIFIC PAPERS OP affects the economy in a very slight degree. My view is, that ifc would affect it very nearly in the same degree as an increase from 60° to 000° would affect it. I come to this conclusion for this reason. I view the general result of combustion in the blast fur- nace, and compare it with the general result of combustion in the heating stove. In the heating stove, you burn fuel into carbonic acid, and for every pound you burn, 13000 Fahr. units are evolved. This amount of heat absorbed by the air is carried into the blast furnace. Now, the action of the blast furnace — the combustion carried on there — is accomplished in a very different way. The quantity of heat imported into the blast furnace counts for more than double that expended in the heating stove. Considering that the capacity and the specific heat of the air at the higher and lower temperature is the same within a fractional amount, for every degree Fahr. by which the temperature of blast is increased, a proportionate amount of stone ought to be taken into the blast furnace. As Mr. Bell admits that by increasing the temperature of the blast he gets a higher proportion of carbonic acid at the top of his blast furnace, he admits that the effect will be an increase in ratio. In the measure in which you increase the temperature of the blast, the amount of carbonic acid at the top of the blast furnace will augment, and the gas at the top of the blast furnace will diminish in volume. I am satisfied that an increase in the temperature of the blast must be highly economical in the results of the furnace. In the adjourned discussion of tJie same Paper MR. C. W. SIEMENS said : With regard to the question raised by Mr. Cochrane, I think I may be able to throw some light upon it by putting it in this way. If Mr. Cochrane finds the gases escape at 700° at the top, and if he was then to throw in a load of ironstone, he would, no doubt, effect a temporary reduction of that temperature ; but long before a corresponding amount of ore was smelted to make room for a further charge, the temperature of the escaping gases would have risen again to 700° or rather more. In order to arrive at real temperature of issue, the ore should be fed, or supposed to be fed, in a continuous manner ; although, for the purpose of experiment, you can put in a heavy charge A/A' WILLIAM SIEMENS, F.R.S. 267 suddenly and effect a temporary reduction of temperature in that manner. With regard to that point of your paper, sir, on which I took the liberty of differing from you at the last meeting, I must say that I still hold that the increase of temperature in the blast would produce a beneficial result, and the beneficial result would rise fully in the proportion of the increase of temperature. I think the chief point of difference between us on that occasion was, that you, Mr. Chairman, referred the result to a unit quantity of ore, whereas, I referred it to a unit quantity of blast ; and I cannot help thinking that the latter is the correct way of taking it. The quantity of heat supplied depends upon the temperature to which we heat the blast ; and if I can show that, for every unit of heat added to the blast, you produce an equal saving of heat in the blast furnace, then, I think, it is proved that increase of temperature benefits you to an unlimited extent. But I would go farther, and say that the benefit goes on in an increasing ratio ; and I think we can show it from the facts which you have brought before us in so complete a manner. Your own figures prove that the higher the temperature of the blast, the lower is the temperature at which the gases issue from the top of the furnace. Therefore, this is no longer a question of a certain bank of heat which you can draw upon to the extent of its debit and no more ; but your bank of heat is an increasing one, because, in the first place, the gases escape at a lower degree of temperature, and, in the second place, the higher the temperature of the blast, the greater is the proportion of carbonic acid es- caping from the furnace ; which signifies that more heat is gene- rated within the blast furnace, inasmuch as every pound of fuel burnt into carbonic acid produces, roughly speaking, three times the number of units than is the case when carbonic oxide is pro- duced. These are two reasons, therefore, why the bulk of heat is very much increased by raising the temperature of the blast. Tlie Chairman. You are now referring to the Consett furnaces. Mr. Siemens. Yes, and to the other examples that have been given to the same effect. With regard to the very ingenious argument which you put before us just now, regarding the negative effect of increased temperature at the boshes, I am disposed to admit it fully in the abstract, and I am pleased to see such clear proportions 268 THE SCIENTIFIC PAPERS OF established, regarding the chemical balance of affinities between carbonic oxide and carbonic acid, in contact with metallic iron at different temperatures. I am willing to admit these facts, which are new to me, to the fullest extent, but I would draw from them different conclusions, inasmuch as I cannot admit that the tem- perature in the blast furnace increases necessarily with the tem- perature of the blast. I believe the temperature of the blast furnace will, on the contrary, be practically the same, whether higher or lower temperature of blast is employed, and the reason why I come to that conclusion is as follows : — If blast of very high temperature is employed, the oxygen it contains takes up carbon very readily and is converted into carbonic oxide. Whereas, if a lower temperature of blast is employed, there will be at once a large proportion of carbonic acid gas produced. The carbonic oxide gas would not nearly represent such an augmentation of heat as would be represented by the mixture of the two gases together, hence the reduced iron would, in the one case, be surrounded by an atmosphere of carbonic oxide with nitrogen only ; and in the other case, with a mixture, containing carbonic acid in variable quantity, but the very chemical balance just pointed out to us would tend to equalize the temperature in both cases. These con- ditions would, therefore, not alter the working of the furnace below, but the result of the higher temperature of the blast would make itself felt in the upper portion of the furnace where finally a higher proportion of carbonic acid gas, is realised when blast of high temperature is used. When these favourable circumstances are taken into account, we may expect, I submit, a continuance of the very beneficial result already realized by further raising the temperature of the blast, notwithstanding the interesting circumstances that you have brought before us. SIR WILLIAM SIEMENS, F.R.S. 269 /,•/ tltf (/isriifision of t/w Paper "ON THE STRENGTH OF IRON AND STEEL, AND ON THE DESIGN OF PARTS OF STRUCTURES WHICH CONSIST OF THOSE MATERIALS," By GEORGE BERKLEY, M. Inst. C.E. MR. C. W. SIEMENS* observed that the paper contained a great deal of valuable practical information ; but he considered enough had not been said, on the one important question which had been raised, viz., whether or not there was a definite limit of elasticity in metals. It was stated in the paper, that a bar of iron 1 inch square would elongate with a strain of 3 tons to the inch, and would, on the load being gradually increased, continue to elongate up to a strain of 9 tons or 10 tons to the inch, beyond which point it was known that a more rapid rate of elongation commenced. These results seemed to imply that there was no definite limit where permanent elongation was produced, but in following up this argument the evident conclusion was, that the bar of metal of 1 square inch, if exposed for a great length of time to the moderate strain of 3 tons, must continue to yield, in the same way as though its elastic limit was really exceeded, and must ultimately yield to that force. But all experience went directly against such a suppo- sition. One of the most perfect experiments that could be tried on that point might be found in the old cathedrals of Italy, where heavy chandeliers weighing £ a ton, or more, had been suspended for hundreds of years, by long rods of not more than f of an inch in diameter. If any permanent injury was produced by such a load, it would no longer be safe to go into these buildings ; and the heavy chandelier in the Pisa cathedral, which swung sug- gestively above the head of Galileo Galilei, must inevitably have long since fallen to the ground. He thought practically that no one had any belief in any such action of time, but he was not disposed, on the other hand, to condemn such experiments as * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Vol. XXX. Session 1869-70, pp. 268-209. 270 THE SCIENTIFIC PAPERS OF those of Hodgkinson and Fairbairn. Possibly it might be the case that, in subjecting a bar for the first time to a strain, elonga- tion did take place, which might be explained in this way : it was conceded that in the manufacture of a bar of iron internal strains must arise, owing to the different action of the rollers upon different portions of the material, and such " virgin " bar might be regarded as consisting of a number of aggregate fibres of metal strained one against the other, the internal metal, which had been the hottest, being permanently in tension, and the external metal in compression. In subjecting such a bar to a moderate strain, only the internal fibres would be permanently elongated, while the external metal would be simply released from compressive strain, after which all parts of the bar would bear the strain equally, and this equalising of the active forces must necessarily be accompanied by a moderate stretch. Therefore, in order to ascertain the true limit of elasticity of a material, the first experi- ment upon a virgin bar should not be taken, but the strain should be continued till it had reached a certain moderate limit, when it should be reduced, and then the same series should be gone through again. In proceeding thus he thought it would be found that there was no permanent elongation till the true limit of elasticity was reached. This true limit of elasticity he regarded as being a very important point. Mr. Phipps had justly remarked that, in the long series of experiments on breaking strains, published by various authors, a conclusion was arrived at, more by guess than by scientific reasoning, to the effect that a load might be applied to, say, one-fourth of the breaking strain, with tolerable safety, without any distinction being made regarding the limit of elasticity of the particular material under examination. It would be found, however, that two bars of metal, which might break at nearly the same point, and which might consist, chemically speaking, of nearly the same materials, would be capable of bearing with safety a very different load. The one might begin to elongate with less than one-half the breaking strain, and the other would not begin to elongate till two-thirds of the breaking strain had been reached. He had made some experiments with cast steel, which, being the most refined and uniform metal, was best adapted for such experiments, proving these discrepancies according to the mode of its production ; and he had no doubt SIR WILLIAM SIEMENS, F,R.S. 271 that similar results would be obtained with iron, though it might not be so easy always to obtain the same degree of regularity with that material. He thought that the limit of elasticity of a mate- rial was of much greater practical importance to engineers than its ultimate breaking strain ; because a structure was safe if no part of it was loaded past the point of limit of elasticity, but must ultimately fail if that limit was exceeded. In the discussion of the Paper " ON THE TESTING OF RAILS ; WITH A DESCRIP- TION OF A MACHINE FOR THE PURPOSE," By JAMES PRICE, M. Inst. C.E. MR. C. "W. SIEMENS* said that having lately made some experi- ments with steel rails and iron rails, he could bear out the author's remarks, confirmed already by Mr. Bramwell, as to the great sus- ceptibility of steel to break under the influence of a shock. The paper which Mr. Bramwell read before the British Association f pointed out the reasons why it was so. In the case of an iron rail there were innumerable fibres capable of yielding individually to take a greater strain when necessary. Now in the case of steel which was homogeneous, no such independent fibrous action could take place, and if one part of the line of strength was broken an indefinite amount of tearing strain was thrown upon the adjoining part. In trying steel rails under a blow, he found that where an entire rail would stand the impact of a ton weight falling 20 feet, in the case of a rail being supported rigidly between 3 feet bear- ing, a blow from a fall of only 4 feet of the same weight would break it at the place where the hole was drilled through the web of the rail. It followed from this experiment that in drilling or i * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Vol. XXXII. Session 1870-71, pp. 206-208. t Vide Report of British Association, 1859, p. 422. 272 THE SCIENTIFIC PAPERS OF punching a number of holes through a rail the strength of that rail was diminished to less than one-fourth, as measured by a falling weight ; and this fact should lead to the preference being given to a mode of fastening in which no such holes were made. It was true that in ordinary use no such working strain as the weight of a ton falling through a number of feet was put upon a rail ; but engineers liked to err upon the right side in a question of safety, and were justified, he thought, in giving the preference to steel rails of mild or ductile quality ; for if the steel was not of tough quality, there was danger of its being hardened by acci- dental exposure to cold during manufacture. Steel containing more than fV Per cent, of carbon would become very brittle if by accident it was thrown into water when red hot ; and such a rail might break with a very slight shock. In France it was the habit to make steel rails containing ^ per cent, of carbon, and as far as wearing qualities were concerned French engineers were right ; but there was some danger in using such rails, particularly if the continuity of the rail was broken by holes. Therefore he did not agree with the author in his assertion that the test by blows was altogether inadmissible : he thought it a desirable test to apply along with others. The particular test which the author proposed was valuable in so far as it proved the fair wearing quality of the material ; but he did not consider it sufficient as a test for the wearing quality of rails under the most trying circumstances. Mr. Bramwell had pointed out one of the reasons why it was not sufficient, inasmuch as it did not provide for the propelling action of the driving-wheels on the rail. But, he might have added, it did not provide for the sliding action of the wheels. Upon inclines the wear and tear of rails was much greater than on a level road ; and that was owing, not to any increase of weight, but to the different mode in which that weight passed along the surface of the rails. If the load merely rolled over the surface, the effect upon the rails was very different to what it was if the same weight slid over it, burnishing or trying to dislodge every particle from its neighbour. The machine therefore appeared to him to be incomplete, unless some means of testing that sliding action upon the rail were provided in addition to the rolling action. If stopping the rotation of the wheels would not lead to the expendi- ture of too much power, it would provide a means of subjecting WILLIAM SIEAfENS, F.R.S. 273 rails in a short space of time to a test which, in the ordinary working of a railway, would only be obtained after some months, or even years, of trial. But if any railway company were public- minded enough to devote a length of their main line, where there was a steep gradient or a terminal station for experimental pur- poses, placing the same at the disposal of engineers to put down their rails, such a trial would be as valuable, perhaps, as any that could be desired. In the discussion of the Paper « DESCRIPTION OF TWO BLAST FURNACES ERECTED IN 1870 AT NEWPORT, NEAR MIDDLESBROUGH," By BERNHARD SAMUELSON, M.P., M. Inst. C. E., MR. C. W. SIEMENS * observed that the information contained in the paper and elicited by the discussion went far to show that, by carrying out a chemical operation on a large scale, the utmost results which theory indicated could be almost realised. Two years ago, when the question of large furnaces was first mooted, he made a calculation of the work done in a blast furnace, and of the heat that was developed in that blast furnace. By taking into account, on the one hand, the ore to be heated and reduced, the pig to be melted, the slag to be melted, and the heat and com- position of the escaping gases at the temperature at which they were carried away ; and, on the other hand, the temperature of the blast and the heat due to its combustion with coke, in pro- ducing the gaseous mixture escaping from the top of the blast furnace, he found that 20 cwt. of ordinary coke should suffice theoretically to smelt a ton of pig iron from Cleveland ironstone containing 40 per cent, of metallic iron, and that 21 cwt. per ton of iron was a result that might be practically realised. Assuming * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Vol. XXXII. Session 1870-71, pp. 361-364. VOL. I. T 274 THE SCIENTIFIC PAPERS OF the temperature of the blast at 1000°, the best results at that time were about 26 cwt., but it struck him that Mr. Samuelson had obtained the calculated minimum result almost completely ; his consumption being 20| cwt., and the temperature of blast about 1100°. Mr. Bell arrived at nearly the same figures by another mode of reasoning, and had followed up this subject very minutely, by examining into the particular stages of the chemical operation carried on in the blast furnace, deducing very valuable data for the metallurgist. Nevertheless, he would not recommend others to follow Mr. Samuelson under all circumstances in the construction of a blast furnace. He was at that moment constructing some blast furnaces of very different dimensions ; they would only have a cubical capacity of 10,000 feet instead of 30,000 feet ; for he believed it would be inexpedient in this case to adopt such extreme dimen- sions. It would require the peculiar conditions of the Cleveland iron district in order to do so with advantage ; namely, an excel- lent hard coke and an ironstone rather strong and comparatively poor. For richer ore and tender coke he believed the size of blast furnace such as Mr. Samuelson had described would be inappli- cable. With regard to the effect of extreme capacity, he agreed Avith Mr. Bramwell's views, while at the same time he admitted that Mr. Forbes's remarks were perfectly correct. But Mr. Bramwell spoke of the mechanical absorption of heat — the regenerative action within the blast furnace ; — on the other hand Mr. Forbes spoke of the chemical action between the gases of the blast furnace and the ores ; and both these actions were subject very much to the same laws. To get from the fuel a maximum of effect in a steam boiler plenty of heating surface was given, as in the case of the Cornish boilers ; and it was reasonable to suppose that more sur- face would give superior results, simply because the difference of temperature between the heat-transmitting current and the heat- receiving surfaces was brought down to a minimum. Where a current of gas flamed rapidly among a mass of solid matter, there must be a considerable difference of temperature between each particle of the fluid and the solid receiving that heat : where- as, if the mass was greater, and the current relatively slower, there must be a more perfect adjustment between the two temperatures, WILLIAM SIEMENS, F.R.S. 275 giving rise to a more economical result. In the same way the chniiical action would be more perfect if a gas containing a cer- tain proportion of carbonic oxide (mixed with carbonic acid and nitrogen) had plenty of time to communicate its carbon to the pitrc of ore which was ready to take it in yielding up its oxygen. If the quantity of material present were infinite a perfect adjust- ment between these conditions would arise, depending upon the temperature and the proportional amount of carbonic oxide pre- sent ; but such a condition of equilibrium could never be obtained. It was therefore necessary in practice to consider how much would suffice for the purpose, because other considerations entered into the subject. If a blast furnace was very large in proportion to the quantity of work that was to be performed in it, a greater economy would be attained by a relative increase of first cost. This was the case in Mr. Samuelson's blast furnaces, where 30,000 cubic feet capacity produced only 500 tons of pig metal per week ; whereas a furnace with a capacity of 10,000 or 11,000 cubic feet would produce 300 tons. It was therefore clear that these large furnaces produced approximately only about one-half the amount of work per cubic foot of capacity that the smaller furnace did. The question arose how far was it judicious to expend more capital to obtain additional saving, if other means might be resorted to of arriving at the same, or even a greater increase of economy. This point had not been touched upon in the course of the discussion. Mr. Bramwell had shown that where there was a greater outgoing current than a heat-absorbing material to meet it, an unstable condition or waste of heat must ensue ; and Mr. Forbes has argued in the same way on chemical grounds. In the blast furnace the object was to waste as little heat as possible, and to bring out the gases at the top as cool and as thoroughly de- prived of their chemical or reducing power as was practicable. Both these objects were obtained by diminishing the relative quantity of gases. If, for instance, the relative amount of gases for a given amount of incoming material could be reduced by one-half, and if the chemical conditions were the same, it was clear that the smaller quantity would be more thoroughly deprived of its heat ; but the smaller quantity would have had time to divest itself more thoroughly of its chemical action also : there would be a larger relative amount of carbonic acid gas produced, T 2 276 THE SCIENTIFIC PAPERS OF and the coke would be consumed in the furnace to greater advan- tage. This could be accomplished by a blast of high temperature ; and in this respect his opinion differed very much from the theory of Mr. Bell, to the effect that there was a theoretical as well as a practical limit to the beneficial heat of hot blast. He believed, on the contrary, the blast could not be made too hot for economical purposes, and that real progress in iron smelting must henceforth be looked for chiefly in that direction. In the discussion of the Paper " ON THE CONDITIONS WHICH FAVOUR, AND THOSE WHICH LIMIT, THE ECONOMY OF FUEL IN THE BLAST FURNACE FOR SMELTING IRON," By ISAAC LOWTHIAN BELL, Assoc. Inst. C. E., MR. SIEMENS* said that Mr. Bell had watched blast furnaces more carefully than almost any other metallurgist. Some of the facts brought out in this paper were extremely interesting ; amongst others the proof that the reduction of iron ore was a source of heat instead of, as was more generally supposed, the cause of loss of heat ; and that reduction was effected at so low a temperature as 420° Fahr. Mr. Bell had endeavoured to show that in the blast furnace the different operations, constituting the process of smelting, might be carried on in such a way as virtually to complete one process before the other commenced ; and from this the somewhat astounding conclusion was arrived at, that nearly all the advantages derived from the hot-air blast might be realised by simply increasing the size of the furnaces. The argu- ment was not pushed to the practical conclusion, that the capacity of the furnace should be increased to the point of realising all the * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Vol. XXXIV. Session 1871-72, pp. 133-136. WILLIAM SIEMENS, F.R.S. 277 advantages of the hot blast, but the permissible temperature was limited to 960° Fahr., at which point it was considered that the maximum effect could be had with a furnace of limited capacity. This argument was based upon the supposition that iron ore was reduced at 420° Fahr. ; and that the second action, which was that of carbonic acid splitting up in contact with carbon, could only be accomplished at a higher temperature. If, therefore, the carbonic acid had all been split up in contact with carbon, and a zone had now been reached at which no more unburning of carbonic acid took place, the whole remaining capacity of the furnace would be reserved for the final action — that of the reduction of the ore to the metallic condition, and the production of a large proportion of carbonic acid gas in the gases leaving the furnace. He thought, however, that iron ores, as a rule, were not reducible at the extremely low temperature of 420° Fahr., which was really below that of incandescence. In dealing with calcined Cleveland ore he had no wish to doubt the fact, but if it was considered what this ore consisted of, it would be seen why its reduction and carboniza- tion took place at that low temperature. In calcining Cleveland ore 25 per cent, of volatilised matter was evolved ; therefore the calcined ore must be regarded as a sponge, consisting of extremely divided particles of iron ore. This sponge being brought into contact with the reducing gas, the carbonic oxide was mechanically absorbed in large quantities, and the reduction of the ore facili- tated. The sponge into which Cleveland ore was converted by calcination might in effect be compared to platinum sponge, which, when a current of hydrogen gas was directed upon it, absorbed that gas so violently as to produce ignition. Again, when a solid bar of iron was exposed to a dry atmosphere, no appreciable oxidation would take place in one hundred or even in one thousand years. There were iron bars which, in o.J Roman buildings, had been exposed to the atmosphere for two thousand years and were not oxidised ; but the same iron in a pulverulent condition would take fire instantly in a room, showing that the same material would behave differently under similar circum- stances, according to its aggregate conditions. He had paid considerable attention to the reduction of iron ores, and he had found that, whereas hydrated ores or spathose ores were reducible at a low temperature, the peroxides required a 278 -THE SCIENTIFIC PAPERS OF higher temperature ; whilst there were certain ores which were not reducible at a temperature below 1500° or 2000° Fahr. Those were the dense magnetic oxides which had no gases to give out, but were perfectly dense, like a piece of glass. Such compact ores, he believed, were not reduced in the upper part of the blast furnace in the way supposed — viz., by a current of carbonic acid, but only in a lower part of the furnace after they had become liquid. Certain ores, such as Ilmenite or Marbella ore, had been known to pass through the blast furnace and to come out un- changed with the slag, notwithstanding the heat through which, they had passed. He thought if such pieces of ore could tell a tale, they would speak of actions and reactions going on in the blast furnace which did not altogether tally with the beautiful stratifications Mr. Bell had shown. The author's conclusion, that the hot blast could not be beneficial beyond a certain point, was mainly based upon the argument, that with the temperature of the blast the heat towards the top of the furnace was also in- creased. But the temperature of the blast affected the temperature at the top of the furnace in the contrary way to what Mr. Bell had in his argument supposed. If the temperature of the blast were suddenly raised, then indeed a rise would be perceptible throughout the furnaces, and the gases would escape at a somewhat higher temperature. In that case the same amount of oxygen would be introduced, and the same amount of carbon accompanied the charge ; therefore there must be the same proportion of car- bonic oxide and of carbonic acid issuing at the top, with an increase of temperature resulting from the greater importation of free heat with the blast. But if at the same moment when the temperature of the blast was raised, the relative quantity of coke in the furnace could be diminished, to the point of producing not more than the requisite amount of heat, then a diminished quantity of products of combustion would have to impart its heat to the same quantity of ore ; and inasmuch as the relative quantity of matter to be heated and smelted would be increased, it followed that the temperature of the escaping gases must be less than before, and that there must be advantage in raising the temperature of the blast. As to the effect of the increased temperature of the blast upon the temperature of the crucible of the blast furnace, he had S//? WILLIAM SIEMENS, r.R.S. 279 his views very fully on a former occasion, when the author of the present paper argued on the other side of the question.* He might now state that, in advocating high tempe- rature of blast, he did not look for any great increase of heat in the zone of fusion. He looked for the advantages of hot blast to the greater importation of heat into the whole economy of the blast furnace, resulting, he believed, necessarily, in great saving of fuel. In the statements of results which were frequently put forward, certain elements were generally wanting ; and the most important of these was the relative quantity of blast used. If the tempera- ture of the blast was increased without its being stated whether the same quantity was injected relatively to the amount of carbon in the charge, no positive conclusion could be arrived at ; but these discussions would assume a more definite character, if the amount of blast was in all cases stated, and if the working of the furnace was only taken after it had been readjusted after a change of temperature to a minimum percentage of carbon with the charge. It could be easily conceived that with too much carbon the blast would produce an excess of carbonic oxide, and this would issue at the top of the furnace at a very moderate temperature. It might be argued, in that case, that the hot blast produced unfavourable results ; but if an increasing quantity of ore had been mixed with the coke, and the proportion gradually increased with increased temperature of blast till a positive minimum, to insure fusion of the mass, had been reached, the result would have been much more favourable. The general basis which he went upon was, that if free heat was imported into the furnace with the blast, that heat was produced economically in burning fuel into carbonic acid ; whereas the blast furnace could at most produce carbonic oxide, with a proportion of, say, |th or £th of carbonic acid. The author had clearly shown that, in producing carbonic oxide, only about * th the amount of heat was produced from a given quantity of coal as when carbonic acid was formed. Therefore every unit of heat applied to the blast outside the furnace represented really 8 units of heat produced by the combustion of coke within. * Vide The Iroiv and Steel Institute— Transactions, Vol. I. i>. 222 ; see p. 264, ante. 280 THE SCIENTIFIC PAPERS OP In the discussion of the Paper "ON THE PEACTICAL WORKING OF DANKS'S ROTARY PUDDLING MACHINE," By MB. JOHN LESTEB, Wolverhampton, ME. SIEMENS * said he congratulated the members of the Iron and Steel Institute on the very able reports •which they had re- ceived on the subject of Danks's rotary puddling furnace. He had listened to these reports with great interest, and it seemed as though the facts brought out conclusively proved the value of the apparatus that had been brought before them. That was not the first attempt at a rotating puddling apparatus, as they well knew. He had, many years ago, seen the apparatus, erected, at Dowlais Works, by Mr. Menelaus, and he looked with regret at the difficulty which prevented its practical success. That difficulty had, to all appearance, been overcome by Mr. Danks, by the in- troduction of a judicious fettling material. In the report mention was made of one or two points which called for remark on his part. In one of them, by Mr. Jones, a paper "On Puddling Iron " was mentioned, which he (the speaker) read some years ago before the British Association, setting forth a theory of puddling which had been much criticised by practical ironmasters, but which was very- fully confirmed by the results obtained in the Danks furnace. The reports in question expressed some surprise at the greater yields realised in puddling grey iron than in puddling white iron. Now, he would submit that his paper furnished a complete explanation of that result. He there endeavoured to prove that puddling was, strictly speaking, a chemical reaction between fluid cinder and fluid cast-iron, and he showed that for every pound of carbon in the metal, 3*5 pounds of metallic iron have necessarily to be reduced and added to the charge. In like manner, for every pound of silicon in the metal 2*8 pounds of metallic iron had to be produced. If, therefore, his theory was * Excerpt Proceedings of the Iron and Steel Institute, 1872, pp. 293-295 and 314-315. SIR WILLIAM SIEMENS, F.K.S. 281 correct, it followed that a pig metal, rich in carbon and in silicon, would give greater yields than a metal containing those foreign substances in smaller proportion, or that grey pig metal would produce larger yields than white iron. The report also made mention of the possible application of this furnace to what was called the " Siemens-Martin " process. He could not fall in with that view. It would be very difficult to realise such a temperature in a rotating furnace as was required for carrying out a process in which they had five or six tons of almost pure iron in a fluid con- dition— iron containing about one-tenth per cent, of carbon. Another fatal circumstance would be that the lining of the Danks furnace was composed of oxides of metal, and in the presence of oxides of metal they could not have fluid mild steel. The steel would immediately part with its small percentage of carbon, and become wrought metal. Therefore, it could not be applied, he felt certain, to carrying out that process. But he might remark that some years ago his attention had been directed towards a rotating apparatus, not for puddling, but for accomplishing just the reverse operation — that of reducing oxides into the metallic con- dition. He had steadily followed out those experiments, and before long he might have the pleasure of bringing them before the Institution. Before sitting down he wished to express that he was entirely satisfied with the able, and evidently strictly impartial, reports which they had received. Mr. I. Lotvthian Bell said he should like to put one question to Mr. Siemens, who mentioned that the richer the pig iron was in silicon, the better the yields. That, he supposed, he ascribed to the action of silicon upon the oxide of iron. But he (the speaker) believed a very general impression prevailed amongst puddlers that that could only be true to a moderate extent ; because the silicon, by taking the oxygen, was changed into silica, and that, not being able to exist in a puddling furnace in its uncombined state, combined with oxide of iron, and was thereby a source of waste. Mr. Siemens in reply stated that with regard to the carbon, the result had been proved in the most conclusive manner, by ex- periments which he himself had made in the regenerative gas- puddling furnace. The richer the pig iron was in carbon, the greater was the yield of wrought metal produced. The same 282 THE SCIENTIFIC PAPERS OF chemical reason and the same practical result applied to silicon, although he would quite admit certain drawbacks, which Mr. Bell had alluded to, to the presence of much silicon in the pig metal. The silicon in the pig metal had to be combined with oxide of iron to form a tribasic slag, and this oxide of iron had to be supplied by the fettling. Therefore, if they puddled an iron con- taining much silicon they would require an extra amount of fettling to dissolve the silicon afterwards in the slag, and in the absence of this extra supply of fettling the operation would not progress favourably ; but the chemical reasoning still held good. They could obtain from pig metal rich in silicon a larger yield than from the same pig metal containing no silicon, the simple reason being that the atomic weight of silicon was considerably less than the atomic weight of iron. In his paper read before the British Association he had shown that in puddling ordinary forge pig iron the theoretical increase of weight was about 8 per cent., and that he had already obtained weight for weight in practical puddling — taking the average result of six months' working — without using more fettling ore than was necessary under all circumstances to accomplish the operation. ME. SIEMENS said he had certainly misunderstood the remarks made by Mr. Jones on the previous day, perhaps it was because he had not explained them fully. He had understood that Mr. Jones thought it possible that the Siemens-Martin process of making steel could be carried out in the Danks furnace. If the question was one of puddling Cleveland pig so as to make it suitable for this process, he would not say a word against it, except that he must see the analysis of the puddled material before he made up his mind as to its merits. If that analysis were shown to him he would be able to say at once whether the metal was suit- able or not for the Siemens-Martin process, because he knew exactly how much phosphorus and how much sulphur he could do with ; and if in the first instance Mr. Samuelson had put clearly to him the question whether he would be able to make steel from Cleveland pig, he (the speaker) would most decidedly have told him that he did not believe he could. He thought it could not be done unless they could show him that they could remove phosphorus to a much greater extent than the ordinary puddling S/X WILLIAM SIEMENS, F.R.S. 283 furnace had yet accomplished. With regard to the yield he agreed entirely with the views that had fallen from Mr. Snelus, and which were in conformity with the chemical reasoning the speaker had advanced in his paper on puddling iron. He had showed on that occasion that he could gain 8 per cent, in puddling Cleveland pig in a theoretically perfect manner, and he felt glad to see that results so near perfection had been realised with the Danks furnace. He accorded with Mr. Danks's view that it was not at the expense of the fettling ore that they obtained the increase. In the ordinary furnace it happens that although they had much silicon in the pig metal, a portion of that silicon was burnt off by the direct action of the flame, but in a furnace where there was but little oxidation by flame, very little of the silicon was burnt, and the great bulk of it was oxidised by chemical re-action with the oxides of iron present ; but they must have the oxides present, no matter whether they intended to make iron of them or not, and the dillerence between economical and wasteful puddling was due to whether they retained the iron from these oxides, or whether they wasted it after getting it. In Mr. Danks's furnace, and also in a regenerative gas furnace, if properly conducted and worked, they need not waste the iron, and they could then at least get " weight for weight." ON SMELTING IRON AND STEEL. By C. WILLIAM SIEMENS, D.C.L. (Oxon.), F.R.S.* [A Lecture delivered before the Chemical Society, March 20th, 1873.] ON the 7th of May, 1868, I had the honour of addressing you on the subject of " the regenerative gas furnace f as applied to the manufacture of cast steel," my object being at that time to point to the important part which that furnace was likely to play in such metallurgical processes where intense heat is required. At that time I described a method of producing cast steel upon the open hearth of a regenerative gas furnace by the dissolution either * Excerpt Journal of the Chemical Society, 1873, pp. 661-678. t The joint invention of C. William and F. Siemens. 284 THE SCIENTIFIC PAPERS OF of scrap iron or of ores in a more or less reduced state in a bath of intensely heated pig metal. These processes have now received very considerable practical development at the works of the Lan- dore Siemens-Steel Company, of Messrs. Vickers and Company of Sheffield, and at several other works. Two processes are employed at these works, the Siemens-Martin process, which consists in dis- solving scrap metal or steel in a bath of pig metal to which spiegel- eisen is finally added, and the ore-reducing process in which pig metal and ore in a more or less reduced condition are employed. The process chiefly employed at the Landore works consists of introducing on the bed of an intensely heated regenerative gas furnace, as shown in Plates 43 and 44, about six tons of pig metal, which may be No. 3 or 4 hematite pig. When a fluid bath has been formed, oxide of iron (which should by preference have been melted beforehand with such proportions of lime or other fluxing materials as to form with the silica in the ore and in the pig metal a fusible slag) is added, or natural ores may be used in their raw condition if they contain lime and manganese, as, for example, the African Mokta ore. When about 30 cwt. of this ore have been dissolved (with ebullition) in the metallic bath, it is found that a sample taken from it contains only about O'l per cent, of carbon ; a point which can easily be detected by the eye of the workmen owing to a peculiar bright appearance of the sample when chilled in water and broken by the hammer. In order not to pass beyond this point, samples are taken out from time to time during the latter part of the operation, and such a series of samples, which have been kindly supplied to me by Messrs. Vickers and Co., together with samples of steel made by the process, are now placed before you. The requisite point of decarburisation being reached, the supply of ore must be stopped, and from 8 to 10 per cent, of ferro-manganese or spiegeleisen added to the bath. When this has been well incorporated by stirring, the metal is ready to be tapped into a ladle mounted upon wheels, which is afterwards propelled into the foundry, and discharged either into ingot moulds, to be hammered and rolled, or into dried clay moulds for the production of steel castings. Considerable difficulty was experienced to find a material to resist the excessive heats necessary for carrying out this process ; ordinary Dinas bricks, which are considered the most refractory SIX WILLIAM SIEMENS, F.R.S. 285 material in general use, would be rapidly melted, but a brick, specially prepared by crushing pure quartz rock, and mixing it with not more than '2 per cent, of quicklime to give cohesion, answers well. The hearth of the furnace is made of white sand with u small admixture of more fusible fine sand, which mixture sets exceedingly hard at a steel-melting heat, and possesses the advantage of combining into a solid mass with fresh materials introduced between the charges to make up for wear and tear. The hearth and the furnace-roof, if of the materials just specified, are very little attacked when the Siemens-Martin process is used, although the heat must be sufficient to maintain wrought iron containing only a trace of carbon, in a perfectly fluid condition. If pig metal and ore (previously fused with the necessary amount of flux) are used, the furnace also stands well, but the use of raw ore entails the disadvantage of a more rapid destruction of the furnace ; even magnetic oxide of the purest description necessitates the addition of raw lime for the formation of a fusible slag, and the dust arising from the lime and through the decrepitation of the ore causes the silica bricks to melt away rapidly, so that after perhaps two months' usage, the 9-inch arch of the furnace is re- duced to the thickness of from 1 to 2 inches. It is evident that silica is chemically speaking an objectionable material to be used in the construction of these furnaces, because it prevents the for- mation of basic slags, and that a furnace bed constructed of pure alumina or lime would be preferable. My friend M. Le Chatelier, Inspecteur-General des Mines, whose valuable labours for the ad- vancement of iron metallurgy are well known, suggested to me years ago the use of Bauxite (from Baux in France, where it was first discovered), a mineral consisting chiefly of alumina, for making the furnace-bed, but I was not able to succeed with this owing to the great contraction of the mass when intensely heated, and non-cohesion with the same material introduced for the pur- pose of repair. In attempting to construct the sides and roof of the furnace of Bauxite bricks, these were not found to be equal in heat-resisting power to silica bricks, which latter are indeed unob- jectionable, except when raw ore and limestone are used. If good pig metal, such as is used in the Bessemer process, is employed, a metal of high quality is the result, equalling in most respects the steel produced by melting Swedish bars in pots by the old Sheffield process. 286 THE SCIENTIFIC PAPERS OF There is manifestly an analogy between this and the Bessemer process, both of them being processes of decarburisation of pig metal ; yet there are very important differences, both as regards the nature of the chemical reactions and of the metal produced. In the Bessemer process the silicon and carbon are fully oxidised by the action of the blast, whereas sulphur and phosphorus are known to remain unoxidised. Manganese is oxidised in the Bes- semer process only to a certain extent, and therefore it is not necessary to add spiegeleisen at the end of the operation, when the pig metal employed contains a moderate amount of metallic manganese, as is the case in Sweden and in Styria! Mr. W. Hackney, the manager, and Mr. A. Willis, the resident chemist at the Landore Steel Works, have analysed Bessemer metals made without the final addition of spiegel, and found them to contain no less than 0*3 per cent, of manganese. Notwithstanding the non-oxidation of manganese, from 8 to 10 per cent, of iron is oxidised in the Bessemer process, although iron has naturally less affinity to oxygen than manganese. The oxidation of this amount of iron in the Bessemer converter is, in so far, a fortunate circum- stance, as without it the amount of heat necessary to liquefy the resulting malleable iron could not be produced, and the metal would necessarily set in the converter. In the ore-reducing pro- cess above described a totally different result ensues, as is shown by the following experiment. A manganiferous pig was melted, and ore charged in the usual manner. After the pig was completely melted, it contained the ingredients stated in the first line of the following table, from which it will be seen that silicon and manganese were eliminated first, and then very little change took place in the carbon until the two other constituents were completely removed : — • Contained. Samples taken. Carbon. Silicon. Manganese. When pig was melted . 1-90 •57 1-14 1 hour later 1-8 •233 •576 2 hours later . 1-7 •183 •2 3 , „ ... 1-65 •05 •08 4 , „ . ' - 1-6 none none o , „ ... 1-1 •6 f Manganese and silicon 7 , „. % . •2 ( completely gone. .s/A' WILLIAM SIE.MEXS, I'.R.S. 287 Tin- sulphur and phosphorus are oxidised to a considerable extent; a circumstance which enables us to use pig metal con- taining a certain small percentage of these admixtures, which are not absolutely objectionable unless they occur in excessive propor- tions, the quantity admissible of both phosphorus and sulphur bt ing about '08 per cent. The decarburising agent employed being ferric oxide, no cast- iron can possibly be oxidised, and a ton of pig metal with its quota of spiegel, containing from 9 to 10 per cent, of foreign substances, yields fully 21 cwt. of steel ingots. In this process the addition of spiegeleisen at the end of the operation is an abso- lute necessity, however much manganese may have been contained in the pig metal employed, because the manganese is rapidly oxi- dised, as can be seen from the foregoing table. The reason of the different reaction in the Bessemer process is, in my opinion, that the silica liberated from the beginning of the operation requires a base for its saturation, and that its great affinity to protoxide of iron determines the oxidation of this metal (free oxygen from the blast being present) in preference to man- ganese. A characteristic difference between the two metals, in their fluid condition, is that Bessemer metal on cooling in the moulds sets up a violent ebullition, probably resulting from a reaction between occluded oxygen and carbon, which is counteracted by stoppering the moulds. The ore process metal, if it has been made with care, on the contrary, contains no occluded oxygen, and sinks in the moulds on cooling in the same way as " dead melted " steel does, produced by the old Sheffield process. It has been an open question between metallurgical chemists whether manganese is really required to be present in malleable steel, some maintaining that its beneficial action is confined to the elimination of sulphur during the process of production. Such, however, is not the case, as may be seen from the following extract from Messrs. Hackney and Willis's report : — " Our observation, based on five years' experience, is that no chemical reaction takes place between the manganese of the spiegeleisen and the other elements of the steel, but that it acts simply as an alloy. With regard to manganese not removing any sulphur in a bath of steel, it is a curious fact that the reverse 288 THE SCIENTIFIC PAPERS OF takes place in a blast furnace. As the percentage of manganese in the pig increases, so does the sulphur decrease ; for instance, if to ore and coke, which in the ordinary way will produce a pig containing from 2 per cent, to 3 per cent, of sulphur, mangani- ferous ore is added so as to put 2 per cent, of manganese into the pig, the sulphur will be reduced to "05 or '08 per cent. ; but when 3 per cent, of manganese is found in the pig it never contains more than a slight trace of sulphur. "We have had occasion lately to analyse several hundreds of samples of pig iron made under these conditions, and can vouch for the accuracy of this state- ment, and we think it a fact well worth the attention of iron- masters who are troubled with an excess of sulphur either in their ores or fuel. " Every one must have noticed the absence of sulphur in all analyses of spiegeleisen, although much of it is made from coke, and most of the ores used contain a considerable quantity of pyrites. " That the manganese acts by its actual presence, and not by any chemical reaction, is. we think, proved by the fact that, if through any accident or carelessness of the workmen, the charge is left in the furnace for more than twenty minutes after the spiegeleisen is fairly melted the steel is invariably bad, owing to the oxidation of the manganese, and therefore if such delay occurs, a small addition of spiegeleisen is made, and no bad results follow." About the impurities of steel the same gentlemen report : — " The presence of sulphur, it is well known, makes steel red- short, and the only question is, how much may it contain without injury ? Our experience is, that up to 0'08 per cent, will do no harm, provided there is also present 0'3 per cent, of manganese, and we have even found '112 per cent, without having any com- plaint from the hammermen. "Phosphorus does not appear to affect either the rolling or hammering of steel, even if 0'2 per cent, is present, but if it ex- ceeds 0*08 per cent., the rails become so cold-short that they will not stand the severe test to which they are subjected. " The presence of arsenic and phosphorus increases the hardness of steel at the expense of its toughness. " The effect of copper is not yet understood ; according to Percy it renders steel red-short to a greater extent even than the same amount of sulphur. .S7A' \\-ll.I.L\M SIEMENS, FJLS. 289 - I-'rom the nature of the process, as a rule, very little if any silicon is found in Siemens steel. The carbon and silicon appear to be eliminated equally when manganese is not present, and, as the carbon is generally in excess of the silicon, none remains when the carbon is reduced to 0'2 per cent. The small amount found in the steel is derived from the spiegeleisen." At the Landore Works upwards of 1,000 tons of cast steel are produced weekly by these processes, and other works, such as Vickers and Company, Krupp, of Essen, etc., are using the same for the production of steel of high quality. Both in the ore-reducing and in the Siemens-Martin or scrap process, pig metal forms the principal basis, being used either as such, or as puddled iron or Bessemer scrap-metal, resulting from the conversion of pig metal by a previous process. In my former lecture I expressed my belief that the direct con- version of ores into iron or steel would ultimately be accomplished, and, having since been actively engaged on the problem, it is now my chief object to lay before you the results I have up to this time' attained. I am aware that, on the one hand, the direct conversion of iron ores into wrought iron or steel is no novelty, inasmuch as the ancient Indians and Romans produced their iron by a direct process from the ore ; and that, on the other hand, the blast furnace offers immense facilities for the wholesale extraction of metal from the ore, by the side of which the puny efforts of the ancients producing half a cwt. of metal intermixed with half-fused cinder by a day's toil, and with the expenditure of large quantities of rich ore and charcoal, sink into utter insignificance. Mr. Riley says, in his able lecture " On the Manufacture of Steel and Iron," read before this Society on May 22, 1872 : — " The great improvement lately introduced in the manufacture of pig iron, the enormously increased production at a diminished cost of what may be considered to be the raw material from which we start in the manufacture of iron and steel, are, I think, sufficient to convince not only practical men, but scientific men also, that in any improvement in iron manufacture we must commence with the pig, and consider that our starting point." Mr. Riley here gives expression to the prevailing opinion amongst metallurgists ; but still I do not despair of being able to VOL. i. v 290 THE SCIENTIFIC PAPERS OF prove to you that upon theoretical grounds the blast furnace is open to very grave objections, inasmuch as it produces iron com- bined with nearly all the objectionable substances contained in the materials used, that only expensive fuel, such as coke, can be employed, and that its combustion is necessarily imperfect. Plate 45 shows the distribution of temperature in the blast furnace, as given by Mr. Lowthian Bell in a paper read by him before the Institution of Civil Engineers, in 1872. It shows that the reduction of the metallic oxides to spongy iron is accomplished within the first 20 feet of their descent in the furnace, and at a comparatively low temperature. This upper zone is followed by one where the limestone is decom- posed and the carburisation of the spongy metal is commenced. Between this second zone and the zone of fusion in the boshes of the furnace a zone of great magnitude intervenes, where apparently no other change is effected than an increase of temperature of the spongy metal, but where in reality a very powerful reducing action is accomplished of substances which had much better not be joined to the iron. It is well known that almost all the phosphorus con- tained in the iron-stone, the lime-stone, and the coke is here incorporated with the spongy iron. The silica is reduced to its metallic condition, and, together with sulphur, arsenic, and other bases which may be present, combines with the iron. The final action in the blast furnace consists only in fusing those reduced substances and forming the slags which envelop and protect the fused metal. As regards the fuel question, it will be observed that the result of the combustion in the blast furnace is for the most part car- bonic oxide, and that the heat developed in this combustion amounts to only 2,400 heat units per pound of pure coke con- sumed, whereas a perfect combustion (to carbonic acid) of the same coke would be attended by the development of 8,000 heat units. It is practically impossible to obtain more than one-fifth of carbonic acid to the carbonic oxide issuing from the top of the blast furnace, and taking also into account that the gases leave the top of the blast furnace at 350° C., it may fairly be asserted that only one-third of the heat-producing power residing in the coke is utilised. A portion of the heat thus left undeveloped may .be used, it is true, in burning the gases for the generation of WILLIAM SIEMENS, F.R.S. 2QI steam or for heating the air blown into the blast furnaces ; but fliis utilization represents only a small proportion of the value of the coke or charcoal charged with the ore into the furnace ; whereas a much cheaper material might be employed for the pur- poses just named. The introduction of hot blast was unquestion- ably a very great improvement in blast furnace economy, because the heat thus introduced is obtained by means of the perfect com- bustion of fuel, and, in reducing the combustion necessary within the furnace, the quantity of products of combustion as compared to a unit quantity of ore is greatly reduced, the effect being that the incoming ores have a relatively greater capacity for absorbing the sensible heat from the products of combustion, which latter must therefore issue from the top of the furnace at a lower temperature. Relying upon this argument, I am inclined to believe that the consumption of coke in a blast furnace must materially diminish with increased temperature of blast without limitation of degree, and in this respect I venture to differ from my friend Mr. Lowthian Bell, who maintains that mere increase of capacity of furnace up to a certain limit produces the same effect as increase of temperature of blast, and that no beneficial effect can be obtained by increasing the temperature of blast beyond 515° C. In taking however, the best examples of blast furnaces, the products of com- bustion escaping from the top, four parts out of five, as CO with- out counting the N, and at not less than 350° C. of sensible heat, carry with them fully two-thirds of the heat they would be capable of producing, if they were burnt to carbonic acid. In my former lecture I described a plan of reducing iron oxides by feeding them, mixed with carbonaceous materials, into a rever- beratory furnace through inverted hoppers of fire-clay, the inten- tion being to effect the reduction of the iron ores into spongy metal during their descent, and the fusion of the spongy metal so produced on the open hearth of the furnace, pig metal being used to facilitate the fusion. It was found, however, that the quantity of heat that had to be transmitted through the sides of the fire- clay hopper was so great that the process of reduction proceeded very slowly, and the hoppers themselves were rapidly destroyed by the intense heat of the furnace. The reduction of the metallic iron in closed chambers of this or any other form which I have tried u 2 2Q2 THE SCIENTIFIC PAPERS OP cannot be effected in less than about 36 hours, and that at a great expenditure of fuel for heating the chamber externally. This unsatisfactory result directed my thoughts to another method of producing spongy iron by means of a rotative furnace. This furnace consisted of a long cylindrical tube of iron about 8 feet diameter, mounted upon antifriction rollers ; the brick lining of it was provided with longitudinal passages for heating currents of air and gas prior to their combustion at the one extremity of the rotating chamber. The flame produced passed thence to the opposite or chimney end, where a mixture of crushed ore and car- bonaceous material was introduced. By the slow rotation of this furnace the mixture advanced continually to the hotter end of the chamber, and was gradually reduced to spongy iron. This dropped through a passage constructed of refractory material on to the hearth of a steel-melting furnace, where a bath of fluid pig metal had been provided. The supply of reduced ore was continued till the carbon in the mixture was reduced to the minimum point before indicated. The rotation was then arrested to prevent further descent of reduced ore ; spiegel was added ; and the con- tents of the melting furnace tapped into a ladle and thence into ingots, as before described. This rotary furnace was erected by me at the Landore Works in 18G9, and it was so far successful, that the reduction of the ore was accomplished in a comparatively short time. A difficulty, however, presented itself, which led to its immediate abandonment ; it was found that the spongy metal produced, absorbed sulphur from the heating gases, and was rendered unfit for the production of steel ; the spongy iron moreover, upon its introduction into the steel-melting furnace, floated upon the metallic bath without being readily absorbed into it, and was in great part reoxidised and con- verted into slag by the action of the flame in the furnace. These experiments convinced me that the successful application of reduced ores could not be accomplished through their conversion into spongy metal, and fully explained to me the want of success which has attended the previous efforts of Clay, Chenot, Yates, and others, to produce iron directly from the ore. On the other hand, I had observed that in melting iron ores no sulphur was absorbed from the flame ; and it occurred to me that by melting ores mixed with fluxing materials in a furnace so arranged as to \\-JLIJAM SIEMENS, F.R.S. 293 accomplish its fusion in a continuous manner, and on a large scale, the fused ore might be acted upon by solid carbonaceous matter, so as to separate the metallic iron in a more compact form, while the earthy constituents of the ore would form a fusible slag with the fluxing material. Experiments proved that this reduction by precipitation of the iron could be accomplished only at an intense heat, exceeding the welding heat of iron, but that the iron so pro- duced was almost chemically pure, although the ores and the fuel used might contain a very considerable percentage of sulphur and phosphorus. The specimens of iron which I exhibit were made in this manner from ores of various descriptions, and the following tables give the analysis of the ores and the iron, as also the yield of iron obtained from a ton of ore : — RESULTS OP PRECIPITATION PROCESS AT LANDORE. Orea. Charge. Yield, Total. Coal charged in furnace. Mokta ore . .12 cwt. ) Scale . . . 8 „ / 20 cwt. 6 cwt. 14 cwt. Mokta ore . . 10 „ 1 Scale . . . . 8 ., / 18 „ 4 „ 14 cwt. 2 qrs. Mokta ore . . 12 „ \ Scale . . . 8 „ / 20 „ 6 „ 11 „ 2 „ Mokta ore . . 6 „ \ Scale . . . 4 „ / 10 „ 2 „ 12 „ Mokta ore . . 10 „ \ Scale . . . 10 „• / 20 „ 6 „ 15 „ 2 „ Mokta ore . . 14 „ 1 Scale . . . 12 „ / 26 „ 6 „ 18 „ Total .... 114 cwt. 80 „ 85 „ 2 „ RESULTS OF ROTATOR. Ore. Lime. Coal. Iron. Vickers, Sheffield . . 984 48 40 216 492 .. Birmingham 7S4 176 MM 294 THE SCIENTIFIC PAPERS OF RESULTS OP PRECIPITATION PROCESS AT BLOCHAIRN. Charge. Yield of iron. Analysis of iron. Impurities. No. ~{ *{ Ores. Lbs. Total. Lime. Coal. Purple . . Red 4501 150 / 600 56 356 137 j S =-055 per cent. P=-114 „ Si = -13 ., Purple . . Red 168 \ 56 / 224 12 170 165 »! Melted . . Coke (powder) 3.10 \ 210 / 560 160 4i Purple . . Blackband 300) 600 / 900 90 390 210 •I Blackband Clayband Purple . . 600 ) 600 V 300 ) 1500 150 420 210 •i Blackband Clayband . . Purple . 300 ) 300 \ 300 ) 900 90 145 202 •I Cleveland . . Purple . 900 \ 300 / 1200 120 290 268 ] S =» -041 per cent. P=-150 „ Si = -173 „ WORKING RESULTS OF THE CASCADE FURNACE AT LANDORE. Charge in Cwts. Yield. Mokta ore. Roll scale. Total ore. CoaL Puddled bar. cwt. qrs. 8 8 16 4 7 2 10 8 18 8 15 6 6 12 3 8 4 8 12 4 11 10 8 18 6 13 6 4 10 2 12 12 8 20 6 14 10 8 18 4 14 2 12 8 20 6 11 2 10 10 20 (, 15 2 14 12 26 6 18 102 88 190 cwt. 140 WILLIAM SIEMENS, F.R.S. 295 The ore employed was Moktaore, of the following description : — \ Fe 60-8 FcO Mn304 CaO SiOa . Loss on ignition 82 charges, 14,338 Ibs. ore „ 5,952 „ coal „ 7G8 ,, lime 7:i-7 I 6-48 52-92 •52 •25 4-75 5-11 99-72 Yield in slabs. > 8,115 Ibs. = 56-6 per cent. Other specimens of steel shown are produced by fusion of the iron thus obtained on the open hearth of a regenerative gas furnace, which are undoubtedly of superior quality. The furnace used for carrying out this process of fusion and precipitation consists of a reverberatory gas furnace having two beds formed by the ore itself ; on the upper bed a lake of fused ore is formed which can be let off into the lower bed by piercing the intervening bank of unfused ore ; the lower bed is divided into two compartments, used alternately, each provided with a working door. The dense carbonaceous material, such as an- thracite or hard coke, to be used for the precipitation of the iron in the lower bed, is reduced to a state of powder and mixed with about an equal weight of pulverulent ore. This mixture is spread over the bottom surface of the working bed, and the fluid ore is let in upon it. By stirring with a rabble it is transformed into a pasty and foaming mass, which in the course of from 40 to 50 minutes is shaped into a metallic ball in a bath of fluid cinder, which may be shingled in the usual manner and formed into bar iron or transferred to the pig-iron bath of a steel-melting furnace, where it readily dissolves. The accomplishment of this process involves, however, a certain degree of manual labour and skill, as, if it be carelessly conducted, the yield of iron will be unsatisfactory ; the analysis of the slags shows a variable percentage of iron amounting rarely to less than 15 per cent., but reaching occasionally up to 40 per cent. 296 THE SCIENTIFIC PAPERS OF It was evident that if iron and steel were to be produced largely by direct process, that process must be a self-acting or mechanical one, and here my attention again reverted to the rotating furnace above-mentioned. If I could succeed in furnishing such a rotating furnace with a lining capable of resisting the high degree of heat requisite for the precipitation of the iron, and at the same time capable of resisting the chemical action, I felt confident that this mode of conducting the process must succeed. My attention here re- verted to M. Le Chatelier's former suggestion of the use of Bauxite, which possesses the requisite qualities, if only it can be put into a compact form and rendered sufficiently infusible. A series of experiments to form solid lumps by using different binding materials have shown that 3 per cent, of argillaceous clay suffice to bind the Bauxite powder previously calcined. To this mixture about 6 per cent, of plumbago powder is added, which renders the mass practically infusible, because it reduces the per- oxide of iron contained in the Bauxite to the metallic state. Instead of plastic clay as the binding agent, waterglass or silicate of soda may be used, which has the advantage of setting into a hard mass at such a comparatively low temperature as not to consume the plum- bago in the act of burning the .brick. When the lining is completed, the interior surface of the bricks is preserved against corrosion by fluid cinder, added to bind them together, which also prevents contact with the flame. A Bauxite lining of this description resists both heat and fluid cinder in a very remarkable degree, as I have proved by lining a rotative furnace at my Sample Steel "Works at Birmingham, partly with Bauxite and partly with carefully-selected plumbago bricks. After a fortnight's working the brick lining was reduced from 6 inches to less than half an inch ; whereas the Bauxite lining was still 5 inches thick and perfectly compact. It is also important to observe that Bauxite when exposed to intense heat is converted into a solid mass of emery of such extreme hardness, that it can hardly be touched by steel tools, and is capable of resisting mechanical as well as the calorific and chemical actions to which it is exposed. The Bauxite used for this lining was of the following composition : — Alumina .... 53'62 per cent. Peroxide of irou . . . 42'2G „ Silica . . 4-12 S/K WILLIAM SIEMENS, F.R.S. 297 Other Bauxites which I have had occasion to analyse were composed as follows : — ANALYSES OF VARIOUS BAUXITES. FRENCH BAUXITES. — First Group. SiOa. Al.O,. Fea03. 1-7 66-2 19*7 4-2 54-2. 28-7 37 58-9 25-7 3-2 55-9 28-1 8-2 60-4 25'1 3-9 56-4 22-1 8-2 61-2 23-1 5-9 58-8 23-1 2'8 60-7 25-8 | Raw . 3-5 59-2 24-5 '° \ Calcined . 4-01 67-89 28-09 Second Group. SiOa. A1.0.. Fea03. 2-4 52-5 29-0 2-6 41-8 43-7 1-7 25-2 53-5 2*1 38-7 50-2 1-4 38-7 48-5 1-1 39-2 49-3 ro 38-7 48-0 1-9 41-2 41-7 ( Raw . 1-75 39-5 45-5 0 \ Calcined . 2-02 45-53 52-45 AUSTRIAN BAUXITE.— - Wocheinite (Carniola.} Raw. Calcined. A1203 . . 64-24 85-88 FeaOs > . . 2-40 3-20 SiOa . . . 6-29 8-40 CaO . > . . •85 1-13 MgO . . . •38 •50 S03 . •20 •26 P04 . ^ •46 •51 H.O . . . 25-74 HaO. 12'7 18-0 12-4 12-2 11-5 13-5 11-3 11-8 11-8 1-2-1 HaO. 15-9 13-0 10-05 11-8 12-0 9-4 12-5 15-9 12-57 298 THE SCIENTIFIC PAPERS Ofr IEISH BAUXITE. Raw. Calcined. A1203 . . . 35-0 44-58 Si02 . . .3-5 4-45 Ti02 . . . . 2-0 2-54 Fe203 . . . 38-0 48-40 H20 .... 21-5 The complete rotary furnace, such as is now ill use at Messrs. Vickers and Co.'s, at Sheffield, and at my Sample Steel Works at Birmingham, consists of a set of four regenerators of the usual construction with reversing valves and gas-producers. The rotative chamber is constructed of iron, and rests upon four anti- friction rollers. Wheel-gearing is applied by which either a very slow rotative velocity of from four to five revolutions per hour can be imparted to the chamber, or a more rapid velocity of about 60 to 80 revolutions per hour. The chamber is about 7' 6" in diameter and 9' 0" long, and is provided with a Bauxite lining about 7" thick. A tap-hole is on the working side for dis- charging the slag into the cave below, where it is received in vessels mounted on wheels. At the two extremities of the cylin- drical rotative chamber with its truncated ends, are large orifices, one of which, on the side of the regenerators, serves for the in- troduction of the heated gas and air as well as for the exit of the products of combustion, and the other facing the work- ing platform is closed by a stationary door hung before it in the usual manner. Although the passage for the introduction of the gases in combustion is separated only by a vertical partition wall from the passage through which the products of combustion are led away, the chamber is heated very perfectly, care only being taken that the gases enter the chamber with a certain velocity, which sends them forward towards the door and makes them reach the exit passage only after having traversed the rotative chamber to and fro. This rotative furnace is worked as follows : — The ore to be smelted is broken up into fragments not exceed- ing the size of peas or beans ; to it is added lime or other fluxing material in such a proportion that the gangue contained in the ore and flux combines with only a little protoxide of iron into basic and fluid slag. If the ore is hematite, or contains silica, I prefer .S7A' WILLIAM SIEMENS, F.R.S. 299 to add alumina in the shape of aluminous iron ore ; manganiferous ir-in ore may also be added with advantage. A charge of say 20 <-\vi. of ore is put into the furnace when fully heated, while it is slouly ivvuhin;.r. In about forty minutes this charge of ore and fluxing material will have been heated to bright redness, and at this time from f> cwt. to 6 cwt. of small coal of uniform size (not larger than nuts) are added to the charge, whilst the rotative velocity is increased for a short time in order to accelerate the mixture of coal and ore. A rapid reaction is the result : the peroxide of iron being reduced to magnetic oxide begins to fuse, and at the same time metallic iron is precipitated by each piece of carbon, while the fluxing materials form a fluid slag with the siliceous gangue of the ore. The slow rotative action is again resorted to, whereby the mass is turned over and over, presenting continually new surfaces to the heated lining and to the flame within the rotator. During the time of this reaction, carbonic oxide gas is evolved from the mixture of ore and carbon, and heated air only is intro- duced from the regenerator, to effect its combustion within the rotating chamber. The gas from the gas-producers is entirely, or almost entirely, shut off during this portion of the process. When the reduction of the iron ore is thus nearly completed, the rotator is stopped in the proper position for tapping off the fluid cinder ; after this the quick speed is imparted to the rotator, whereby the loose masses of iron contained in it are rapidly collected into two or three metallic bails. These are taken out and shingled in the usual way of consolidating puddled balls ; the furnace is tapped again and is ready to receive another charge of ore. The time occupied in working one charge rarely exceeds two hours ; and supposing that 10 cwt. of metallic iron is got out per charge, the apparatus is capable of turning out at least o tons of puddled bar per 24 hours. If anthracite or hard coke is available for effecting the reduction of the ore, it should be crushed much finer than when coal or brown coal is used, the idea being that each particle of the reducing agent should be fully consumed during the period of chemical reaction. If wood is used, it has to be charged for the same reason in still larger pieces. If it is not intended to make iron, but cast steel, the balls may be transferred from the rotator to the bath of a steel-melting 300 THE SCIENTIFIC PAPERS OF furnace in their heated condition, and without subjecting them to previous consolidation under a hammer or shingling machine. It is feasible, however, to push the operation within the rotator to the point of obtaining cast steel. If this is intended, the relative amount of carbonaceous matter is somewhat increased in the first instance, so that the ball, if shingled, would be of the nature of puddled steel, or contain even some carbon mechanically enclosed. If now, after removing the cinder by tapping, from 10 to lo per cent, of ferro-manganese or spiegeleisen is thrown in, and the heat within the rotator is rapidly raised by urging the influx of heated gas and air from the regenerator, the metallic balls will soon be seen to diminish, and presently a metallic bath only will be found in the furnace, which may be tapped into moulds and hammered and rolled into steel blooms or bars in the usual manner. Experience alone can determine which mode of working will ultimately prove the best ; but it is probable that for the production of cast steel on a large scale it will always be more profitable to transfer the metallic balls to a separate melting furnace, a series of rotating furnaces working in concert with a series of steel-melting furnaces, so as to produce charges of 5 or 0 tons of fluid steel. In comparing upon theoretical grounds this method of producing metallic iron with the operation of the blast furnace, it will be at once perceived that, whereas in the blast furnace the products of combustion consist chiefly of carbonic oxide, and issue from the top of the furnace at a temperature exceeding 350° C., the result of combustion in the rotative furnace is carbonic acid, which issues from the regenerative furnace into the chimney at a tempe- rature rarely exceeding 175° C. This proves at once a great possible saving of fuel in favour of the proposed method, and to this saving has to be added the fuel required for converting pig metal into wrought iron by the puddling process. It may however be asked, why the rotating surface should admit of the complete combustion of carbon, whereas in the blast furnace such complete combustion is, as is well known, not possible, because each atom of carbonic acid formed would immediately split up into two atoms of carbonic oxide, by taking up another equivalent of carbon from the coke present. The following explanation will serve to elucidate this point : .SYA1 WILLIAM .S7A.1//-W.V, l-.R.S. 30! In the rotative furnace streams of carbonic oxide are set up within the mass under reaction ; and this carbonic oxide on reaching the surface meets the current of intensely heated air proceeding from the regenerators, and completes with it perfect ci.iiilnistion within the free space of the chamber. The carbonic acid thus generated comes in no further contact with carbon or metal, consequently it cannot split up, but is drawn away un- changed into the chimney, while the evolved heat is taken up by the sides of the chamber and transmitted by reverberation and conduction to the mixture of ore, fluxes, and coal. In this process we have, therefore, to accomplish two things, viz., the deoxidation of the ore, and the fusion of the earthy matter mixed with it. If we take (say) hematite ore, consisting of peroxide of iron with 10 per cent, of silica, we shall determine the quantity of carbon necessary for its reduction from the formula Fea03 + 3C, which gives 2Fe + 3CO ; and according to which the consumption of carbon (taking its atomic weight at 12 Q x 1 9 and that of iron at 56) amounts to ' = *32 Ibs. per Ib. of iron 2x56 reduced. The heat absorbed in this reaction amounts, according to Dr. Debus, to 892 units * per Ib. of iron produced, but on the other hand the further combustion of '32 Ib. of carbon from the condi- tion of carbonic oxide to carbonic acid (CO to C0a), by means of the free oxygen introduced into the rotative chamber from the regenerator yields "32 x 5600= 1792 units of heat, leaving 1792 - 892 = 900 units available for heating the materials and for melting the slag. The quantity of materials to be heated per Ib. of iron produced would amount to ore, 1'59 ; lime or other fluxing materials, '16 ; making a total of 1'75 ; and taking the specific heat of Fe203 at •154 as determined by Herman Kopp, and the temperature to which the materials have to be raised at 1500° C., the heat required for this purpose would not exceed 1'75 x '154 x 1500 = 404'25 units. To this consumption would have to be added the latent heat absorbed in liquefying the slag. The slag would amount to '16 Ib. silica + -16 Ib. lime = '32 Ib. per pound of iron * Dr. A. W. Williamson gives 885 '3 units as the result of his calculation, which two figures agree sufficiently for my present purpose. 302 THE SCIENTIFIC PAPERS OF produced, and, although we have no precise data from which we could ascertain the latent heat absorbed in liquefaction, we can hardly estimate it at more than 150 units per lb., or at -32 x 150 = 48 units, which, with the above 404*25, makes 452'25 units, whereas 900 heat-units are available, as resulting from the cal- culation above given, proving that '32 lb. of pure carbon would, theoretically speaking, amply suffice to produce 1 lb. of puddled bar from ordinary hematite ore, without counting, however, losses of heat by radiation and from other causes. In the production of cast steel, three operations are essentially involved, viz., the deoxidation of the iron, the fusion of the slags, and the fusion of the metal itself with such proportion of carbon and manganese as is necessary to constitute steel of the temper required. The theoretical quantity of fuel required to accomplish these operations would exceed that of making wrought iron by the fusion of heated metal, which may be estimated at, say, 1000 units, or at = '125 lb. of carbon per lb. of steel produced. 8000 which have to be added to the '32 lb. used in reduction. - In fine, a ton of iron ought to be producible from hematite ore with 6 "4 cwt. of carbonaceous matter, or say 8 cwt. of common coal, and a ton of cast steel with 8'90 cwt. of carbon, or say 11 cwt. of coal. In giving these figures, I do not wish to imply that they will ever be completely realised, but I maintain that, in all our operations, we should fix our eyes upon the ultimate result which theory indicates, which, owing to the imperfect means at our command, we shall never completely reach, but should con- stantly endeavour to approach. In taking incidental losses by radiation through imperfect com- bustion and through imperfect absorption of heat into account, we find that the actual consumption exceeds the theoretical limits about three times, or that a ton of iron can practically be produced with a consumption of 25 cwt. of coal, and a ton of cast steel with 40 cwt. of coal, which consumption represents a great reduction as compared with other methods of production. WILLIAM SIEMENS, FJl.S. 303 In tlif discussion of his Paper "ON THE MANUFACTURE OF IRON AND STEEL BY A DIRECT PROCESS." [NOTE ON MR. SIEMKNS'S PAPER.* — The Paper f "On the Manufacture of Iron and Steel by a Direct Process," was prepared under severe pressure of business, with the view of being amplified and corrected after delivery. Unfortunately, however, the rough paper, with marginal remarks having reference only to the reading, was handed to the printer without my having had an opportunity of revising and ampli- fying it, as I should have wished. — C. W. S.] DR. SIEMENS \ said, amongst the observations which had been made, he would notice only those that required an answer from him. Some of them had been answered fully or partly by other speakers, and need not therefore be referred to by him again, because their time was naturally valuable. The first speaker was Mr. Snelus, and he had spoken very much in favour of reducing iron from the fluid condition, and had referred to a method, which he had informed them was in course of being tried at Middles- brough, of forcing, he supposed, carbonic oxide gas through fluid ores. Now, he had tried that method of proceeding and he cer- tainly had not succeeded. Carbonic oxide, or any other poor description of gas, was so near the point of saturation with carbon that, if it took up any oxygen from the ore which it contained, it soon arrived at the point where it took no more, and there the reaction would stop. The result would be that a vast amount of gas had to be driven through the fluid ore in order to produce a given amount of reducing work, but that large amount of gas had the disadvantage upon the fluid ore that it cooled it, and thereby checked the reaction that was going on. It was upon those re- sults becoming apparent, which, however, he (Dr. Siemens) partly expected, that that mode of proceeding was given up and solid * Excerpt Journal of the Iron and Steel Institute, Vol. I. 1873, p. 253. f As both the paper "On Smelting Iron and Steel," see p. 283, ante, and this one cover the same ground, the former has been reprinted, with the above dis- cussion on the latter. J Excerpt Journal of the Iron and Steel Institute, Vol. I. 1873, pp. 84-90. 304 THE SCIENTIFIC PAPERS OF fuel resorted to in all cases. With regard to the elimination of sulphur and phosphorus, he had to draw a particular line of dis- tinction between the ore-reducing process carried on at Landore and the process which he now had only partially substituted in aid of it. In the furnace, such as was worked at Landore, and at several other places, it was possible that the elimination of phos- phorus and sulphur proceeded only at the same ratio in which it would proceed in the Bessemer converter, but there was this differ- ence that the operation took eight hours, whereas the Bessemer process was completed in a quarter of an hour ; therefore, it was probable that a larger proportion of sulphur and phosphorus was evolved in the ore reducing process, and that, he believed, was the case in actual practice. In drawing a distinction betAveen the two processes, he did so without the least intention of depreciating the Bessemer process, which, in many ways, he admired excessively, but as drawing attention to an essential difference between the two processes. "With regard to the price of bauxite, he could hardly speak with confidence as yet. The mineral was found in large quantities in the south of France, in Austria, and also in Ireland ; and as there was no present use for it, the probability was that it would be obtained cheaply, and the process of converting it into material for the lining was certainly not an expensive one — not more expensive than that of fire-brick making. He had not been aware that Mr. Snelus had turned his attention to lime for linings ; in the paper, allusion had been made to lime also, and they had, especially in the ore-reducing process, used lime bottoms to some extent. Hitherto he had not been able to obtain lime in such a form as to resist permanently the effects of scoriae, but it was quite possible ; and he might say that he was now engaged upon a course of experiments at Birmingham, with a view to substitute lime, in some cases at any rate, for bauxite in forming a lining. Mr. Snelus had also alluded to a point in the furnace which cer- tainly required explanation — whether the parts of the furnace throat, where it entered out into the rotating chamber, were not very rapidly attacked ? He (Mr. S.) had some little misgivings on that, but he found that experience proved decidedly more favourable than anticipation ; those parts (pointing to some on drawing) had now stood for five or six weeks of working, and they certainly were none the worse for it. It had to be borne in mind .s/A' \VIIJ JAM SIEMENS, FJt.S. 305 that tin- bauxite lining did not actually touch the silica brickwork, but was pt 'i-hups an inch apart from it, and that the flame in making a turn through the furnace did not carry with it so much dust outward as might be the case if it swept across a furnace. He t'< 'inid also in the puddling furnace a very great difference in favour of the return current ; it seemed as though the dust were swept out of the flame and little ashes were deposited in the passages. They could get any amount of heat, even coming up to full steel melting heat, inside the rotating furnace without artificial blast. With regard to manganese and its necessary presence in steel, he thought that Mr. Riley was perfectly right in saying that tool steel was found without more than a trace of manganese, but they must remember that such steel contained one per cent, of carbon, and generally was very free from sulphur ; but it had been established in a very absolute manner at Landore, that mild steel containing sulphur must necessarily also contain manganese in a given propor- tion to the amouut of sulphur present, and that this proportion increased with the mildness or the relative absence of carbon in the metal. Thus, if the metal contained '08 per cent, of sulphur, they considered it not safe to have less than three-tenths per cent, of manganese in the metal, and whenever, through accidental causes, the manganese in the metal was less, the steel did not work so well, nor did it do so well when cold. He (Mr. Siemens) was much impressed by the kind observations made by Mr. Bessemer. Mr. Bessemer had been an early labourer in that field, and the great successes which he had attained were vividly before them. It was no small compliment to him (Mr. Siemens), he considered, that Mr. Bessemer had some years since been thinking of extending his labours in the direction which he (Mr. Siemens) had taken, and if circumstances had not prevented him (Mr. Bessemer), he doubted not would ultimately have arrived at the same, if not superior results, but he (Mr. Siemens) had given attention to this question, not a few years, but many years ; and if results of a practical kind had been obtained, Mr. Bessemer, he was glad to think, would be the last man in the world to dispute or discredit them. Mr. Parks referred to the analysis of a bar of iron (which had been produced at Birmingham) containing one-third per cent, of copper. Now it was an undoubted fact that the process under discussion fetched all the copper out of the ore, and, therefore, if VOL. I. X 306 THE SCIENTIFIC PAPERS OP the ore contained copper, the iron would contain it no doubt also ; but in the particular instance referred to, the presence of copper was accounted for by a previous charge which was made with ore containing about a half per cent, of copper, and some of the charge having remained attached to the sides of the furnace, it worked into the succeeding charge. Some other speakers had spoken with regard to the effect of copper on iron, and he could fully confirm the observations made by Mr. Fothergill, that a very small percentage of copper entirely prevented the iron from coming together ; instead of forming balls, it remained separate, and would not hold together. Dr. "Wright was the first speaker to touch upon the fuel question, which question had been very fully taken up by the President, and carried somewhat against the conclusions arrived at by himself. Now, with regard to that question, he wished to explain his views concisely, but more fully than he had done in the paper. He must say that the furnace in Birmingham was no criterion with regard to the economy of the process, because that furnace was of comparatively small dimen- sions, and was erected simply for the sake of experiments, the object being to see the effect produced on the lining by different treatment, and on the quality of the iron produced by various mixtures and fluxes. Lately, he put in a lining which had not been baked beforehand, and the result was that the balls would not hang well together ; the bauxite came off in small filaments from the lining, and acted, as he might say, like soap between the nodules of iron, preventing their cohesion. That difficulty was removed after exposing the lining to two days' intense heat, and now the results were better, as might be seen by the two balls sent up, which were then in the yard at the back of the building, and had been produced in that little furnace. They were balls of nearly 600 Ibs. each from charges of a thousand pounds ; one of blackband and the other of Acadian ore. The normal way of working the rotary furnace was as follows : — The furnace was charged with say a ton of pulverized ore, and the slow rotation went on until the mass was heated through and through to full redness. Then the carbon was introduced and mixed with the charge in giving a rapid rotation to the apparatus. The conse- quence was that reaction and fusion set in immediately, and it was very important that at that point the action should be very S/A WILLIAM SIEMENS, F.R.S. 307 en. -r^etic in order to weld the particles of iron t <>•.;•' •( her, while at the same time the earthy material with the ore was fused and !'"r;i u.'d a slag with the fluxing material employed. If that opera- tion was normally carried out, the iron formed collected in what he might call a grisly condition — small masses hanging together and slightly rolling over each other — whereas a lake of perfectly liquid cinder formed at the bottom, and after that liquid cinder had been tapped off, more rapid rotation was given, and the mass formed readily into one or several balls of metallic iron. In that process the two actions of the formation of the metallic iron and of the fusion of constituents of the ore were carried on simultane- ously, and that was an essential condition to the making of good and clean balls, and in this the process differed essentially from the processes of Chenot and others, in which spongy iron envelop- ing earthy matter was first formed which absorbed sulphur, and could not, therefore, yield pure metal. Now, with regard to the fuel question, he had certainly appeared to be very bold to prognosticate such results as he had done, but the action in the furnace had hardly been fully understood, or his results could hardly have been questioned. They had there the ore and the carbon mixed together in a state of reaction ; that reaction pro- duced currents of carbonic oxide which rose to the surface, where complete combustion took place, and the whole of the carbonic oxide was consumed under the most favourable circumstances possible, because it was consumed at the moment of its generation without being first taken through a cooling tube or exposed to loss of any kind, and it was burnt by a current of intensely hot air by oxygen heated to at least 2,000 degrees Fahrenheit, perhaps 3,000 degrees Fahrenheit. Therefore, the carbonic oxide thus formed by chemical reaction which was lost in the blast furnace was consumed under the most favourable conditions of the furnace, and the heat thus developed accounted fully for all the heat that was necessary for bringing up the material to the state of heating required, and for melting the slag, the regenerators acting as fly- wheels for taking up an excess of heat at one part of the process, and yielding it at another. Theoretically speaking, '32 cwt. of carbon would be necessary for the production of a hundredweight of metallic iron, but. the result which he had to put forward as being practically attainable and virtually attained by himself, x 2 308 THE SCIENTIFIC PAPERS OF was one and a-quarter ton of fuel per ton of iron. Now, in dividing the one with the other, it would be found that he claimed only 25 per cent, of the theoretical result. Mr. Krantz, in his investigation of his regenerative gas furnace, gave him credit for utilizing from 15 to 20 per cent, of the theoretical heat residing in fuel in heating iron, but he (Mr. Siemens) claimed 25 per cent, in the rotative furnace, because fully one-half of the work was done by reaction of the heated oxygen upon the car- bonic oxide produced there and then in the furnace, and upon that portion there was no sensible loss by refrigeration in cooling tubes or through leakage. Mr. Bell, when he visited his (Mr. Siernens's) little works at Birmingham, had seen the reaction within the rotator going on for a considerable time without any gas being admitted from the gas-producers, showing that the carbonic oxide generated within the mass sufficed to produce the requisite amount of heat to support the process. He (Mr. S.) therefore believed that he should be borne out by practical experi- ence when he asserted that one ton and a-quarter of fuel would suffice for producing a ton of iron. With regard to the quality of that iron, he had already stated in the paper, that it was excellent material for being transferred to the melting furnaces in order to produce steel, being almost entirely free from sulphur and phos- phorus, and although the material produced had not yet been practically proved for iron-making, he felt pretty confident of ultimate success in this direction also. The reason why sulphur and phosphorous did not combine with the iron was that they were in an oxidised condition in the ore and combined with other substances, and that the reducing action of the apparatus was insufficient to move them. If the reaction was insufficient for their reduction, then there was no reason why they should be present at all in the iron, and in that respect the direct process claimed an advantage over the blast furnace, where the reducing action was so energetic that everything reducible was brought into combination with the iron. He thought he had now touched upon all the points referred to in the discussion, and had only to thank them for the patient hearing they had given him. WILLIAM SIEMENS, F.R.S. 309 In the discussion of THE PRESIDENT'S (MR. I. LOWTHIAN BELL) ADDRESS, DR. SIEMENS * said he had not thought of making any remarks of his own, but the President in delivering his address had, as usual, given them a good deal to think about, and he was rather sorry that the discussion had turned only upon one of his remarks, though indeed to discuss all the points raised would fill up the whole time of their meeting. With regard to one question that had been touched upon, Sir John Alleyne had already mentioned that he had tried, with tolerably successful results, the furnace for puddling that he (Dr. Siemens) had brought before the Institution last year. The chief features of that application were, that the regenerative gas furnace was used, and that the products of com- bustion left at the same side of the heating chamber as that at which the flame entered. Puddling furnaces, similar in arrange- ment, but not rotative, were now largely used. He mentioned in his paper last year the works of Messrs. Nettlefold and Chamber- lain, who had then 10 furnaces at work upon that plan, and they had now 20 ; these were working very successfully, and producing excellent iron and good weight. Of course the question of fettling was the important one as regards the rotative furnace, and what- every they might do, it would be a difficult and delicate question to make good fettling, unless they had a large supply of very pure oxides. At Butterley, they were particularly badly off in that respect, as their ores were of a poor description, though in the end they made good iron. Still, however, they were very poor ores, and their quality was not nearly sufficient to supply pure oxide, or even pure enough to use for fettling their furnaces. This difficulty was less formidable in working ores in the manner he had proposed to do last year. That process, although not yet carried out on a commercial scale, was progressing towards practical results. His sample works at Birmingham were steadily working * Excerpt Journal of the Iron and Steel Institute, 1874, pp. 49-50. 310 THE SCIENTIFIC PAPERS OP experimentally at the details of the process, and several applica- tions had been made of it at other works, but they were hardly sufficiently advanced in practice to give any working results. With regard to the President's observation concerning his ore process, he must admit that it was a legitimate criticism, namely, whether in the rotary furnace, carbonic acid could be kept away from the metal as it was forming. He (Dr. Siemens) still main- tained the argument he used last year, that the carbonic acid remained separate from the ore, and that in this respect he had an advantage over the blast furnace. Of course, there was no abso- lute separation of the carbonic acid formed from the ore, and practice alone could show whether the reduced metal was effectu- ally protected against re-oxidation under these circumstances. The results he had obtained showed that they could get about 80 per cent, of the iron from the ore, which did not seem a good result as contrasted with the blast furnace practice, but if they compared it with the working of a blast furnace and the subse- quent puddling furnace combined, it was by no means a bad result, and he (Dr. Siemens) claimed to be judged by that standard. His advantage consisted, however, chiefly in economy of fuel. He was glad that the President had alluded to a project which had found vent in the public press, of using chalk instead of coal. He thought that, on the whole, the President had dealt too leniently with that project. They should remember that chalk was the result of a double combustion — a combustion of calcium and a combustion of carbon — both combustions being perfect in themselves, leading to a further combustion of the two combined together, and, therefore, if the originator of that scheme had looked all the world over, he could not have found a more thorough cinder. .SYA' \V1LLIAM SIEMENS, fi.R.S. 3! I In t/ie discussion of the Paper " ON THE MANUFACTURE AND USE OF SPIEGELEISEN," By MB. GEO. J. SNELUS, DR. SIEMENS* said the Landore Works being producers of spiegeleisen, he could, from his experience there, bear out nearly all that had been said by the author of the paper. He agreed with him that there was no great difficulty in producing spiegel, as, indeed, all things were simple if they knew how to deal with them, though up to that point they were difficult. At first there had been a difficulty in getting the slag right, and according to their experience the slag must be as basic matter as possible. They had succeeded in making spiegel containing as much as from 18 to 20 per cent, of manganese, and they could vary it so as to make it from 10 to 12 per cent., which was what was preferred for common use, the richer spiegel being reserved for producing extra mild steel. There was one point upon which he would like to ask Mr. Riley to give a little more information, that was, why did spiegeleisen never contain even a trace of sulphur ? As he under- stood the paper, it was owing to the manganiferous slag having a greater capacity for sulphur, but he (Dr. Siemens) thought that that explanation was hardly sufficient for the extraordinary fact that they did not find even a trace of sulphur in spiegeleisen. As regarded phosphorus, it had been contended that it acted as a substitute for carbon, and was rather a desirable constituent in spiegeleisen, but he would much rather be without it, and not risk the beneficial effect of phosphorus on the steel. Another interest- ing point with respect to the use of spiegeleisen, was the nature of its effect upon the steel ; was it that the manganese simply deoxidised the iron, or was it that the manganese must be present in a metallic state, in order to produce malleable steel ? He inclined to the latter hypothesis, because his observations went to prove that manganese was necessary in malleable steel, especially if sulphur was present. Manganese seemed, in fact, to have a • Excerpt Journal of the Iron and Steel Institute, 1874, pp. 84-86. 313 THE SCIENTIFIC PAPERS OF specific action in neutralizing the effect of sulphur, and no chemi- cal explanation, that he was aware of, had ever been even given of that fact. On the other hand, he (Dr. Siemens) did not think that the deoxidising action of the manganese was the essential effect of that substance in the process with which his name had been connected, because they could regulate the oxidising action on the bath to such a degree, that the absorption of oxygen by the bath had not commenced before the spiegel was added, and yet the addition of spiegel was necessary. If the operation of decar- burisation was carried on to the point at which oxygen was absorbed from the atmosphere, that is, until the carbon was reduced to below 1 per cent., it was very difficult to get rid of the oxygen. After spiegeleisen had been added, and the bath had become perfectly quiescent, they would find the steel, when poured into the moulds, set up a violent ebullition. Now, that ebullition proved that oxygen existed in the fluid metal and probably in combination with carbon, which was liberated suddenly after the steel had been lowered in temperature to near the point of solidifi- cation, but which the manganese had not been capable of removing. He was aware that, in the Bessemer process, when spiegeleisen was added, a powerful ebullition was set up ; but that was not the case in his process, in which ore was used as the decar- burising agent, and the steel when poured into the ingot moulds, or moulds for casting purposes, showed no sign of ebullition, if carefully prepared ; on the contrary, the steel contracted, or what was technically called piped, but if the operation had been carried too far, it seemed to acquire an extraordinary affinity for oxygen, and that oxygen at very high temperatures did not seem to go out again, notwithstanding the addition of manganese, but remained associated with the metal until it had cooled down near to the point of solidification. He would like to have that important point cleared up in this discussion. WILLIAM SIEMENS, F.R.S. 313 In ihe discussion of the Paper "ON IRON AND STEEL FOR SHIP-BUILDING," By MR. N. BARNABY, DR. SIEMENS * said, there can be no doubt that steel is a metal which is worthy of the highest consideration of ship-builders, engineers, boiler-makers, and all persons, in fact, engaged in construction of that kind. One thing is necessary, namely, that those who use that material should know what it is. We hear of comparative results of steel and puddled iron as produced in one furnace and another furnace ; and one would naturally come to the conclusion that steel was a definite compound varying only as regards quality. What is that compound may I ask ? Steel in the form of a needle, an edge tool, or of a punch, is of a hardness approaching that of the diamond ; steel in the form of a spring is of an elasticity unequalled by any other metal, or any other sub- stance in nature. Then, again, steel in the form of a milled plate is, with few exceptions, the toughest material in existence, tougher than copper or wrought iron. It can be moulded into almost any shape in a cold condition. Therefore, we ought first to under- stand what we mean by steel before we consider its merits or demerits for structural purposes. You may say that the hardness depends upon the proportion of carbon in the metal. Does it ? I have lately experimented with steel containing four-tenths per cent, of carbon. That steel, if treated in a certain way, would make an excellent punching or cutting tool. If treated in another way and annealed carefully, it is so tough that you could work it into the form of your hat. Then, again, drawn into wire and annealed in another way — that is to say, heated in a certain way and then put into oil — it assumes a tensile strength of nearly 100 tons per square inch ; whereas, in the other form just before mentioned, when annealed carefully its tensile strength would not exceed 85 or 36 tons. Now, if the mere fact of after-treatment * Excerpt Transactions of the Institute of Naval Architects, Vol. XVI. 1875, p. 140. 314 THE SCIENTIFIC PAPERS OF can produce such enormous changes in the behaviour of steel, how important it must be to give to steel the nature which we desire for structural purposes. Now, if you take a plate and throw it down in a wet court-yard, and then punch it and use it for the manufacture of a boiler, there can be very little satisfaction in the result obtained from the material. Yery likely in the same plate, if you could cut out pieces, you would find very different qualities, and some of these qualities would be valuable in one place and would be destructive to the plate in another. It may be laid down as a general rule, that a higher material and a higher pro- cess require higher intelligence to deal with them. If you ride a common cart-horse you may go to sleep on him, but if you ride a fine spirited horse all your wits must be about you, or else you may be landed in a ditch. So with steel, you have to understand first of all what quality of steel you have to produce, how much carbon, and how much manganese should be mixed with the material, and how little sulphur and phosphorus you can put up with. Until you have done that, you do not know what you are speaking of. It is a material belonging to a group varying between the hardness of the diamond and the toughness of copper ; and it is also of the highest importance that the manufacture throughout, and the construction throughout, should be carried on with superior intelligence. Now, should we shrink from using a material, because intelligence is required in working and using it ? Surely that would be a very poor compliment to this age of progress. We should have no difficulty in finding what are the conditions necessary to produce steel of such and such a quality, and should see to it that we obtain this quality and obtain it always. With regard to the question of obtaining it always, I maintain that we have a greater power in our hands than with regard to iron ; iron, as we know, is produced in small quantities ; the puddler produces sometimes a ball which is rather young, and at other times produces it overheated ; and this material is piled again, put through the rollers, and in the end we get a sort of average between the qualities of the different balls. In making steel we formerly dealt with it in small quantities also by melting it in pots, but Mr. Bessemer has shown us how to deal with it in large quantities in his converter. I have had considerable ex- perience in dealing with it in large quantities in the open hearth S/X WILLIAM SIEMENS, F.R.S. 315 furnace. There I know that we can produce six, eight or ten tons of steel of perfectly uniform quality. We can take out samples before pouring that steel to assure ourselves of having the quality (1. This metal is thoroughly mixed — it is a perfectly fluid mass — and, therefore, there can be no reason why there should be a difference in the behaviour of one part of this metal from the behaviour of another part. Now, I have lately seen steel of very mild quality produced which is eminently suitable for structural purposes. This steel contains hardly any carbon at all, perhaps one-tenth per cent, only ; but it contains manganese in a larger proportion than has been given to it hitherto. It is possessed of a toughness which is unapproached by any other kind of metal ; and before it breaks it yields even to 50 per cent. Now, if such a material can be produced, and if such a material will resist say 80 tons, which is quite enough for all purposes, I think it is the very best material for structural requirements. In tlie discussion of the Papers "ON THE MANUFACTURE OF STEEL," by WILLIAM HACKNEY, B.Sc., Assoc. Inst. C.E., and "ON BESSEMER STEEL RAILS," by JOSIAH TIMMIS SMITH, M. Inst. C.E., DR. SIEMENS * said that he regarded Mr. Hackney's Paper as so comprehensive that it offered room for observations on many different branches of the subject. His remarks would be confined to the first two portions into which the subject was divided, namely, the chemical and the manufacturing. The author had, perhaps, dwelt too much upon the question of name, and hail proposed to change the prevailing denominations of mild steel, * Excerpt Minutes of Proceedings of the Institution of Civil Engineers, Vol. XL1I. Session 1874-1875, pp. 91-95. 316 THE SCIENTIFIC PAPERS OF hard steel, spring steel, and so forth, and to call "steel" all malleable iron which had passed through the fluid condition. This definition would exclude, however, natural, blister, and puddled steel, and was therefore in his opinion inadmissible. On the other hand, Dr. Siemens considered it would be difficult, if not impossible, to define steel by its mechanical qualities. Steel was almost the hardest substance in nature, if treated in a certain way ; treated in another way it was the most elastic of metals, if not the most elastic substance in nature ; and treated in another way it was nearly the most ductile of metals. It was decidedly the strongest substance in nature. Dr. Percy had said he con- sidered steel a metal in which iron was the chief constituent, and which would harden. If that definition were adopted, a limit would be arrived at where it would be uncertain whether a sub- stance was steel or iron. One rail delivered by a manufacturer would come under the definition of steel, and another rail delivered in the same contract would come under the definition of iron, simply because one had rather less carbon than the other ; and after all, the mildest steel, and iron itself, would admit of tempering. Dr. Percy had said that molten iron, according to Mr. Hackney's definition, ought to be called steel ; but it had been already remarked that such iron could not be treated mechanically ; it would not stand rolling and hammering, and therefore it was not steel. He thought, however, a definition might be found which would answer all requirements, namely, that steel was a compound of iron with any other substance which tended to give it superior strength. This definition would embrace the different kinds of steel, from the hardest tool steel down to the mildest, and would embrace those compounds in which manganese, tungsten, chromium, phosphorus, or sulphur, replaced the carbon of ordinary steel. It had been objected that steel was uncertain in its nature ; that it sometimes was very ductile and very strong, and at other times would break short and was not be trusted. Mr. Walker had said that, on that account, he preferred iron to steel for structural purposes. Steel was a material of a much higher nature than iron. It was much stronger, and could be made to possess nearly any degree of strength, hardness, and ductility, between wide limits, that it was desired to give it ; but it was only natural that such a material should require greater 51//? WILLIAM SIEMENS, F.R.S. 317 care than iron. If extreme toughness was required, care must be taken that the material was not put partially through a process of lur.li'iiing or chilling, and that its chemical constitution w;is uniform. The higher material required a higher intelligence to « tiling mass would go between the rotating lip of the vessel and the standing part of the furnace, and cause it to stop. Mr. Hackney had alluded to experiments carried on in America I iv Mr. Blair, who appeared to have found that, if the ore and rarhon were heated to a sufficient temperature, and left to them- selves, the heat retained in the mass would be sufficient to complete the reduction of the ore. Dr. Siemens maintained that that was an entire fallacy. Although the ore might be hot enough for the reaction to commence, a very large influx of heat would be required, during the operation, to make the whole of the oxygen contained in it combine with carbon. Mr. Lowthian Bell had already proved the fallacy of the assumption that ore, under such circumstances, would combine with carbon and form itself into spongy metal. He had himself paid considerable attention to the reduction of ore, in order to obtain material for the bath, and he had experienced great difficulty in reducing ore into spongy metal. The iron, in that spongy condition, took up sulphur very readily, and sulphur vitiated the steel produced from it. These failures and difficulties induced him to resort to another mode of obtaining metallic iron from the ore, by passing the ore, in a heated condition, through a rotating chamber, and there treating it with reducing material, not at a temperature to produce sponge, but at a melting temperature at which cohesive wrought metal was at once produced. That part of the process was as yet in an experimental stage, and he could not at present reply to Mr. Williams's inquiries regarding it ; but before long it would be at work on a complete scale, and he would then be in a better position to speak definitely regarding it. The chemical process of making steel might be varied almost ad libitum, and that variety was undoubtedly the best which, from impure ore or impure pig metal, would produce material of comparatively high quality. Hitherto phosphorus and sulphur had been regarded as the enemies of steel, but recent experience had shown that they might be innocent constituents under certain conditions. If phosphorus was contained in the metal used for steel-making, it was necessary that the metal should contain very little carbon ; in fact, the carbon should be reduced to a mere trace ; and manganese should be introduced in order to produce a malleable metal. This was being carried out very successfully in 320 THE SCIENTIFIC PAPERS OF France and in this country, and the results were very satisfactory. Years ago the use of rich ferro-manganese had been found to afford great assistance, but manufacturers had not succeeded in producing a soft and tough metal containing so large a proportion of phosphorus as had been produced latterly, more particularly at Terrenoire, in France, in using the Siemens-Martin process. He had very few observations to offer with regard to the working of steel. In solidifying from the melted state it had a natural tendency to become honeycombed, either through the generation of gases, or through mere contraction of the semi-fluid mass, and it was necessary to close these cavities as thoroughly as possible, because steel, unlike iron, did not weld ; and if a hollow space existed in an ingot, that hollow space would remain a break of continuity, no matter through what process it was put afterwards. Probably hammering was the most efficacious of those contrivances which had hitherto been adopted for closing those bubbles ; but Sir Joseph Whitworth had elaborated a plan for remedying the evil at the proper moment. He compressed the steel while it was still in a fluid or semi-fluid condition ; Dr. Siemens expected great results from that system. He was not prepared to say whether it would ever supersede hammering and rolling, for ordinary rail-making, but for such purposes as gun-making, he considered that Sir Joseph Whitworth's plan commended itself as one of great importance. In the discussion of the Paper "ON FLUID COMPRESSED STEEL AND GUNS," By SIR JOSEPH WHITWOETH, BART., D.C.L., F.E.S., MR. C. W. SIEMENS * observed that the paper now read was remarkable on account of the very striking results which had * Excerpt Minutes of Proceedings of the Institution of Mechanical Engineers, 1875, pp. 285-288. WILLIAM SIEMENS, F.R.S. 321 been arrived at, and which the members would have an oppor- tunity of witnessing at the author's works. But perhaps the most ivmarkalilr l< 'uture of the subject was the systematic manner in which those results had been arrived at. The question of gunnery h-iil 1 n taken up by Sir Joseph Whitworth in 1854 in connection with the rifle, and in 1868 in connection with the construction of stei-1 guns ; and on the occasion of his reading a paper before the British Association in 18G9 on the penetration of armour plates by long slid Is tired (»l»lii|iiely, the remark had been made by himself • Mr. Siemens), as President of the mechanical section, that "Mr. Whitworth having taken up the question of gunnery has viewed it from a mechanical point of view, and has arrived at purely mechanical results in this problem. His solution commends itself to all who have gone into the question ; and it is natural there should be some diversity of opinion under such circumstances." The solution at that time arrived at by Sir Joseph Whitworth in connection with the question of constructing guns had reference to the method of rifling that he proposed ; and it appeared to be conclusive. Nothing was more natural than that his attention should next be directed to the production of the material from which the gun was to be constructed ; and having persevered in thoroughly investigating this portion of the subject, he had suc- ceeded in arriving at the remarkable results brought forward in the present paper. In the plan now carried out, the steel after it had been produced was dealt with under a method entirely different from those tefore adopted, being here compressed while in a fluid or semi-fluid state. He had at first felt considerable doubt as to the effect of the new method. It was said that in applying hydraulic pressure upon fluid steel the gases contained in the fluid metal would be driven out ; but he could not see how that was to be done by mere pres- sure. For in applying pressure to a fluid, the pressure acted in all directions equally ; and why a particle of gas held in suspension in the fluid should go in one direction rather than another, and should get away from the pressure to which it was subjected, it seemed difficult to conceive. The facts however spoke for them- selves ; and these being ascertained, it was more easy to find an explanation of what took place. The result he suggested might be accounted for by the circumstance that the fluid steel congeal- VOL. I. Y 322 THE SCIENTIFIC PAPERS OF ing first on the outside of the mould offered more resistance there to the motion of the plunger, and the outside thus became com- paratively speaking porous, while the fluid portion in the centre received a larger amount of compression than the outside which had more power of resisting the pressure. The particles of gas entangled within the fluid mass would therefore encounter rather less resistance towards the outside than towards the inside, the full hydraulic pressure being transmitted to the centre of the fluid mass. In that way the expulsion of the gases from the fluid metal might perhaps be accounted for ; and he should be glad if Sir Joseph Whitworth would give his explanation of the matter. The fact being admitted, it was clear that the steel produced by that mode of treatment must possess many great advantages over metal treated in the ordinary way by hammering ; for it was hardly to be supposed that hammering would be capable of driving out the gases. With regard to the mode in Avhich these gases entered the metal, he did not think they were merely entrapped mechanically at the time of pouring out the metal into the mould ; because in working melted steel in the open hearth of a regenerative furnace he had found that the metal could be made at any moment to evolve gases in great quantities by simply plunging a cold bar of iron to the bottom of the fluid mass. The fluid metal evidently absorbed carbonic oxide to a very great extent ; and it was due to the partial congelation of the metal that the gases were suddenly set free. Similarly in the Bessemer process a great ebullition took place on pouring the fluid metal out of the converting vessel into the iron moulds, and the top of the moulds had to be closed by a stopper to prevent the metal being thrown out by the ebullition. It was clear therefore that the metal contained a large quantity of gas occluded within itself ; and if this was retained in the metal it became a source of weakness. However small the bubbles of gas might be, their presence would have the same effect as the presence of particles of foreign matter between the particles of metal, and must necessarily weaken it. In reference to the proposal to designate as steel any metal bearing a tensile strain of 28 tons per square inch, he thought it would be wise on the whole to fix a limit of strength, but some further limitation seemed also to be needed. For instance, a WILLIAM SIEMENS, F.R.S. 323 in- tul produced in the puddling furnace, with or without being converted into steel by the ordinary cementation process of making blister steel and shear steel, would have the required amount of tcinile strength, and would therefore pass as a steel. But he (..nsidered a broad distinction should always be made between steel which had passed through the fluid condition and that pro- duced by other processes, because the latter was deficient in one essential quality which was always sought for, namely, uniformity of strength. He would therefore willingly accept the suggested definition of steel and iron according to tensile strength and ductility, if it were confined to metal that had passed through the fluid condition. It would appear from the paper that it was immaterial by what process the steel was produced, provided it had been produced from pure materials and would bear the required tensile strain. But however true it might be that the quality of the steel was due to its chemical nature, yet this chemical nature could only be obtained in a uniform and regular manner if the process of manu- facture was in conformity with the conditions necessary to produce the desired result. Such steel, he believed, it would never be possible to produce by the old processes of puddling aud cementa- tion ; and this led him to suggest that the demand for the quali- ties generally associated with steel should be confined to what was known as cast steel. The results of the experiments in testing small cylinders with gunpowder, as shown in the table accom- panying the paper, were most instructive, and appeared to leave very little room for doubt that mild steel must be the proper material for the production of guns. Whether guns made of one block of steel like the old cast-iron guns, or those having an inner core hooped with steel rings, were the best, was a question for gunmakers to solve, and must depend mainly upon the dimensions of the structure. But the results now arrived at sufficiently showed what extraordinary strength and ductility combined might be obtained in constructing guns of a solid block of steel ; and he hoped the Admiralty and the War Office would soon sec their way to affording this system a thorough trial. Y 2 324 THE SCIENTIFIC PAPERS OF In the discussion of the Paper " ON PRICE'S PATENT RETORT FURNACE," By ME. I. LOWTHIAN BELL, M.P., F.R.S., Middlesborough, DE. SIEMENS * said, that when he first saw the paper on that furnace, he could hardly think it was Mr. Isaac Lowthian Bell who had written it, because they all knew that Mr. Bell was thoroughly conversant with the phenomena of heat and the chemical actions that occurred in the combustion of fuel. Yet he found in that paper, prominently put forward, a comparison of Price's furnace with his regenerative gas furnace, in which it was stated that there was an absolute loss of 30 per cent., arising from the action of the gas-producer in dealing with the carbonaceous matter while reducing it to the state of carbonic oxide, before it passed into the furnace. Seeing this statement in Engineering^ he took the opportunity of calling attention to the fact that the gas-producer had several duties to perform. The carbonaceous matter contained in the coal was burnt to carbonic oxide, but in addition to that, all the hydrocarbons were developed from the coal, and besides a quantity of vapour of water being decomposed into its elementary substances, and thus a considerable amount of the heat that would otherwise be lost, was simply transferred from the state of sensible heat to that of latent heat, in order to be re-developed in the furnace. Considered from this point of view, it would be found that the loss in the gas-producer was not 30 per cent, as stated, but about 12 ; it was a subject that could be thoroughly cleared up by theoretical argument, and by measuring the temperature of the gases as they came from the gas-producer. He was glad to find Mr. Bell admitting that he was wrong in his calculation, but still he did not seem disposed to accord to the regenerative gas furnace the reputation for economy which it has acquired. The regenerative gas furnace was sufficiently well known, and its economy was proved in various applications, and he would not take up the time of the meeting by reasserting its * Excerpt Journal of the Iron and Steel Institute, 1875, pp. 496, 497. WILLIAM SIEMENS, F.R.S. 325 merit. In liis letter, he did not make comparisons between the t\v»i furnaces, he merely endeavoured to correct an error which Mr. I'.ell li;ul incidentally fallen into. Rc^anlin^ Price's retort furnace, IK- ini^ht observe, that at one time he had retorts in con- nection with his own gas-producers when he found that he could not get them gas-tight, and also that if, as in Price's furnace, the coal passed through the retort, surrounded by the spent gases on tin ir way to the chimney, the spent gas would speedily take up all the gas that leaked through the joints, and make away with it Dzioonsnmed ; moreover, it was very difficult to construct a vertical retort in such a way, and to heat it to that nicety that the coal would part with its hydrocarbons, and would not adhere to the sides. The probability was that if they gave that furnace into the hands of an ordinary fireman, the retort would soon be choked, the bricks get overheated, and the whole thing come to grief. How such accidents were prevented in Price's furnace did not appear ; probably at Woolwich, where extreme care was bestowed upon it under the author's own eyes, and where any failure could readily be put right, without counting much the cost of doing it, it might answer for a certain time, but judging by his own experience, he should be apprehensive of a considerable amount of difficulty if such a furnace were put into ordinary hands. The furnace, while working, would no doubt give a fair result, and develop a considerable amount of temperature. In the discussion of the Paper "NOTE ON THE MANUFACTURE OF ANTHRACITE COKE IN SOUTH WALES," By ME. W. HACKNEY, DR. SIEMENS* said, he could fully substantiate the results which Mr. Hackney had stated in his paper as having been * Excerpt Journal of the Iron and Steel Institute, 1875, pp. 530-532. 326 THE SCIENTIFIC PAPERS OF obtained at Landore ; but it must be remembered that the coke which had been used hitherto there was very weak coke, and it would be unfair, perhaps, to expect the same difference of results if that anthracite coke were tried, for instance, in the Durham district where coke of a much harder kind was obtained by direct distillation of coal. It would be admitted by the author that the process of making artificial coke from anthracite and binding material was, of course, not new. He (Dr. Siemens), had first seen it in operation many years before at the Creusot Works, and he had then formed a very favourable opinion of the coke produced ; and when about seven years ago he had been requested by the Landore Siemens Steel Company to design two blast furnaces, he designed them with the idea that such coke would be used. The question which had then most occupied his mind was what height he ought to give to those furnaces. It was at a time when the general opinion of iron-masters was very much in favour of high furnaces. Some had suggested 70 or 80 feet furnaces. Others had said that GO feet was the least height that should be employed. His idea had been to make the furnace only 52 feet high, as being the height most suitable to the fuel at his command in the locality ; but he had added another 2 feet, and the first furnace was made 54 feet high. Nothing had been changed since in the proportions of the furnaces. The blowing engines worked splendidly, and the Cowper stoves had given no trouble, and yet the result had not been such as he had anticipated. That was due entirely to the weak coke that had been employed, and though before they started those furnaces all the machinery had been ordered for making anthracite coke, their erection had been postponed, as coke of that description was at the time not well known in this country. It had been a very fortunate circumstance, therefore, that Messrs. Penrose and Richards had taken up the question of making an- thracite coke. They seemed to have come to the conclusion that to make hard anthracite coke, besides binding coal, a high binding material, such as pitch, was required ; and he (Dr. Siemens), willingly admitted that pitch was necessary, in addition to binding coal, if it was their intention to make coke very rich in anthra- cite ; but he was not quite so certain, notwithstanding the results which they had recorded, that it was desirable in all ca*ses to have coke containing quite so much anthracite as 60 per cent. He .S7A' WILLIAM SIEMENS, F.R.S. 327 looked upon tin- l>last furnace as requiring a fuel which would live down to the crucible, and there perish. If they were to charge graphite, they would get it all into the crucible, and have to tap it out with the slag, unconsumed ; and what Professor Williamson had just said showed the great resistance of hard coke to combus- tion, and its great advantages in certain respects ; but they might ha\v too much hardness and so make the coke imperishable in the furnace. He had therefore proposed that before deciding upon the proportion of anthracite, comparative trials should be made, using coke containing a very large per ceutage of anthracite, formed with pitch, and weaker coke containing only from 25 to 30 per cent, of anthracite, made without pitch. He had with him a piece of coke containing 25 per cent, of anthracite and no pitch, which appeared to him probably hard enough for their height of furnace and their blast ; but he might be mistaken. It might be that the harder coke gave still better results ; but he must say that if the hardness exceeded a certain limit, he expected that a, large amount of carbonaceous matter would come out with the slag, and in fact, their experiments already showed that evil to exist to some extent, but they had hardly been carried on for a sufficient length of time to say definitely to what extent. There could be no doubt whatever that the production of coke of such hardness that it would resist the action of hot car- bonic acid in the upper portion of the furnace and furnish carbonizing material down to the very bottom of the furnace, was a matter of very great importance. One result which had been observed and which Mr. Hackney had not stated, as far as he could gather from his paper, was this, that while they were troubled with sulphur in using their ordinary coke, which contained a good deal of sulphur, the sulphur disappeared as by magic the moment the anthracite coke came down to the bottom of the furnace, producing, in fact, No. 1 pig metal with only a trace of sulphur, instead of No. 4 pig, containing a very large proportion of that objectionable ingredient. The coke now brought before them had been produced in the horizontal coke oven, commonly used in South Wales, but he thought that u still denser quality would be produced in vertical retorts of the Appold type, and in making his designs for the Landore Com- pany, this had been the form of coke-oven he , had specified ; 328 THE SCIENTIFIC PAPERS OF his reason having been that the powdery material of which an- thracite coke was constituted, required a certain degree of com- pression to bring the particles into contact, and that the absence of this pressure caused the coke to be more or less spongy near the upper surface of the mass. In the discussion of the Paper "ON A METHOD OF PRODUCING PURE CHARCOAL STEEL DIRECTLY FROM THE ORE," By HENRY LAEKIN,* Dr. SIEMENS, F.R.S.,* said the old Sheffield method of making cast steel might be called a method by error. They took the ore and smelted it in a blast furnace, turning out a product which consisted of iron mixed with slag, and a great deal of carbon, all the carbon that could be gathered from the ingredients put into the furnace. All that foreign matter had then to be removed, and so it was puddled. The result was iron mixed with slag, but with- out any trace of carbon, or at any rate in no definite combination therewith. This was not what was wanted, which was iron com- bined with carbon, or steel, and so it was again subjected to a very different process, termed cementation, whereby it was kept heated for a fortnight in a furnace, packed with charcoal. This gave a metal which was certainly steel, but it was mixed with slag and full of blisters, so that it was not yet fit to be used. After some years they adopted the method of fusing it in pots, and so pro- duced cast steel such as was used in Sheffield to the present day. Any means of producing this material by a short process must be of great importance to the country, since steel was becoming more essential every day. Several methods of producing steel direct from the ore had been mentioned, but others had been omitted. He him- * Excerpt Journal of the Society of Arts, Vol. XXIV. 1875-1876, p. 93. 5/7? WILU 'AM SIEMENS, F.R.S. 329 self introduced the system of reduction by a rotator in 1868, and illicit state the results he obtained. The cheapest and most direct method of reducing iron ore was in a rotary furnace ; the iron ore and the carbonaceous material were introduced at one end of a large rotating cylinder, and brought out in the condition of spongy iron continuously at the other end ; nothing could be simpler or cheaper, but still he saw reason to abandon it. First, because the spongy iron thus obtained absorbed in the very process a good deal of sulphur, and this could not be remedied unless you could prevent its contact with the sulphurous acid produced in the combustion of the coal. Then, again, it was not easily dissolved in the bath of metal, even if that were sufficient, because it floated on the top, and rapidly oxidised under the influence of the flame of the furnace. Moreover, unless you used such materials as could not practically be employed on a large scale, the spongy iron became enclosed in the gangue of the ore, and would not melt in the metallic bath, the gangue forming a screen which prevented intimate contact between the fluid and the solid sponge. He therefore modified the process without abandoning the principle of the rotary furnace, and now raised the heat to the point of melting, not the ore but the gangue contained in it, and thus effected the reduction. The result was a metallic ball enveloped in scoria, which did not absorb sulphur, and which could be hammered out into bars, or transferred to the open hearth furnace and melted down into steel. He believed that would be found the cheapest and most direct method. He alluded chiefly to the pro- duction of mild steel in large quantities ; with regard to tool steel he was not sure if the presence of a little foreign matter, such as silicon and sulphur, should be entirely avoided. The famous hard steel of India contained a considerable proportion of these elements, and generally compounds ol' iron were harder than the pure metal. 330 THE SCIENTIFIC PAPERS OF In the. discussion of the Paper "OX SOME RECENT METALLURGICAL PROCESSES," By J. A. PHILLIPS, THE Chair was taken by Mr. C. W. SIEMENS,* who in closing said : The process which Mr. Phillips had brought before them was one of many which distinguished the metallurgy of the present day. Ancient methods were always found to be very wasteful, both in fuel and materials, because it never occurred to the ancient metallurgist to separate the silver or gold from the copper, or to make use of the iron as a secondary process. He selected his ore for the one purpose he had in view, whether it was copper, silver, or iron, and used his fuel very wastefully in extracting it. This process was conducted at the expense of the iodide, which had only lately come into use mostly through photography, and at first sight he had been struck by the apparently great expense attaching to it. The discussion, however, had shown that this was really of very little importance, because, though iodine was relatively expensive, the process was so perfect that it was used over and over again. This reminded him of another process lately come into use for the production of soda, where another expensive material, ammonia, was used over and over again to produce carbonate of soda directly from common salt, without the intermediate stages of soda ash, soda cake, and so forth. The question had been asked whether the extraction of silver dete- riorated the value of the copper, and the answer was that it did not, but rather enhanced its value, and he could fully believe that. Lord Palmerston once defined dirt as "matter in the wrong place," and certainly silver in the copper must be reckoned as dirt, and those who dealt with copper as a metallic conductor of electricity regarded it as dirt of a very objectionable character, for a very slight admixture of silver or any other foreign matter in the copper would reduce its conductivity to perhaps one-fourth of the proper amount. There could be no question, therefore, that * Excerpt Journal of the Society of Arts, Vol. XXIV. 1875-1876, p. 291. .S7A' WILLIAM SIEMENS, F.R.S. 331 it was advantageous to produce the metals separately and in their utmost purity. With regard to the use of the residue in the blast furnace, with all respect to Mr. Ililey's opinion, he still thought copi>- 1 per rent., was very soft. That might be partly owing to the tempering, for if the steel had been slowly cooled it would be soft, but it might also be owing to the manner in which the carbon was combined. Carbon was not always chemically combined even in steel. In the process of mixing spiegeleisen with the blown metal at the last moment in the Bessemer process there was hardly time to form a chemical combination, and hence metal might be pro- duced which contained a considerable proportion of carbon, and yi't was essentially soft metal because the carbon was not chemi- cally combined. He had observed, in boring a large cylinder of steel cast from metal of that description, that at one point the boring tool went deeply into the metal, and at another point there was a resistance as though the metal were hard. In such a case no effect of temperature, of sudden cooling, was involved, because of the particular form of the metal. The phenomena showed clearly that steel was not always homogeneous unless special care had been used to make the mixture perfect. Mr. Cowper had attributed to manganese the quality of making the metal tough, whereas carbon made it hard. That was not universally the case. In the case of steel containing as much as 0'4 or 0*5 per cent, of carbon, little manganese was desirable or necessary to make the metal forge properly ; but in the case of very soft metal, and metal containing phosphorus, the manganese was an essential condition. For instance, 0*2 per cent, of phosphorus, which was about the maximum amount admissible, necessitated about 0*4 per cent, of manganese to make the metal at all workable and to prevent its extreme brittleness when hard ; but in metal containing hardly any carbon, less than 01 per cent, manganese was of the utmost importance, and without it the metal could not be got to work or stand against the grinding axle. The manganese seemed to bind the particles of metal together, and to make it more homogeneous. Mr. Riley had mentioned the difficulty of determining such a slight amount of carbon by the ordinary colour test. No doubt the diffi- culty was great, but Mr. Willis, of the Landore "Works, had intro- duced a test for determining a very slight proportion of carbon, sufficiently accurate for all practical purposes, by dissolving the Z 2 340 THE SCIENTIFIC PAPERS OF metal in nitric acid and observing the effect of colour on the solu- tion. The nitric acid did not act upon the carbon, and it produced a brown tinge of sufficient intensity to be distinctly observable, even though the proportion of carbon should be considerably below O'l per cent. This test would enable manufacturers to produce steel of extreme mildness, such as was now used largely for engi- neering purposes. It was impossible to estimate so slight a differ- ence in carbon as 0'05 or O'l per cent, by any mechanical test ; but by a ready chemical test of that kind the manufacturer was enabled to bring the metal down to an exact point considerably below O'l per cent. No doubt these questions were at present only partially understood, and much work was still required in order to arrive at certain conclusions regarding the conditions necessary to produce steels of definite qualities. If steel was pro- duced from pure iron, such as was found in Sweden, a metal could be made containing hardly any manganese, and only a trace of carbon, and no appreciable percentage of phosphorus or silicon ; and metal of that description, which was as nearly as possible of pure iron, was perhaps the toughest that could be made, exceeding in toughness copper or even silver. A further advantage of such metal was that it was less liable to rust. Experiments lately made in France showed a percentage of rust, as compared with wrought and cast iron, in the proportion of 0'4 to 1'4, being much in favour of a pure metal such as a very mild steel — a quality of great value for shipbuilding and purposes of that kind. SOME FURTHER REMARKS REGARDING THE PRODUC- TION OF IRON AND STEEL BY DIRECT PROCESS. BY MR. C. WILLIAM SIEMENS, D.C.L., F.R.S.* IN mixing comparatively rich iron ore in powder, with about 25 per cent, of its weight of pounded coal, and in exposing this mix- ture for some hours to the heat of a common stove or of a smith's * Excerpt Journal of the Iron and Steel Institute, 1877, pp. 345-359. SJX WILLIAM SIEMENS, l-.R.S. 341 fire, metallic iron is formed, which, on being heated to the welding p lint, on the same smith's hearth, may be forged into a horseshoe i.t' cxirllcnt quality. The admixture with the ore of some fluxing materials, such as lime or clay, will, in most cases, be of advantage to rid the iron of adherent slag. The simplicity of this process is such that it naturally preceded the elaborate processes now in use for the production of iron and suvl upon a gigantic scale, nor can it surprise us to find that attempts have been made from time to time, down to the present day, to revert to the ancient and more simple method. It can be shown that iron produced by direct process is almost chemically j.uiv, although the ores and reducing agent employed may have contained a considerable percentage of phosphorus, sulphur, and silicon, and that, if freed from its adherent slag, it furnishes a material superior in quality and commercial value to the ordinary iron of commerce. The practical objections to the direct process, as practised in former days, and as still used, to a limited extent, in the United States of America and in some European countries, are that — 1. Very rich ores only are applicable, of which about one-half is converted into iron, the remainder being lost in forming slag. 2. The fuel used is charcoal, of which between three and four bons are used in producing one ton of hammered blooms. 3. Expenditure of labour is great, being at the rate of 33 men, working twelve hours, in producing one ton of metal (see Percy). Iron produced by direct process in the Catalan forge is therefore expensive iron, and could not compete with iron produced by modern processes except for special purposes, such as furnishing melting material for the tool steel maker. But, it may be asked, could not the advantages of the direct process be combined with those of modern appliances for the pro- duction of pure and intense heats, and for dealing with materials in large masses, without expenditure o.f manual labour, and cannot chemistry help us to obtain larger yields and facilitate the using of comparatively poor and impure ores ? A careful consideration of these questions led me to the con- clusion, some years ago, that here was a promising field for the experimental metallurgist, and that I possessed some advantage over others in the use of the regenerative gas furnace as a means 342 THE SCIENTIFIC PAPERS OF of producing the requisite quality of heat without the use of charcoal and blowing apparatus. I engaged, accordingly, upon a series of experimental researches at my sample steel works, at Birmingham, and, in 1873, I had the honour of submitting the first fruits of these enquiries to the Iron and Steel Institute, in a paper entitled " On the Manufacture of Iron and Steel by a Direct Process." Encouraged by the results I had then obtained, I ven- tured with others upon some larger applications, the principal one of which has been made at Towcester, in Northamptonshire. If viewed by the light of present experience, it would have been wiser to have fixed upon another locality with fuel, skilled labour, and better ores within easy reach ; but in extenuation of the error committed, it may be urged that the site was fixed by force of cir- cumstances rather than by selection, the chief temptation being an ample supply of small Northamptonshire ore at a very low cost. It was, however, soon discovered that this ore, although capable of producing iron of good quality, was too poor and irregular in quality to yield commercial results unless it was mixed with an equal weight of rich ore, such as pottery mine, Spanish ore, or Roll-scale, all of which, as well as the fuel, are expensive at Tow- cester, owing to high rates of carriage. It is in consequence of these untoward circumstances that the works at Towcester have not been completed by the addition of rolling mills, the intention being to transfer the special machinery ultimately to existing ironworks when the process has been sufficiently matured for that purpose. The Towcester Works were visited, in the autumn of last year, by two eminent metallurgists, Professors Von Tunner, of Leoben, and Akermann, of Sweden, who have published the results of their observations in separate reports.* The results noted down by Mr. Von Tunner are referred to by our past-president, Mr. I. Lowthian Bell, in his paper on the " Separation of Carbon, &c.," which was read in March last, and will be discussed at the Newcastle meet- ing. The criticisms contained in these publications are conceived in the fairest possible spirit, and form indeed a most valuable record of the progress achieved up to that time, but they furnish me with an inducement to break silence sooner than I had in- tended, regarding the further progress which has been effected, * Das Eisenhiittenwesen von L. Ritter von Tunner, Wien, 1876. SIR WILLIAM SIEMENS, J-.K.S. 343 and the conclusions I am disposed to draw, from past experience, regarding the direct process of the future. The leading idea which guided me in these researches was to operate upon such mixtures of ores, fluxes, and reducing agents as would, under the influence of intense heat, resolve themselves forthwith into metallic iron and a fluid cinder, differing essentially f roiii the methods pursued by Chenot, Gurlt, Blair, and others, who prepared spongy metal in the first place, by a slow process, which is condensed into malleable iron or steel by after processes, but assimilating to some extent to the process first proposed by .Mr. \Vrn. Clay. In my paper of 1873, I described two modes of effecting my purpose, the one by means of a stationary, and the other by means of a rotative furnace chamber, the former being applicable chiefly where comparatively rich ores are available, and the latter for such poorer ores as occur near Towcester. At the Towcester works, three rotative furnaces have beeu erected, two of them with working drums 7 ft. in diameter, and 9 ft. in length, and the third of smaller dimensions. The gas flame both enters and passes away from the back end of the fur- nace, leaving the front end available for the furnace door, which is stationary. The ends of the furnace chamber are lined with Bauxite bricks, and the circumference with iron oxides, resulting from a mixture of furnace cinder enriched with roll-scale, or calcined blackband in lumps. About 30 cwts. of ore mixed with about 9 cwts. of small coal having been charged into the furnace, it is made to rotate slowly for about 2£ hours, by which time the reduction of the metal should be completed, and a fluxed slag be formed containing the earthy constituents and a considerable per- centage of ferrous oxide. The slag having been tapped, the heat of the furnace and the speed of rotation are increased to facilitate the formation of balls, which are, in due course, taken and treated in the manner to be presently described. These balls contain on an average 70 per cent, metallic iron and 30 per cent, of cinder, and upon careful analysis it is found that the particles of iron, if entirely separated from the slag, are pure metal, although the slag may contain as much as G per cent, and more of phosphoric acid, and from 1 to 2 per cent, of sulphur. In shingling those balls in the usual manner, the bulk of the cinder is removed, but a sufficient residue remains to impart to the fractured surface a dark appearance without sign of crystallisation. Upon being worked, the metal shows what appears to be red- shortness, but what should be termed slag-shortness. In re-piling and re-heating this iron several times this defective appearance is gradually removed, and crystalline iron of great purity and toughness is produced. But a more ready mode of treatment was suggested by Mr. Samuel Lloyd, one of my co-Directors in the Towcester Company, in reverting to the ancient refinery or char- coal hearth. The balls as they come from the rotator, are placed under the shingling hammer and beaten out into flat cakes not exceeding an inch in thickness. These are cut by shears into pieces of suitable size and formed into blooms of about 2 cwts. each, which are consolidated under a shingling hammer and rolled into bars. The bars have been sold in Staffordshire and Sheffield at prices varying from £7 to £9 per ton, being deemed equal to Swedish bar as regards toughness and purity. It may therefore be asserted, as a matter of fact, that iron and steel of very high quality can be produced from ores not superior to Cleveland ironstone by direct process, but the question remains — at what cost can this conversion be effected ? The experi- mental works at Towcester are unfortunately not sufficiently com- plete to furnish more than the elements upon which the question of cost may be determined, the principal reasons being that the one re-heating furnace and a 30 cwt. hammer at the works are not sufficient to deal with the iron produced by the three rotators, that the iron has to be finished at a rolling mill elsewhere, and that transport weighs heavily upon the cost of production. The prin- cipal factor in the calculation of cost is unquestionably the rotator, and Table I, furnishes the working result of eighteen consecutive charges as taken from the charge book. The mixture of ores consisted for each charge of 12 cwts. of Towcester ore (containing about 38 per cent, metallic iran), 8 cwts. of calcined Great Fenton ore, 1 cwt. of tap cinder, 1 cwt. of limestone, and 6 1 cwts. of small coal. The time occupied for each charge was about 4j hours, and the yield of hammered blooms was, on an average, 6 cwts. 2 qr. 13 lb., whereas the metal contained in each charge, amounted (by estimate) to 8 "2 cwts., showing a loss of 19'3 per cent. This loss is, however, partially recovered in using Sffi WILLIAM SIEMENS, F.R.S. 345 a portion of the cinder again in succeeding charges, but the pro- l»onion of cinder that may be so used with impunity, depends upou the amount of phosphorus, sulphur, and alumina contained in the ore.* The coal used in the producers amounted to 2 tons per ton of hammered blooms produced, and in pricing the mate- rials used and labour engaged upon the work, the table — prepared by the manager at the Works— gives £3 8s. as the cost per ton of hammered blooms. To this amount must be added repairs and general expenses, and the cost of rolling the hammered blooms into bars, which in the case of Towcester practice are very heavy, but of which an experienced ironmaster would form his own esti- mate. The cost of working the metal in the hollow fires is also not included, and this may be taken to add from 25s. to 80s. to the ton. The refined iron so produced will, therefore, cost from £5 5s. to £5 10s. per ton. Tables II. and III. give the analyses of irons produced from various descriptions of ores, and Tables IV. and V. give Kirkaldy's tests of the mechanical properties of the iron ; but it should be under-stood that these tests were taken with a view to ascertain the influence of different methods of manipulation rather than to show high results. Only a small proportion of the samples had been subjected to the refinery process, and the variable percentage of phosphorus may be taken really as indicative of the extent to which the cinder had been removed from the metal. Table VI. gives the analyses of slags produced in the process. These are no doubt rich in iron, but it must be remembered that in the case of comparatively pure ore they can be used almost entirely in succeeding charges, and that in the case of ores con- taining much sulphur and phosphorus they are the recipients of those impurities — in the same way as the puddling cinder carries off the same impurities in the puddling furnace — and thus serve a useful end. If rich ores, such as hematites, are available, it is more advan- tageous to use a stationary furnace, and to modify the process as follows. * Since this paper was prepared, further experience has shown the possibility of obtaining greater yields of iron from the ores employed, and of making, at the same time, a greater number of charges per 24 hours ; some of these results are recorded in Tables VII. and VIII., which may be considered as appendices to this paper. 346 THE SCIENTIFIC PAPERS OF A mixture is prepared of pulverulent ores combined with fluxing materials and reducing agents in suitable proportions, and of this 4 to 5 tons are charged from a platform into the heated chamber to the depth of some 12 or 15 inches. But, before charging the mixture, some coke dust or anthracite powder is spread ov r-< £s 1 oa 2 * M ,2 IM e>« S « 55 S M II II II II II II R- « o 55 1 h S j JH 2 °^ 2T *"" ^* 41 O .2 ° rf 5 3 O O O O O O » —i ^ c. oo e>« i- JJ C • 6-1 2.S . | !!!.!!! i| c -** ^h O rH O O lit 5 1 X X X X X X g c» eo o e» g eo eo eo eo co eo ^"2=0 S 5-^ - = 1 o £5 . . |»1 33 m at «K at ai « S^3! 0 •X.'X *x 'X "X 'X - ': :-: 'I '.= '.£ '=' •£ -.5 •-. ,CO .CO .M .30 .CO .« 0 H u 0 -» $ - « s 1 « § 00^ \ 0? 00_ S 350 THE SCIENTIFIC PAPERS OF tt 55 21 HI Appear- ance of Fracture. i -si - -1 JL* * S = r5£ - = | g «£ M a 0 o «> ip h-

AH co co oo IN n I-H £- co o ooi'j'oo 5 X H 3 COGC CO S-) GO CO OimScO CO 0> H IN rHt-COO O >N -* GO t-H i i i o Square Inch of Fractured Area. „; IN r F-T cT t-T cT t-T t-T 1- 1C 1- O O 0 <0 0 | 8 o CO»O COO5 OOO COQO C-* I— ' OlrH WrH CN f— I Oi-COO OCOiOS Of'OO rtO«CO 1 S OOt-C> •M'J'CiCi iOC^*»iO Ot-OO 1 5 - §'^) oo o i~ c; *-O *o c-3 « ri oo c^ ^ o 3i -O O '-O O 1 - 'C *-O OO t - O -i< Cs X O •* I •< 3 OOCOm!NOO M«OO ifJtOOOOS Md'J'OO Or-i(Mr-i O^'MO) OO"^ OOrt^-1 s a XXXX XXXX XXXX XXXX OOOO^'-O iCp-<>i r-CT Swc^i C3C$ e^w ^HI^-I ^«I^ CO_ -O 0__ of i-T i-T cT cT oT oo~ r-T OO 4O*O *O-^ ••*•**< t-ocoi— i o^-»c; o -^to^ci cotc^oo . _^.ij.i_ c-. o-f^i o«r-i- or7OrH S O5Cq»r3tf3 CO'XH-CO OCO!N CirfOO 2 & T (N(MOr- O>-o >o o -o •« •* «n ic tn >o •* >*<•*•*•* •3 i- -o o o o "0 i- « o i~ o o >o ea c^ o «: tococot— «»TiOto i— IOI-M »orH^oo _2 COi-IJ-O OOiTftO Ol-Ot- •*r^--OO I J 1- t- •£, 1— to '•£> CD tD r-D »O O O >O iC »O •* i 00 00 r-l i— 1 COOOrHt-t tOMCiCi (OlMOICi O3C1WCO C^OICOCO f^^Hl— I^H ^Hf-lrHrH j •< a •a ssi^ 8883 s?sss -s?s;s5^ o 1 8 XXXX XXXX XXXX ,XXXX COXOJOO C/)OOCOGO COOCQOOO 'OOQOGCQO "N N ffl Cl (NIM"MC^ (MC^(NC^ CIC^C^C^ s 0 i 1 1 ++ 1 1 ++ 1 1 ++ 1 1 ++ ~0 . .g-6 ri-||c ^ ^"3^' 3 ^^o __."« . . . -S 2 ® -.-"5 ...... 1 R Srtv C w3v C C — rt _H S w«S -H <"=£ •OO OOO^ SS^S ^jT^T-^ -^ •*"•*' -t **" -** ••*'•'* •* •^• jgO3 r s Si WILLIAM S/KMENS, F.K.S. 351 TABLK VI. \v u.YSEs OF SLAGS FROM ROTARY FURNACE. 1 2 8 4 5 6 '•• of iron . . . . l->-63 traces 19-50 7-05 • If. of iron . .•Ir of lllilllpllll-M- . Sulphuric uc i>l Phosphoric acid Alumina .... Slli.M I.imi' 40-20 •50 •458 4-94 15-56 29-00 2-68 17*00 '•99 5-40 18-90 •82 55-83 i-io 3-05 " -869 10158 1-65 •518 257 10-20 14-50 5-60 I.;--, •489 1 -032 10-50 28-10 2-09 !••_•: •768 20-40 18-80 trace Total SHl'338 99-02 100-009 100-008 100 381 99-753 Metallic iron 35-93 .13-64 43-42 44-39 30-51 43-25 No. 5 first tapping. No. 6 second tapping. TABLE VII. CHARGES MADE IN "C" FURNACE AT TOWCESTEU Description of Charge. In Charge. Time. Yield. Iron. Coal. Blooms. Gaiii % Loss0/, Lbs. Lbs. H. M. Lbs. Scale . 1,008 Ibs. . 1 1,250 T-'s 3 55 l,l-»8 8-16 Cindi-r. . . 784 Ibs. . M 4 50 1,152 7-84 Soinorrostro . 224 Ibs. . ) ,, 5 0 728 4-17 Towivster . . 224 Ibs. . ,, 3 30 1,180 5-60 Limestone . 112 Ibs. . J M 3 35 1,232 1-44 » » ,, 3 SO 1,15(5 ,. 7-52 Same charge as preceding ones,'! with the addition of 108 Ibs. of 1 Fentonorelumpsusedforfettling f 1,330 4 10 1,232 7-86 4 15 1,200 8-00 4 30 1,456 9-47 4 10 1,038 23-15 3 50 1,883 7-36 4 0 1,174 11-73 5 10 972 26-91 3 50 l,4tt 7-67 5 15 1,488 11-88 3 10 l,-24(> e'-ai 4 15 1,092 17-89 4 5 l,17(i 11-57 4 0 1,386 4:21 4 30 1,900 5-26 5 5 1,280 8-76 3 55 1,.V-'0 14-28 4 25 1,168 ms 3 45 1,106 16-84 3 50 1,218 8-42 3 25 1,162 12-63 2 52 1,156 13-08 Averages . 131'."2 728 4 8 1.232 6-07 °L low. 352 THE SCIENTIFIC PAPERS OF TABLE VIII. CHAKGES MADE IN " C " FURNACE AT TOWCESTEE. No. Description of Charge. In Charge. Time. Yield. Remarks. Iron. Coal. Blooms. Gain % Loss % Lbs. Lbs. H. M. LbS. 1 fSame as charges - Nos. 2 to 13 follow- 1 j ing, but without I •\ Fenton lumps, 1 and with ' only 1 784 Ibs. scale J .1,100 728 4 0 966 12-18 ( Small charge to clear fur- nace of ac- cumulations on lining. 2 Scale. . l,0081bs.^ 1,310 728 4 10 1,248 4-65 3 Cinder . 7841bs. 4 0 1,153 11-90 4 Somorrostro 2241bs. 3 35 1,309 o-oo 5 Towcester . 2241bs. ) 3 50 1,360 3-89 6 Fenton lumps 1121bs. n , 3 20 1,195 870 7 Limestone. 561bs. , 3 30 1,288 1-68 8 Coal . . 728 Ibs. J § 3 50 1,090 17-55 9 n j 3 40 1,153 11-91 10 n j 3 45 1,097 16-18 11 yj t s 3 25 1,283 1-98 12 ,, M , 3 40 1,092 16-64 13 ,, , 3 40 1,103 15-57 (Same as charges 14 Nos. 2 to 13, with ( ( 3 5 1,029 21-45 15 the limestone in- } . 3 25 1,032 21-22 16 creased from i 3 35 1,005 23-20 561bs. to 1121bs. J 17 ,, n 3 0 1,059 20-68 18 ,, j, 3 5 1,069 18-31 19 ,, , 3 5 1,122 14-27 '20 » i 3 0 1,019 22-14 21 „ ?| . j 3 15 1,044 20-22 (Same as charges^ 22 Nos. 14 to 21, Fen- 1 1,250 ^ 3 15 963 22-88 23 ton lumps being f t 3 15 951 23-84 omitted . J 24 j 3 0 1,123 10-88 25 3 0 1,156 7-52 26 j 3 20 1,106 11-36 27 3 20 1,004 1800 28 j 2 50 1,021 18-24 29 3 10 1,091 12-48 30 j 3 10 1,003 19-68 31 ) 2 55 1,126 9-84 32 3 15 900 28-00 33 3 0 1,128 9-68 34 2 40 1,121 10-80 35 2 50 1,178 5-60 36 j ( 1,205 4-32 37 ! S"d 1,223 2-08 38 2 45 934 25-20 39 3 0 1,159 7.04 40 3 0 1,031 17-22 41 2 55 1,100 11-92 42 M ! 3 0 1,310 4'"80 43 ii .. . 2 45 1,313 5-28 \ ^__ / Averages . . 1,274-4 728 3 12 1-113 12-6 % loss. S7/? lVILL!A.\f SIEMENS, f.R.S. 353 In the discussion of the Paper •ON THE SEPARATION" OF CARBON, SILICON, SUL- PHUR, AND PHOSPHORUS in the REFINING and PUDDLING FURNACES and in the, BESSEMER CONVERTER ; with some Remarks on the MANUFACTURE AND DURABILITY OF RAILWAY BARS," by Mr. I. LOWTHIAN BELL, M.P., F.R.S., and some further remarks regarding "THE PRODUCTION OF IRON AND STEEL BY DIRECT PROCESS," by Mr. C. WILLIAM SIEMENS, D.C.L., F.R.S. THE PRESIDENT * (Mp,. C. "W. SIEMENS) said that perhaps he might be permitted to explain a point to which Professor Williamson had referred, as it might save time hereafter. Professor Williamson wished to know how it was that in a rotative furnace the phosphorus did not go back to the metal, seeing that the temperature must be as high as in a puddling furnace. This question would give him the opportunity of explaining the action as it took place in a rotative furnace. Thirty hundredweight of material was introduced into the fur- nace ; and heat was applied — intense heat, if they liked — to work upon this mixture. At first the temperature of the mixture did not rise, because the work that had to be done was carried on, as it were, at its own temperature — that of the reducing point of iron ore. But as the deoxidation of the iron proceeded, the tempera- ture would rise, and a point would be attained where metal would become malleable ; but at this point the fluxing materials, which had been mixed with the ore, would have commenced to be fluid, and would form fusible slag which, immediately upon fusion, would away from the mass, sinking to the bottom of the rotative whereas the solid material formed on one side, and rolled about until it went into balls. Hence, although the flame that * Excerpt Journal of the Iron and Steel Institute, 1877, pp. 389-395. VOL. I. A A 354 'TH-E SCIENTIFIC PAPERS OF was brought into the furnace would produce a full welding heat if it was continued, yet the essential work done was accomplished at its own temperature, just as water would be evaporated at its own temperature in a boiler, whatever might be the intensity of the heat applied outside. Probably to this circumstance was attribut- able the fact that the iron when taken out of the furnace was really free from phosphoric acid. But he attributed in large part this freedom from phosphoric acid in the iron to the circumstance that the phosphorus was combined in the ore — very often combined — with oxygen and lime as phosphate of lime, and to the fact that it would take a greater heat to disturb this compound which already existed than would suffice to retain the phosphorus in com- bination with metallic iron after having been combined with that metal in the blast furnace. This argument would lose its force probably if the time allowed for these reactions was unlimited, and it must further be borne in mind that the final chemical reaction in both the puddling and direct process did not probably exceed a quarter of an hour, during which dephosphorization would go on in the one and phosphorization in the other process to a limited extent. No one would be better able to judge than Prof. Williamson to what extent this question of time might be expected to influence the final result in the two processes. Before proposing a vote of thanks to Mr. Bell for his valuable communication, he would reply very shortly to some of the remarks that had been made with reference to the paper he had had the honour to bring before the Institution. Mr. Ridley wished him to explain how it was that in dealing with an ore containing much phosphorus he should be able to get an iron free from phosphorus, whereas in the puddling furnace a cinder containing 5 or 6 per cent, of phosphoric acid would readily com- municate that phosphorus, or a portion of that phosphorus, to the iron. In dealing with chemical processes they had, of course, to take into account all the circumstances of temperature, and the relative proportion in which the substances liable to act upon one another existed. Now, he explained yesterday that in treating poor ores, and poor ores containing a great deal of phosphoric acid, in a rotatory furnace, such as the one erected at Towcester, care was taken that a very fluid cinder was the immediate result of the heat acting upon the mixture. The first action of the heat upon SfK WILLIAM SIEMENS, F.R.S. 355 lixture was no doubt the reduction of the iron, but as the n •dilution got more and more completed the fusion of the earthy iluents immediately set in, and it set in practically before the n'.Iiu'iiuii was completed. The moment fusion took place, which was necessarily at the minimum temperature, the cinder drained a \viiy from the iron, accumulated at the bottom of the rotating 1, whereas the iron separated more and more from it, and as soon as the cinder had accumulated in any considerable quantity it was tapped from the vessel. The result was that the first cinder coming from the vessel contained a considerable quantity (he had seen and tested it even up to 8 per cent.) of phosphoric acid. At that time the temperature of the vessel was not sufficient to re-act upon the phosphate of lime or other chemical combination in which the phosphorus was held in the slag so as to bring it back to the metal. If the temperature was now pushed forward in the rotative vessel, that action, which had been so ably described by Mr. Hell in reference to the puddling process, no doubt would set in there also. The iron would gradually but slowly take up the phosphorus again, but, in order to break up the combination in rhich the phosphorus was by that time comfortably settled, time iras required ; and in that process, although the total duration of 3h operation was between three and four hours, yet the time luring which the metal was in contact with the fluid cinder was rery short indeed, in fact, the ball was brought out as soon as the ictal would hang together, and it was purposely brought out at as >w a temperature as possible, in dealing with impure ore, and cinder squeezed out as he had described in the paper, not by jueezing it or hammering it in large masses, but by either lering it flat out or rolling it into thin sheets, squeezing the ider out, and dealing then with the bar metal either in the linary way in the re-heating furnace, or, what was better, in a lollow fire, where the cinder was more thoroughly washed out from 3 metal, without increasing the temperature very rapidly, to such extent as to make the phosphorus go back to the iron. There- )re, he thought there was nothing contradictory in those results ' all those circumstances were taken into account, and at any rate analysis showed that iron was produced from very impure ores ctically free from phosphorus, and what was very curious, )metimes charges from ore containing a great deal of phosphorus A A 2 356 THE SCIENTIFIC PAPERS OF were almost entirely free from that ingredient, whereas other charges made of richer and better ore, contained phosphorus in somewhat more tangible proportion, owing no doubt to the presence of cinder which had not been sufficiently removed before the iron was consolidated. Mr. Bell, in criticising the process which he (the President) had submitted — and criticising it very fairly, and contrasting it with the method of treating iron rich in phosphorus which he (Mr. Bell) proposed — observed that, in dealing with Towcester iron, he (Dr. Siemens) found it necessary to mix richer oxides with it, and that that would put the process altogether out of consideration in dealing with similar ores in the blast furnace, but it must be remembered that Towcester ore could not be smelted in the blast furnace by itself either. It was a very valuable ore as an admixture with other ores, on account of the large proportion of alumina which it contained, but all attempts to smelt it by itself in a blast furnace had hitherto practically failed, and, therefore, it was but reasonable that they should find it necessary to mix other ores with the Towcester ore. Then his friend, Mr. Bell, said that he (Dr. Siemens) required forty-two rotators to produce the metal yielded by one of his great blast furnaces.- That was very true, and if the two apparatus produced the same results he would say at once the blast furnace had the advantage ; but it must be remembered that the blast furnace pro- duced pig metal, whereas the rotator produced wrought metal, and that probably forty-two puddling furnaces were required, in addition to the blast furnace, in order to produce the same result ; therefore he, at any rate, had the advantage of one. Mr. I. L. Bell, M.P,, remarked that he had been talking of steel. The President said he would come to that presently. There- fore, as far as wrought iron was concerned, the number of apparatus required was certainly not greater, and it must be remembered that the results which he had placed before the meeting were by no means final results (that they were tentative results, and that they hoped to do a great deal better), whereas with the blast furnace, after the powerful mind of his friend Mr. Bell had been given to it for so long a time, he supposed they had very nearly reached finality. Then, his friend found fault with his consumption of coal, three tons being required to produce a ton of S7X WILLIAM SIEMENS, F.R.S. 357 malleable iron. Well, that was higher than he wished to see it, but Mr. Bell admitted it was no higher than his consumption in smelting nud puddling iron. Mr. I. L. /Icll, M.P. : No ; smelting and making into steel. The President : I am now speaking of iron. Mr. I. L. Bell, M.P. : Pardon me, Mr. President, for interrupt- ing you. 1 was contrasting the conversion of iron from the ore into steel by the two methods, considering the fact that we have steel to look forward to. The President : Mr. Bell says he wishes to compare my iron with his steel, but in the description which he gives of his process I do not see a trace of steel. He describes a method of purifying the pig metal of its phosphorus and then transferring it — remelting it, it appears, before he can puddle it, and then he says this puddled iron may be converted into steel in an open hearth furnace ; but he fails entirely to bring forward any proof that by his method he produces steel in one operation. Mr. L L. Bell, M.P. : You must let me explain, please. I am quite willing, sir, to admit that if you can make bar iron by your process from a poorer ore containing phosphorus, it is obvious that there are certain advantages in doing so ; but if you inform us that you require richer ores free from phosphorus, this is a totally different matter. I did not intend to compare your process with the one I had previously described, and I hope nothing I said induced the meeting to imagine that such was my intention. All I wished to draw attention to was that portion of your charge which consisted of hematite, and the question I raised was whether such ore was most economically treated by being made into malle- able iron, and then converted into steel, than by being smelted in the blast furnace, and the pig iron then treated in the Bessemer converter or in the open hearth for the purpose of obtaining steel. The President said he wished, first of all, to reply to the obser- vations with regard to the production of iron, considering iron as the goal to which they tended. If he had rich ores, and wanted to convert these rich ores into steel, he modified the process entirely ; and, indeed, he described the modus operamii which he adopted in that case. If he had rich ores and wanted to make steel, he put five or six tons of a mixture of that rich ore with fluxing material and carbonaceous matter on the bed of an open 358 THE SCIENTIFIC PAPERS OF hearth furnace — a regenerative gas furnace — and he applied heat to it for several hours, until a thick crust of metallic iron was formed all over the surface. He then added, on the surface of that, pig iron, perhaps in the proportion of about 25 to 30 per cent, to the amount of iron contained in the ore, and that pig metal as it melted acted upon the crust of metallic iron formed in the furnace, melting it gradually, and constituting with it a bath of steel, which, after being adjusted and mixed with the requisite amount of manganiferous material, was tapped into ingots and worked in the usual manner. In that case he did not touch the ore from the time he charged it into the furnace to the time of tapping it from the furnace as liquid steel, and he believed a more direct process could not well be conceived. But that process of converting rich ore into steel was not applicable to poor ores and to ores containing a great deal of such materials as phosphorus and sulphur, which would undoubtedly go into the ingot metal if they were left in contact with it at a high temperature. There- fore, they must draw a broad line of distinction between the process of making iron and that of making steel. In dealing with poor and impure ores they could still make steel from them, but, in that case, they must eliminate the earthy matter, the sulphur, and the phosphorus, at a low temperature, and then re-melt the material at a high temperature. That was an extra operation, which ought to be paid for by the difference in the cost of the ore. In that case, if they dealt with those impure ores, they had to go so far on the road of making wrought iron as to take the metal out of the furnace and squeeze it or roll it in order to get rid of the cinder. Then it was in a proper condition to transfer it, either to the re-heating furnace to be worked up into wrought iron, or into the bath or open hearth furnace to be converted into steel. With regard to his friend's process (and he supposed he would allow him now, on his side, to make some objections), his objection to it was that it was an additional process, which necessarily would cost money to accomplish, and he doubted very much whether the iron resulting from his refinery furnace would work in a Bessemer converter. Mr. I. L. Bell, M.P. : I said this was doubtful. The President: Mr. Bell admits it; therefore, it had to be treated and used as iron, or that iron would be melting material WILLIAM SIEMENS, F.K.S. 359 for the open hearth process, but sti.l in that case they would have to compare his results with those obtained by simple puddling, i he President) had lately made some experiments at the request of Messrs. Hopkins, Gilkes, and Co., which proved in a satisfactory manner that Cleveland pig metal, when puddled r.nvfully in a rotative furnace, and then melted on the open hearth furnace, produced a very good steel. He believed Mr. Hopkins had exhibited some of the steel upstairs which was so produced, and Mr. Cramptou had given them proofs long before that time of the suitability of Cleveland pig to produce steel if treated in his (Mr. Crampton's) puddling furnace, and subsequently in his (Dr. Siemens's) open hearth furnace ; therefore, in that case they would have to compare the results obtained by the refinery process proposed by Mr. Bell with those of ordinary puddling done in the most careful manner. In other respects he was ready to compli- ment Mr. Bell upon his very valuable communication. He had placed before them experimental facts which he (Dr. Siemens) believed were entirely reliable, and which in themselves consti- tuted most valuable information. Whether or not the particular process which he had lately followed would lead to practical results or not, was a matter which perhaps did not interest even Mr. Hell very much, because he was searching for information at present, and in those researches he was powerfully assisted by the North Eastern Railway Company, who — acting very differently to railway companies in general — encouraged research instead of rather throwing impediments in the way of those who proposed any new method of manufacture. His (the President's) experi- ence had been that even when they had got a result it was very difficult to make people take the trouble to test that result, and it was a very refreshing sign that here a great railway company not only encouraged research, but found large means for carrying that research into effect. One of the implements proposed to be used in carrying out those researches was a very large hydraulic squeezer. That machine had been constructed by Sir William Armstrong & Co., and they would have an opportunity of seeing it to-morrow. A vote of thanks having been passed to Mr. Bell for his valuable paper, Mr. Menelaus said the President could not very well include 360 THE SCIENTIFIC PAPERS OF his own name in that vote of thanks, but he (Mr. M.) would ask them to pass a hearty vote of thanks to their friend, Dr. Siemens, for the paper he read yesterday, and on which, with Mr. Bell's they had had such an interesting discussion, although the two were opposed to each other on certain points. He was quite sure that if his (Mr. B.'s) process was to be successful, he must go hand-in-hand with Dr. Siemens, and use his open hearth for converting the material which he was modest enough to say he was purifying for the purpose of using it in the shape of iron. He was quite sure that his (Mr. Bell's) meaning was to make steel, and, if he was going to make steel, he must go hand-in-hand with Dr. Siemens and use his open-hearth furnace. A vote of thanks was accorded to the President by acclamation. On the presentation of THE BESSEMER MEDAL To PROFESSOR VON TUNNER, THE PRESIDENT * (MR. C. "W. SIEMENS) observed that, thanks to the liberal provision of our past President, Mr. Bessemer, it was the pleasurable duty of the President of the Iron and Steel Institute, at the ' beginning of each year of office, to present this medal to any gentleman who, in the opinion of the Council, had highly distinguished himself in that branch of science which the Institute specially cultivated. The choice of the Council had this year fallen on a gentle- man who, all would agree, was fully entitled to the distinction. Members of the Institution all knew Professor Tunner by repute, and those who did not know him personally would also be pleased to learn that this compliment was paid to a gentleman who, although drawing towards the close of the average period of active life, yet retained all the energy and all the active interest in his work that made it still productive of useful results — a gentleman * Excerpt Journal of the Iron and Steel Institute, 1878, pp. 8-10. S//? WILLIAM SIEMENS, F.R.S. 361 who, by his amiable, modest manner, impressed every one very much in his favour. It was, however, not his personal qualities wliivh the Institute had to look to. Professor Tunner was, it iniirlit be said, at the head of a very ancient iron district. Styria hud produced for centuries iron of very high quality. The cutler of Damascus had for centuries forged his blades of Styrian iron — at any rate, Styrian iron had entered largely into the composition of the material of which those blades were made ; and he remem- bered that when, in 1851, the International Jury made certain itnents upon the scythes sent from Styria, they were perfectly surprised to find that the keen edge of those implements would cut off the head of a nail without being injured by the operation. Nature had been very kind to the ironmaster of Styria in providing him with a spathose ore of extraordinary purity, and with a fuel in abundance of the highest quality in the form of enormous and beautiful forests. Still, with all those advantages, results such as we heard of could not be realized without skill and the application of scientific knowledge. In this country, we were very proud of our achievements in blast furnaces, but the Styrian furnace, although a different thing from the blast furnace of this country, was one of peculiar merits, and the economical results which had been obtained from it were very surprising. He learnt that a ton of iron was smelted with something like thirteen cwt. of charcoal. That result was a remarkable one, although, of course, it could not be fairly compared with the results obtained from coke and the inferior ironstones of this country. Professor Tunner might be said to be the leading spirit in that centre of industry. It was unnecessary to enlarge upon his literary works, which were well known to members, and which were largely quoted in our excellent "Metallurgy" by Percy ; but Professor Tunner had for many years been active in educating young metallurgists who had done good work in Austria, and who had also given us indirectly some benefit. We were now receiving from the district of Styria a large supply of ferro-manganese, a material which we could not produce from substances of our own. Professor Tunner had been active on many commissions, in which his practical sense, and his thorough mode of investigation, going to the very foundation of every matter that came before him, had left a remarkable impress on inquiries into metallurgical subjects. I therefore think (the 362 THE SCIENTIFIC PAPERS OF President concluded), that members will approve the action of the Council in giving our annual award of the Bessemer Medal to Professor Tunner. I have great pleasure, Mr. Bell, in presenting this medal to you, as representing Professor Tunner on this occasion, and I hope you will convey to him the high appreciation in which he and his works are held amongst us. In the discussion of the Paper "ON THE SEPARATION OF PHOSPHORUS FROM PIG IRON," By J. LOWTHIAN BELL, M.P., F.R.S., &c., THE PRESIDENT* (MR. C. W. SIEMENS) remarked that Mr. Bell had contributed some valuable facts on a subject which interested many members. Mr. Bell had found that he could, by treating Cleveland pig metal in a rotating furnace (such as was to be seen at the Clarence Works), reduce the phosphorus to the extent of from T3oths to -rijths per cent. ; but other results had been given, showing that the phosphorus had been reduced below TVth per cent., while the slag produced gave- 6 and a fraction per cent, of phosphoric acid. These figures relating to phosphorus in the slag and in the metal, agreed well with the results which he himself had found in treat- ing the subject in another way. At Towcester, in the rotary furnace, according to figures given by him at the Newcastle meet- ing, the slag was generally found to contain from 6 to 7, and sometimes 8 per cent, of phosphoric acid ; but the metal produced in that process had been brought to a very low percentage indeed. So far, therefore, we might consider it an accomplished fact that, whether they dealt with pig iron or with ores containing a large percentage of phosphorus, that phosphorus could be eliminated to * Excerpt Journal of the Iron and Sttel Institute, 1878., pp. 41-44. SIR WILLIAM SIEMENS, F.R.S. 363 such :IM extent as to make the metal perfectly applicable to the production of steel. The question as to the relative merit of the two modes of doing it was one of expense, and on that subject they were still without sufficient information. Mr. Bell had given rertjiin data which commenced with Cleveland pig metal. He subjected the material to a refining process, and in that operation he used 10 cwt. of oxide of iron to the ton of metal. Now with- out desiring in any way to discourage Mr. Bell and his friends, he thought they would have to modify that process before they could tempt steel manufacturers to use it practically. The employment of 10 cwt. of rich oxide of iron, which could nob be valued at less probably than lUs., would form an item of expense altogether out of proportion to what was now practically admis- sible. Adding to that, the cost of the operation itself, and the fuel used, he thought there would be no margin in favour of using the cheaper Cleveland as compared with the dearer Cumberland metal. But, as Professor Williamson had said, some bases might be found to take the place of oxide of iron ; and Mr. Snelus had brought forward a scheme, which he had been working out, to employ lime for lining. For his own part, he could not look with much favour on that proposal. At his experimental works at Birmingham, he had made an experiment with a lining of that description. The difficulty he found was that the lining was not sufficiently hard to resist the action of the charges. He thought that as much heat was applied as the material could stand, but the limestone employed contained a percentage of magnesia, which rendered it fusible to some extent, and probably prevented satis- factory results from being obtained. With regard to the extent of phosphorus allowable in the steel, he might speak with some confidence, having made a great many experiments, and having seen the results on a large scale in a process of making steel from materials containing a considerable percentage of phosphorus. There was no difficulty, for instance, in converting old iron rails — which might be to a great extent Cleveland rails — into steel rails of such quality as would satisfy all the mechanical tests that engineers insisted on. The limit he would assign to phosphorus in such a material was j per cent. In increasing the amount of phosphorus in steel beyond £ per cent., there was great danger of making the steel brittle — that was to say, of making it liable to 364 -THE SCIENTIFIC PAPERS OF fail under the test of a falling weight. That difficulty increased very much with the reduction of temperature. On a hot summer's day such a rail might resist the test, but on a cold winter's day it would not. Another very essential condition was that the steel rail containing \ per cent, of phosphorus should contain certainly less than -^ths per cent, of carbon, and considerably less in order to withstand the falling weight test, and it must contain not less than T7oths per cent, of manganese. Such metal would stand almost any ordinary mechanical test that could be applied to it. He could quite believe the result which had been given by Mr. Price, that he had produced a metal containing T%ths per cent, of phosphorus, and -^ths per cent, of carbon, which would stand the Admiralty test, but he could not go with Mr. Price further than that. It might be said that manganese was to the steel maker what charity was to religion : it covered a multitude of sins, and these were of a lucifer kind — phosphorus and sulphur. If you gave him the worst class of iron, and wished him to make steel of it that would stand the Admiralty test, he would undertake to do it ; but such steel, nevertheless, should not be used in such appli- cations as were now contemplated of mild steel — no boiler should be made of it, no forging should be made of it, and he thought also no ship should be made of it. Steel of that description depended for its mechanical qualities on the larger dose of manganese which it contained. Now every practical steel maker knew that manganese was a somewhat treacherous element in steel. Its distribution was never so uniform as to make a homo- geneous compound. Then, in the working of a plate containing a large amount of manganese, the manganese was apt to be burnt out, and in attempting to flange it, although sometimes it would stand the test, at other times it would break. That was a question to which the users of steel should direct particular attention in order to prevent failure in the application of a comparatively new material. Good mild steel, such as could be safely recommended to the boiler maker, should contain only mere traces of man- ganese ; TVth per cent, was about the limit which he considered such steel could contain with entire safety, when the material had to undergo certain preparations in order to put it into its definite shape. Then, again, we heard a good deal about the liability of mild steel to corrode, and some results which had lately S/K WILLIAM SIEMENS, f.R.S. 365 to light seemed to throw great doubt upon the desirability of nsiii^ mild steel, especially in the Navy. He believed that a tendency to corrode was also the result of excessive manganese, and some experiments which he had himself made went certainly in confirmation of that view — that as the manganese in mild steel was increased, so its liability to corrosion increased. He quite agreed with the suggestion of Mr. Fox that the subject of the (|ii;ility and treatment of mild steel should be carefully inquired into. The Committee of Lloyd's Register were collecting experi- mental data regarding it, and the Board of Trade had also turned their attention to it recently ; but whether individually or col- lectively, the Iron and Steel Institute should not be indifferent to a subject so important. In tfw discussion of the Paper "ON SOME EECENT IMPROVEMENTS IN THE MANUFACTURE OF IRON SPONGE BY THE BLAIR PROCESS," by MR. J. IRELAND, THE PRESIDENT * (MR. C. "VV. SIEMENS) said the converting of ore into spongy iron was not new. It was first proposed by Mr. Clay, many years ago. "We had also heard much of the Chenot process, and after that there had been many other attempts to produce spongy iron. He himself gave very considerable attention to the subject at one time, and he had produced spongy iron by methods somewhat analogous to that which had been brought before the meeting. He did not think, therefore, that any particular name could be attached to the process of making iron sponge for the purpose of utilising that spongy metal in the after-process for the production of iron and steel. The difficulties which made him desist from his endeavours to arrive at a practical solution of the * Excerpt Journal of the Iron and Steel Institute, 1878, pp. 57-58. 366 THE SCIENTIFIC PAPERS OF problem in that way were several. The iron sponge locked up in it all the earthy materials of the ore, and if you threw it in the open hearth furnace these materials prevented liquefaction of that sponge in the metal. Another great difficulty was that the iron sponge absorbed sulphur at a most extraordinary rate from flame. In fact, he would deprecate any process of making the sponge or using the sponge afterwards, which brought it into contact with coke gas of any kind, as even the purest coke gas might give so much sulphur to the sponge as practically to make it unfit for steel. Mr. Ireland proposed a novelty which consisted in melting the sponge in a cupola furnace, and then puddling or otherwise treating the liquid pig metal so produced. He altogether failed to see the advantage of these processes. "We had an apparatus which made spongy iron better than any other, and that was the blast furnace. Take a blast furnace at a certain heat, and you had your spongy iron produced at the lowest possible cost and in a heated condition. Why cool it, and then melt it in a cupola ? There it was, perfect sponge, in the lower part of the blast furnace, heated and ready to be melted. He quite failed to see what advantage you could gain by dividing the process into two. Altogether, the difficulties connected with spongy iron were very great indeed, and were such as had induced him, at any rate, to abandon that mode of proceeding entirely, and to endeavour rather to treat the iron ore in such a way, that while the iron was reduced to the metallic condition, the earthy matter contained in the ore was at the same time fused and combined with the fluxing material. The product had been obtained by a method which involved but one instead of two intermediate processes, and which produced iron at once in a perfect metallic condition. He was sorry to be obliged to speak thus discouragingly of a paper brought before the meeting, but, as Mr. Bell had said, it was much kinder to point out plainly and clearly the objections one felt because it could not be to the advantage of the inventor or patentee to be encouraged in a direction which was open to objection. If Mr. Ireland could show that these objections were inapplicable to the process he brought forward, he should certainly be most happy to congratulate Mr. Ireland on having overcome difficulties which had made himself desist. SfX WILLIAM SIEMENS, F.R.S. 367 /// t/M discussion of th* Paper " ON STEEL FOR SHIPBUILDING," by B. MARTELL, DR. CHARLES W. SIEMENS * said, with reference to the observa- ti<>n that fell from Mr. Reed, as to the difficulty of rolliug steel plates to dimensions that would present a reduction of weight n|;i:il to 20 per cent., T would mention that when the material for the Iris and the Mercury were ordered from the Landore Company, a wish was expressed by the authorities that the weights of the plates should in no case exceed those specified, but that it would be desirable to make those plates perhaps 2 per cent, less in weight than would follow from the calculation. I believe the Landore Company acted strictly up to that, and that the total weight of the material supplied was just 2 per cent, below that calculated, showing that there really is no difficulty in working by weight instead of dimensions. I would suggest that it would be a far more rational thing to order the plates by weight per square foot, rather than by vulgar fractions of an inch thickness. With regard to riveting, I, for one, would strongly advocate steel rivets in preference to iron. It is true that at Pembroke the experiments tend rather to show that no material advantage would be gained by the employment of steel rivets, but at that time the question was hardly sufficiently understood. Now steel has been produced which I think answers its purpose perfectly, and reduces the risk of rivet heads falling off to a minimum. I may mention that at another Institution, Mr. Boyd, the engineer of the Slipway Com- pany, will read a paper to-day giving the result of the construction of several steel boilers in which steel rivets were employed, and he states in that paper that not a single rivet gave way or gave any trouble whatever in the manipulation, showing that with a little care difficulties that have been complained of, such as overheating, may be overcome. The advantage of steel riveting over iron is not only in the rivet itself, but it is in a great measure in the plate, which has to be cut away to a much less extent, and thus * Excerpt Transactions of the Institute of Naval Architects, Vol. XIX. 1878, p. 29. 368 THE SCIENTIFIC PAPERS OP leaves a larger nett area of metal to resist the strain. Then again, if the rivets are put the same distance apart as they would be put in an iron plate 20 per cent, thicker, it is natural that these rivets stand too far apart for this reduced thickness of the plate, and thus throws a buckling strain on the plate. I would suggest that in riveting steel plates together, the distance between rivet and rivet should be the same as that which would be adopted if a thin iron plate were used — in fact, the reduction should be propor- tionate. The moment you use one material for the plate and another material for stitching the plate together, there is a dis- proportion between the two elements introduced which naturally must tend to weaken the whole. Perhaps I may be allowed to say one word before I sit down with regard to corrosion. Certain laboratory experiments which have been tried seem to show that steel corrodes faster than iron, whereas most of the working results that have come to my knowledge seem to show the contrary, and that steel wears longer. We have heard to-day of steel ships from Mr. Martell himself, that have stood wear and tear exceedingly well. But I have no doubt that some steel may be introduced which is liable to corrode at a greater rate than iron would ; and although I perhaps have no right to speak absolutely and definitely on the subject, I believe it is the result of an excess of manganese in that steel, and it would perhaps be well for steel users to turn their attention to that subject. Manganese is an exceedingly con- venient agent in order to give to steel, or homogeneous iron, the high degree of ductility which is desirable ; but it is by no means a necessary element, because at least the same ductility, and the same strength, may be obtained without an appreciable percentage of manganese in the material ; and my experience, which is some- what limited as to the wearing quality and resistance to corrosion of the two materials, goes distinctly to prove that with an increase of manganese beyond a very narrow limit the steel becomes more corrosive, does not weld with the same facility, and is not so abso- lutely uniform as when a little manganese is used. /•:!//•:. v\. I--.K.S. 369 fn I fit- discussion of the Paper «ON THE USE OF STEEL FOR MARINE BOILERS AND SOME RECENT IMPROVEMENTS IN THEIR CONSTRUCTION," by W. PARKER, I )u. Si KMKXS* slid, I think this paper of Mr. Parker's has brought • us some very important matter, and the questions arising upon it have been so well discussed already that I feel it is almost unnecessary for me to say anything. The Chairman. There is a question upon which you can give us some important information, namely, whether the thing called steel and the thing called iron exist any more as separate existences ? Dr. Siemens. Chemically the only difference is, that what we call mild steel is pure iron — it is more essentially iron than what is sold as such ; but as regards the physical properties of the material, it differs in many points from iron and ought not to be confounded with it, because if we were to call it iron and confound it with iron, we should think it right to treat it in the same manner, whereas it requires in many respects different treatment. In fact, Mr. Parker has given you one or two instances. I had occasion to allude at another place to one point which was brought before my notice very forcibly with regard to the steel boilers which Mr. Boyd has constructed. After testing samples of the plates that were supplied by the manufacturers the rumour was spread that the material was wholly unreliable — that instead of breaking through the riveted seam, through a narrow strip of metal, it broke through a line of 50 per cent, greater extension rather than through the narrow place ; and as iron would not have given way in that manner, and as the experience of engineers has been derived from iron, it was at first concluded that the new material was not reliable ; but it was soon discovered upon further investigation that the method of riveting employed had been such * Excerpt Transactions of the Institute of Naval Architects, Vol XIX. 1878, pp. 188-190. VOL. I. B B 370 THE SCIENTIFIC PAPERS OF as to be unsafe for this mild steel. Two large rivets had been put in a forward position and other rivets to make up the holding strength between the piece under test, and the shackles yielding were put back. In dealing with a material like this mild steel, the strain comes entirely upon the forward rivets, whereas the backward rivets being, as it were, the elongation of a much larger piece of metal, do not feel the strain at all. As it appears to me these two forward rivets were near the edge of the metal, and they set up a tearing action. Now, it was remarked that although the sample was expected to elongate 25 per cent, before rupture took place, it did not elongate at all, but broke in the manner already alluded to. In further testing this metal it was found to be per- fectly homogeneous and capable of an amount of elongation of 25 or 28 per cent, before breaking. If you take a strip of india-rubber you may elongate it to several times its length, but if you make the least nick in the edge of the india-rubber, and try to elongate it, it will tear readily. In the same way, if you give this mild steel a chance of tearing it will tear. In that case no elongation will take place, because in tearing the strain is confined to an infinitesimal amount of area, and its course in fracture will be the result not of the total amount of resisting area, but of the direction the tearing action may choose to take. With regard to riveting, Mr. Parker states, and perfectly correctly I need hardly say, that in punching a plate such as is used in the construction of large boilers, the metal in the act of punching is reduced 30 per cent, in strength. Mr. Kirk has already offered an explanation which is similar to the explanation I should give ; but with your permission I will draw attention, perhaps a little more, to the precise action that I conceive takes place in punching a thick plate of this material. Suppose the plate is being punched, the punch being above and the supporting die below it. As the punch penetrates into the metal, the latter does not immediately sever ; it will first yield by compression, and it will, as it were, be forced laterally into the mass of metal surrounding the punch, where it will create a zone of highly com- pressed metal all round the hole that is being punched. The metal beyond the zone of compression will be to a certain extent under tension. If the piece punched out is afterwards examined it will be found to be about 10 per cent, thinner than the original thickness of .SYA1 ll'lUJAM >•//; .J//:. V.S", /^.S1. 371 the plate, and that diminution in thickness is accounted for by these forces of compression and extension set up within the metal. If the metal is now subjected to a tearing strain, it has to resist besides this, the abnormal states of strain into which it has been thrown by the punching action, and is therefore destroyed by a force con- siderably less than that, it can resist in the original condition, as the paper shows. Now, if this plate after the punching has taken plan- is subjected to annealing, then this strain between metal and metal will be relieved and the plate will regain its full strength ; or if the strained metal be rimed away, and the hole be en- larged, the plate will have its full strength. But I have the results of some experiments which were made by Mr. Riley at the Landore Works, near Swansea, proving that punching does not ••ii the plate, but increases the strength of it. His experi- ments were not confined to one or two cases, but comprised a whole series that, strange as it may appear, went to prove that the punching absolutely increased the bearing strain of the punched plates, without annealing, to something beyond the strength of the plate per square inch before it was punched. I should first say he used the precaution to make the die larger, to perhaps a greater extent than is usually done, and the result was, to my mind, that the mass of metal under compression of which I have spoken was not formed, and that the plate was thus relieved from the abnormal strains generally produced in punching. Under these circumstances I can understand that a slight increase of strength should take place, for the same reason that when you subject a bar of metal of any form to strain, its strength will be increased. It is a subject, perhaps, not sufficiently understood, but I have had an opportunity of observing very extraordinary results in that way. Take a bar of iron or steel and subject it to a strain exceed- ing the elastic limit, and allow this strain to be active for some time, in testing the same bar again you will find not only the elastic limit has been raised, but that the ultimate breaking strain is considerably increased. In that way whatever strain you put upon a piece of metal you increase its strength, unless the strain is applied in such a way as to set up contending forces within the metal. Mr. Parker has alluded to two forms of construction with regard to marine boilers. The one is the admirable furnace of corrugated form which is represented by the drawings, and which B B 2 372 THE SCIENTIFIC PAPERS OF I quite believe is a step in the right direction. The other is an experiment of construction which I had occasion to make, and which, by Mr. Parker's request, I have put before the meeting. I was asked to design a vessel that could resist the pressure of at least 1,000 Ibs. per square inch, and with a capacity of not less than 100 cubic feet. The mode in which such high pressure air- vessels have been hitherto constructed has been in making them multitubular, but in resorting to that construction you get many joints and you have also a voluminous structure. It occurred to me that a better result would be gained by rolling cylindrical bands of metal from solid steel ingots — cylinders of 1 foot in depth and 44 inches in diameter. In rolling metal in this fashion you get the whole strength of the metal in the right form for re- sisting a bursting strain. The difficulty was to make joints between the cylinders, and this was accomplished by turning in the face of each a V groove of about \ inch deep, rings of copper wire of f inch thickness are thereupon placed between groove and groove, and the whole set of cylinders are screwed up and bolted together by sixteen or twenty long bolts made of steel of great elasticity containing about \ per cent, carbon, with a resisting power of about 50 tons to the square inch on the ends of the vessel. After screwing down these bolts hydraulic pressure was applied, and the vessel stood 1,300 Ibs. to the square inch without a leak, but at that point a great many joints began to weep. The bolts were then drawn up |th of a turn, when the vessel was found to be perfectly tight at the pressure of 1,300 Ibs., but the joints began to weep' again at 1,400 pounds. We might have continued the operation of drawing up and have reached a higher limit of pressure, and seen whether all the parts of the vessel were not strong enough to resist 2,000 Ibs. to the inch, but inasmuch as the vessel in use was only to resist a pressure of 1,000 Ibs. to the square inch, it was thought sufficient to tighten these bolts to the limit of 1,400 Ibs., because we felt that if ever the pressure should reach that point the bolts would yield owing to their elastic property, and allow the fluid within to escape, thus avoiding the risk of an explosion taking place. In that way vessels I believe can be constructed which are perfectly safe and capable of resist- ing a very high pressure. I may mention that in this form steel will bear a pressure of 45 tons to the inch with perfect ease and .s/A' WILLIAM SIEMENS, F.R.S. 373 v. It occurred to me, therefore, that marine boilers might be constructed on the same principle, by rolling a number of rings in this fashion and placing them one behind the other, with these copper rings inserted, and lx>lting the whole down. In that way we should have at any rate a boiler-shell capable of resisting •jon (.r ;;oo Ibs. pressure without the least risk of an explosion, wlu-reas in riveting very heavy boiler plates of an inch in thick- there is always some difficulty in treating the material. In the discussion of the Papers "ON THE MECHANICAL AND OTHER PROPERTIES OF IRON AND MILD STEEL," by DANIEL ADAMSON, C.E., Manchester ; and "ON CERTAIN MATTERS AFFECTING THE USE OF STEEL," by M. ERNEST MARCHE, Paris, The PRESIDENT * (ME. C. W. SIEMENS) said he would proceed to make a few observations upon the papers before them, com- mencing with Mr. Adamson's, which he thought was one of great practical merit. He agreed with Mr. Adamson both in his objection to short speci- mens and in his reason for such objection, but regretted that he had adopted a 10-inch specimen instead of the standard length of 8 inches ; for the 8-inch standard, or the length of 200 millimetres, had found its way into very large practice. It had been adopted first of all by the French Admiralty, and afterwards by the English Admiralty and by Lloyds, and it was of very great importance to have uniformity. There was, of course, no a priori objection to Mr. Adamson's standard, but it would render comparison of his results with those obtained by the Admiralty standard less easy, * Excerpt Journal of the Iron and Steel Institute, 1878, pp. 414-427 and 457-458. 374 THE SCIENTIFIC PAPERS OF and this was the more to be regretted as, in his opinion, ^Ir. Adamson's paper would be largely referred to hereafter regarding the mechanical properties of steel. "With regard to weldings, he would observe that all the speci- mens which Mr. Adamson had brought before them were very beautiful indeed, and he had succeeded in welding up an angle- iron ring in a very perfect manner ; but he (the President) objected altogether to welded rings. Why not roll them at once as they would roll a tire ? This had been done already to some extent in England, and he thought it was a very excellent prac- tice. The results which Mr. Adamson had placed before them regarding corrosion were very interesting. This question of cor- rosion, as they were aware, had occupied the attention of the English Admiralty, and had been discussed on several occasions. The results which Mr. Adamson now brought before the members of the Institute made steel come out much better than they could have hoped after the results that had been brought before them by the Admiralty Committee ; and he must say he could not see why a really pure metal like melted iron should corrode more than an impure metal where different substances were at war one against another. The reason why some specimens of mild steel had given such unfavourable results was in his opinion (and he simply repeated the opinion now) due to an excessive quantity of manganese. Manganese was a highly oxidisable metal, and if eaten out of the mixture, there remained only a sponge, which was easily de- stroyed. Altogether he fully maintained the view he expressed that manganese was only a cloak to hide imperfections in steel, and when they wanted a really high-class metal, they should have it as pure as possible, containing a little carbon in order to give strength, but as little of other materials as they could possibly do with. Manganese, no doubt, was a good metal for the maker. It enabled him to push stuff through the rolls, whatever it might be made of ; but now that they spoke of really high-class metal, he thought manganese was one of its worst impurities. Mr. Adam- son had also alluded to steel higher in carbon than the mild steel which was now used for engineering purposes. He thoroughly agreed with Mr. Adamson that it was absurd, in a bridge whore they wanted any moderate extensibility and great strength, to A7A1 \ni.UAM S//-.1//-.VS, F.K.S. 375 employ a nirt.il that \\oiild hear without breaking a tensile strain •..us, when th.'V mi-Ill have for tin' same money and with; (•;!<'• a iiii'lal I hat . \v n-iieaii h and the Bessemer metal. Ho had been always a greai admirer of the Bessemer process and a great friend of .Mr. l'« s 'iiier, but he thought Mr. Bessemer himself would probably take r\e.-pt jon to that sentence. Was it probable, he would ask, that if they commenced with the same pig metal, put a portion of it into a Bessemer converter, and another portion into an open- In ail h furnace, treating the one by blowing air through it, diminishing its quantity by 15 per cent., and treating the other with rich ore such as they used for the reduction of the carbon in pig metal on the open hearth, that the results would be the same ? II could not sec how the results could possibly be the same. It might be better in the Bessemer process than in the open-hearth for au^ht he knew, but it could not be the same. If absolutely pure pig iron were used, such as is found in Sweden, then the analysis might show no difference in the amount of phosphorus 376 THE SCIENTIFIC PAPERS OF and sulphur in the final result, because taking the half of nothing, it was again nothing. But if they had an impure pig metal to deal with, the simple diminution in weight must, as it was well known it did, increase the percentage of phosphorus and sulphur in the Bessemer metal, whereas the ore in acting upon the bath not only substituted for every pound of carbon and silicon it took away a pound of pure iron, but the slag took away at least a small portion of the impurities from the metal, especially if lime were used in the process. One of the essential differences between the two metals was this (and it was well known in practice at those works where the open-hearth furnace was carried on), that if they wanted a certain ductility, they must put TVth per cent, more carbon into the open-hearth metal than they would require in the Bessemer metal. That was common practice. It was alluded to in Mr. Akerman's paper, but with a doubt thrown upon it. He could inform them that it was a positive fact, and it was a signifi- cant fact also ; because if for the attainment of a certain degree of ductility they could put in TVth per cent, more carbon, it meant that they had the extra strength due to the -j^th per cent, of carbon in their metal, and for that reason he believed that the open -hearth metal would have its own special application, in which it would take the first position, whereas the Bessemer metal was very excellent indeed for perhaps the majority of purposes. He thought it was but right that he should call attention to this difference without wishing in any way to detract from the value of the paper. Mr. Barnaby, the Chief Constructor of the British Xavy, was, he believed, in the room, and as he was a very large user of steel and iron, they would be glad to hear his views. In closing the Discussion, The PRESIDENT said he only wished to refer to two points in the discussion. One was an observation by Mr. Kitson, to the effect that steel did not stand heating and cooling as well as iron. Now, he had received from Messrs. Easton and Anderson, only the previous day, a statement of some very interesting experiments which they had made with steel boilers. The cylindrical bodies were heated to redness, then plunged into cold water, and again reheated and flanged. In other experiments they were flanged -S7A' WILLIAM .s'/AM/A'A'.S1, F.R.S. 377 while in a state of redness, and then plunged into water. With- out going into the details of those experiments he would, with the jxTiuission of the Meeting, hand them to the Secretary, in order that they might appear in their "Transactions." He had the misfortune, though he very highly esteemed Mr. Bell, and put store upon his views, of often differing from him, but in this instance he believed Mr. Bell had been perhaps too severe upon him. He certainly took the view that if they wanted to make a high-class steel, such as Mr. Adamson had brought before them, they must exclude, from that material foreign substances, not only phosphorus and sulphur, but also manganese. He knew from his own experimental facts, and from long experience, that they could not produce a very high-class material unless they made it exceed- ingly pure ; and with all deference to Mr. Bell, he thought there was a broad line of difference between carbon and manganese. Carbon, they knew, associated itself with the iron, and for every loth per cent, of carbon they got a definite increase of tensile strength, therefore when they wanted tensile strength they put in carbon, but that was not the case with manganese. They did not put l£ per cent, of manganese into their rails in order that they might resist the action of corrosion better, or in order that they might stand the test better to which they were subjected, but it was well known that they used that amount of manganese in order that the stuff might roll better, and, as regards rails, he had not much to say against it ; on the contrary, he looked upon the steel which had latterly been brought forward so much by the Terre- Noire Company as a feather in the cap of the open-hearth process, and therefore he had no reason to find fault with it ; but he saw great danger in the indiscriminate use of manganese for the pro- duction of the higher classes of steel. When they heard such extraordinary results as Mr. Kitson had alluded to, when they heard from an authority like M. Fremy such results announced to them as that, under certain circumstances, steel utterly failed, he believed that if the case were to be examined chemically it would be found that the steel was, as it were, forced into a condition of mechanical aptitude for its purpose by the addition of silicon, which was another of those substances which, he thought, under the circumstances, ought to be strictly excluded from high-class steel. Mr. Adamson had called iron a " concrete " of " slag " and 378 THE SCIENTIFIC PAPERS OF " iron." He (the President) thought the same appellation applied to a material containing If per cent, of manganese, besides an ample allowance of phosphorus and sulphur, and, however perfect the material might be for such a purpose as rail-making, he was quite certain it would not stand the higher tests required of a material such as Mr. Adamson had brought before them, and when they wanted to melt it and heat it rapidly and cool it to stand the tests alluded to by Mr. Kitson, or when they wanted to expose it for a length of time to corrosive action, they would find out the difference. ON THE PRODUCTION OF STEEL, AND ITS APPLI- CATION TO MILITARY PURPOSES. BY C. W. SIEMENS, Esq.,* D.C.L., LL.D., F.R.S., &c. THE Chairman, Lieut.-General Sir Henry Lefroy, K.C.M.G., R.A., F.R.S., said, It is scarcely necessary for me to remind you that you have before you one of the most distinguished physical philosophers of the present day. "We have to do to-night, not with the distinguished electrician, with the constructor of the Faraday, with the inventor of the bathometer, with the fertile in- ventor whose range has gone over subjects as various as the setting of type, and the measure of the depth of the ocean, but with one of the most scientific metallurgists of England, the inventor of many remarkable processes in that art, and particularly of one \vhich I daresay he will allude to for the direct extraction of steel and iron from the ore, and of whom it may be very safely said that he has touched no subject which he has not adorned. Dr. Siemens. The subject-matter regarding which I propose to engage your attention this evening is not new. Steel was known to the ancients, and is still produced by semi-barbarians in a similar manner to what we find described in ancient records. * Excerpt Journal of the Royal United Service Institution, Vol. XXIII., 1879, pp. 536-553. .svA- WILLIAM >•//•;.!//•:. v.v, I-.R.S. 379 Rich ferruginous ores were placed upon ignited charcoal in a cavity formed in the side of a hill, and as the result of a day's hard labour in activating goat-skin bellows, a lump of metal mixed with charcoal and slag was produced, which after being subse- quently forged, would prove sometimes of a comparatively soft nature, when it was called iron, and at other times harder, when it was denominated steel. This shows that the two metals iron and steel are substantially the same, and that they are distinguishable only by difference of physical qualities which are the result of very small chemical admixtures. The steel produced by the ancients was of very high quality, remarkable for its great hardness, and for its, power to resist abrasion. Who has not heard of the blades of Damascus, and at a somewhat later period of those of Toledo, and of the remarkable swords that were made by the Norsemen ? So much value indeed did the Norsemen place upon the production of cutting edges of great hardness coupled with tenacity to resist chipping, that those who could produce a blade of unequalled edge were highly esteemed and in one or two instances even rewarded with the purple of royalty in being elected sea-kings. Notwithstanding the antiquity of the metal called steel, its pro- duction and its application have taken a new and very remarkable stride within our recollection. It was, however, as early as the year 1722, that Reaumur, the distinguished French philosopher, proposed to produce steel on a large scale by fusing cast or pig metal with wrought metal or scrap. He put these ingredients into a crucible, and melting them together produced a metal partaking of the nature of steel. The difficulty he encountered, however, was insufficiency of heat. As far as we can make out, Reaumur's suggestion amounted to little more than a proposal, and it was not until 1820 that steel melting was introduced into commerce in a successful manner by Huntsman of Sheffield, using coke in a furnace actuated by intense draught, such as we know at present as an air furnace. Huntsman succeeded in melting steel in con- siderable quantity in pots, and from that date steel has become of great value in commerce for various applications. Steel has variable properties depending upon very slight differences in chemical composition. Thus one steel when hardened will be next to diamond in its power to resist abrasion, and in its 380 THE SCIENTIFIC PAPERS OF suitability to cut other metals, or when drawn out it will show a permanent elasticity not equalled by any other substance ; it is susceptible of retaining magnetism, and will become what is called a permanent magnet, which property is shared with it to an inferior degree by only two other metals — nickel and cobalt. It is now produced in another condition known as mild steel, in which it manifests a quality of a totally different kind, a ductility not equal only but superior to that of copper and silver. I hold in my hand a vase that has been wrought from a bar of this mild steel by an ordinary blacksmith, or I should rather say by an extraordinary blacksmith, because upon examination the workmanship displayed in the production of this vase is found to be really astonishing. The vase is hollow throughout, and not more than J^ of an inch in thickness and perfectly sound, without weld or soldering. For this work of art I am indebted to my esteemed friend Mr. Henri Schneider, of the celebrated Creusot works in France, who has forwarded it to me as a sample of what he had produced by the open hearth process of steel making, of which process I shall have occasion to speak further on. It was not, however, until the year 1856, that a means was pro- posed of producing steel at a cheap rate. This was the year when Mr. Henry Bessemer read his famous paper at the meeting of the British Association at Cheltenham. His paper was entitled " The manufacture of malleable iron and steel without fuel," and it naturally created the greatest possible interest throughout the country. Mr. Bessemer, however, did not immediately succeed in producing by his process such steel as could be used. It was not until the year 1862, the time of the Universal Exhibition in Lon- don, that Bessemer steel attained a decided position in commerce. But, in speaking of this very important process, I feel in justice bound to make reference to the name of Mushet, who, when he heard of the Bessemer process, thought that it would require an addition — analogous to what Heath made in the Sheffield pot- melting process — that of manganese. Mushet proposed and patented a mode of adding spiegeleisen (or pig metal containing a considerable percentage of manganese) to the Bessemer metal whilst it is still in the liquid state, thereby separating from it the oxygen held in suspension in the metal in consequence of the blowing, and as we now know, adding to it some manganese which 5/A' U'l I.I.I AM SII'.MKNS, F.R S. 381 is essential in order to make the metal thoroughly malleable. We h:i\< here then a process that has done more than any other in- vent inn in modern times to revolutionize, I may say, the most important industries of the land. At present not only railway machinery, but the very rails upon which we travel, are made not of iron, but of steel, and if I say that steel rails have shown a power of endurance five or six times greater than those of iron, I may add, with some regret (and I now speak not as a consumer, but as one connected with the production of steel as a manufacture) that they are unfortunately produced at a price almost cheaper than iron or any other metal that could be named. Perhaps, however, the manufacturer will learn to produce them at those prices and yet clear some profit. Almost at the same time that Mr. Bessemer made his remarkable invention experiments were instituted, at a distance of not 100 yards from this place, which have led to another process of pro- ducing steel upon a large scale. I, in conjunction with my brother, Frederick Siemens (who had previously been my pupil), erected an experimental furnace at Scotland Yard, by which we proposed to attain very high degrees of heat, and it was almost from the first that I looked upon that furnace as capable of accomplishing what Reaumur, and after him, Heath, had proposed to do, namely to produce steel in large quantities upon the open hearth. At first our attention was confined to melting steel in crucibles, to melting glass, and to other applications of this mode of pro- ducing intense heat ; the difficulties encountered were very great, and it was not until the year 1861 or 1862 that the prejudices in the way of the practical application of the furnace were sufficiently overcome, and that the furnace itself had assumed such a shape as to enable us to show that it could be applied with commercial advantage. And it is a curious coincidence that it took us just as long to mature this furnace as it took Mr. Bessemer to mature his process. In the year 1861, a large furnace was erected at the glass works of Messrs. Lloyd and Summerfield, near Birmingham, which has been at work up to the present time, and has realized those results that we, up to that time, had only hoped to attain. The success then achieved encouraged me to commence a series of experiments in the direction of producing steel on the open hearth, but, in order not to weary you, I will proceed to describe the 382 THE SCIENTIFIC PAPERS OF regenerative gas furnace in the form in which it is now applied for the production of steel on the hearth, in quantities of from 5 to 10 tons at a time. The regenerative gas furnace is so essential a part of the process of open hearth steel-making that it is indispensable to describe its principle and construction to some extent. It consists of two distinct parts — the furnace proper, with its reversing valves, regenerators, and melting chamber, and the gas-producer, in which the raw fuel (mostly small coal) is converted into gaseous fuel, which is thus separated from all the drossy and dirty constituents in the coal. It would appear, at first sight, a roundabout opera- tion to convert fuel from the solid into the gaseous condition and then to take and burn this gas in a furnace elsewhere ; the gas, as it passes from the producer, is in a heated state, and in its transit to the furnace a great deal of that heat must necessarily be lost ; therefore, it might well be asked, why make this conversion of solid into gaseous fuel ? Surely, in burning the gas less heat is obtained than if the fuel were burnt in the heating chamber of the furnace, and produced its effect there. That would be per- fectly sound argument, if it was not for the regenerators of the furnace. These regenerators are by far the most important part of the whole arrangement, and, in order to understand the general principle of the furnace. I will first describe their action. Plate 46, represents the furnace in longitudinal section ; the gas from the gas-producer passes in through a reversing valve, by means of which it is directed into the bottom part of the re- generator chamber-. The gas flowing up through the mass of brickwork the chamber contains, and which is placed so as to form a large aggregate surface, with intricate zigzag passages, will become heated, providing any heat has been accumulated therein. In the first place, there will be no heat, and the gas will pass unheated through this chamber and thence to the combustion chamber of the furnace. At the same time, a current of air is admitted through the air-reversing valve into the air regenerator chamber, which is larger than the gas chamber. The air passing up through the chequer work will reach the same point as the gas does at the entrance into the combustion chamber of the furnace. Now, since both the air and gas are cold, and as they meet for the first time at the entrance into the furnace, they will, if there ignited, WILLIAM .sv/-;.i//-;.\'v, r.R.s. 383 a heat not certainly superior to what would be produced it -olid fuel had been burned there instead ; on the contrary, gas of the description we are dealing with is a poorer fuel than solid fir -I. and the heat produced in the furnace will, therefore, be very m 'derate indeed. But the flame, after passing over the bed of the furnace, does not go to the chimney direct, but has to pass through two iTg'-Merative chambers, similar to those already described ; the larger proportion of the heated products of combustion will pass through the air regenerator chamber, simply because it is the largest channel, and another portion will pass through the gas regenerator. The products of combustion pass from these chambers through the reversing valves, and are by them directed into the passage leading to the chimney. The operation, therefore, is simply this, that the air and com- bustible gas pass up into the furnace through the one pair of chambers, and pass away, after combustion, towards the chimney through the other pair. But in passing through the second pair, the heat of the products of combustion is given up to the brick- work. The upper portions of this brickwork take up the first, and, therefore, the highest degree of heat, and, as the burnt gases are passed downwards through the regenerators, they are, by degrees, very completely deprived of their heat, and reach the bottom of the chambers and the chimney comparatively cold. After this action has been going on, say, for an hour, the reversing valves are turned over. They are simple flaps, acting like a four- way cock, and, by throwing over the levers which work them, the direction of the currents is reversed. The gas and air will enter now through the second pair of chambers, and the air passing up one regenerator and the gas passing up the other, will take up heat from the bricks previously heated by the descending current. The gases so heated, say, to 1000° Fahr., will enter into combustion, and if the heat produced at the former operation was 1000°, it ought this time to be 2000°, because the initial point of temperature is 1000° higher. The products of combustion will also escape at 2000°, and passing through the chequer work of the first pair of regenerators, its uppermost ranges will be heated to very nearly 2000°. The temperature will diminish by degrees in descending till the gaseous currents have again reached the bottom nearly cold. Again reversing the process, after another hour or half-hour, 384 THE SCIENTIFIC PAPERS OF as the case may be, the gas will take up the heat to the extent of nearly 2000°, and since another 1000° is again produced in com- bustion, the temperature of the furnace will this time attain 3000°, and in this way it might be argued that, unless work is done in the furnace, the heat developed in combustion will, step by step, increase the temperature of the furnace 1000°, or something less, each time the reversal of the valves takes place, till we arrive at the practical limit imposed by the melting point of the most refractory substance we can find (pure silica, in the form of Dinas brick), of which the melting chamber is usually formed. This high temperature is obtained by a gradual process of accumulation, and without any such current as would be likely to destroy, by oxidation, the metal in the bath, or cut away the sides and roof of the melting chamber. There is, however, a theoretical as well as a practical limit to the degree of heat obtainable in combustion, which was first pointed out by M. H. St. Claire Deville, namely, the point of dissociation at which carbonic acid would be converted back into its constituents, carbon and oxygen. If carbonic oxide or any other combustible gas and air enter the furnace at a temperature very nearly equal to the point of dissociation, it is evident that association or combustion cannot take place, and thus nature fortunately steps in to restrict the increase of heat by accumula- tion, within comparatively safe limits. In a furnace fully heated up to the melting point of iron, this action of dissociation can be very clearly observed. At first, when the gas and air are com- paratively cold, combustion takes place sluggishly, the gases will flow through the furnace and produce only a dark-red flame ; the next time the valves are reversed a whitish flame is produced ; the next time a short white flame ; and after having reached a full white heat, exceeding the welding point of iron, the flame will again become a long one, but this time not red, and of little apparent power, but bluish white, and flowing in clouds. This indicates the near attainment of the point of dissociation ; com- bustion can no longer take place, except in the measure of the heat being dispersed to surrounding objects, or to the metal in the furnace, and that is about the degree of heat required for the process of making steel on the open hearth. Before I leave the question of the furnace, I must refer back to S/X WILLIAM SIEMENS, F.R.S. 385 t'l-- apparatus in which the solid is converted into gaseous fuel. This is a very simple apparatus, consisting of a cubical brick chamber of about 8 feet side, one side of which is cut off in a slanting direction. Fuel descends on this inclined plane, to the grate at the bottom where combustion takes place. The result of this combustion is carbonic acid at a high degree of temperature, ami if this product of combustion was allowed to pass up the gas- collecting channel, and through the overhead tube to the furnace, there would be nothing to burn ; and the only result we should probably observe would be that the iron tube would very soon become red hot, and be melted down. But the carbonic acid as it is formed near the grate, encounters a further layer of fuel descending from above, which is also incandescent, but which cannot be consumed on the same terms, because there is no longer any free oxygen present The first result of combustion being carbonic acid, a compound of one atom of carbon and two of oxygen, this carbonic acid in passing through the subsequent layers of incandescent fuel is broken up, and a second molecule of carbon is added to the first, thereby producing carbonic oxide, which is a combustible gas. But coal is not simply carbon, it consists also of volatile matters, hydro-carbons, water, and the constituents of ammonia, and the hot carbonic oxide in passing through a further thickness of the fuel which contains these gaseous constituents, acts upon them in the same manner as heat does upon the coal in a gas retort. This action absorbs a portion of the free heat in the carbonic oxide, and the result is a gas consisting of carbonic oxide, hydrogen, hydro- carbons, aqueous vapours, and nitrogen, which latter, being a constituent of atmo- spheric air, necessarily passes with it through the fuel, and dilutes the combustible gas produced to the extent of about 50 per cent, of the total volume. This combined gas leaves the producer not at 3,000°, the temperature of direct combustion, but at about 700° F. only. This remaining heat is thrown away and purposely so, and many criticisms have been made in consequence of this apparent waste of heat in the regenerative gas furnace, but I think I can prove that although there is loss of heat, no waste is incurred. The gases passing from the gas-producer could be forced to the furnace by mechanical means, but this would be very troublesome VOL. i. c c 386 THE SCIENTIFIC PAPERS OP and costly, and the duty performed by the 700° of heat is to give them onward motion in the direction of the furnace. The hot gases rising in the uptake represent a column of heated gas at a temperature of 700°, at which its density will be about half the density at ordinary temperature. From the uptake they pass through a long tube of sheet iron or steel, and on their journey through this horizontal tube they part with most of their heat, so that when they reach the downtake their temperature has probably fallen from 700° to 200°, having parted with 500° of heat by radiation from the tube. The consequence is that the descending column will be of about twice the specific weight of the ascending column, and therefore a continual flow of the gas will take place, ascending on the one side, and descending on the other in forcing its way towards the gas furnace ; by this means the heat apparently lost in the gas is utilized to produce useful mechanical effect. But suppose that the gas passed from the producer to the furnace without being allowed to cool, what would be the result ? The gas would enter the regenerative chamber at a temperature not of 200° but of 700° ; it would, in ascending, take up more heat and enter the heating chamber at the temperature previously imparted to the upper ranges of the chequer work by the descending current or product of combustion. The same tem- perature would be attained by the gas if it entered at 200*, the only difference being that the regenerator in the case of the cooled gas would work through a greater range of temperature by 500". But a regenerator will work with the same economy through a greater range as through a less range ; therefore, this heat, if it could be saved, would be of no benefit whatever to the gas furnace. The only difference in result would be that the gases would get less cooled in descending on their way towards the chimney, and that we should have a hot chimney instead of a comparatively cool one. Therefore, no loss to the furnace is in- curred in cooling the gas on its way to the regenerative chambers, and the temperature of the gas is utilized to produce the very essential mechanical effect of urging the gas from the producer to the furnace. The economical action of the furnace depends upon the circum- stance that the products of combustion reach the chimney, not at S/K WILLIAtf SIEMENS, F.A\S. 387 :"mperature of the heating chamber, as is the case when ordinary f urnaces are employ t-0° F., thus rendering nearly all the heat produced in actual combustion available for accomplishing useful work. It will I) • readily perceived that the economy of this system must be greatest in melting steel or in accomplishing operations of melting or heating at very high temperatures, whereas for the attainment of low temperatures, such as the heating of boilers, the economy would be comparatively small. Its practical economical result for ligh temperatures is well illustrated by the fact that in melting steel in pots in the ordinary air furnace at Sheffield, 3 tons of Din-ham coke are required to melt a ton of steel, whereas a ton of small coal suffices to melt a ton of steel in the same pots when the regenerative gas furnace is employed. In melting steel in bulk upon the open hearth, the consumption of fuel is further reduced, and does not exceed 12 cwt. of coal for the production of a ton of steel. In re-heating iron, the practical economy effected in the regenerative gas furnace over the ordinary furnace amounts to from 40 to 50 per cent., owing to the inferior degree of tempera- ture required. When applying the system to inferior tempera- tures, there is advantage in suppressing the cooling tube and gas regenerator, and in approaching the gas-producers to the furnace, to consume the gas at its initial temperature. At large works such as are now erected for carrying out the open-hearth steel process, a cluster of producers are put up outside the works ; and the fuel is delivered from the railway at an elevated point in order to be put into the producers in which it is gradually consumed, and flows as a gas through the large overhead tubes into the works, where a number of furnaces are supplied for the production of steel. I think these observations may suffice to describe the furnace which plays a most important part in the process to which I shall presently refer. I have already stated that one of the chief objects I had in view in maturing this furnace was the production of steel on the open hearth, but, as usual, in introducing a new process, great difficulty was encountered in first attempting to carry that idea. The question arose whether steel could be melted and maintained as steel upon the open hearth of a furnace at a temperature exceeding the melting point of most fire-bricks. The general opinion of c c 2 388 THE SCIENTIFIC PAPERS OF practical men was entirely opposed to the idea of accomplishing the object, and it is, therefore, perhaps natural that its realization was a question of time. The first attempt to make steel on the open hearth of a regenerative furnace was made by Mr. Charles Atwood, of Tow Law, who, in 1862, agreed to erect such a furnace — a small one, it is true — to my design ; but although he was partially successful, he abandoned the attempt because he was afraid that the steel so produced would not be of the proper quality. In the following year, another attempt was made in France. A large furnace was erected at the Monthi£on Works, and my colleague in the experiment was a very celebrated French metallurgist, the late M. le Chatellier, Inspecteur-General des Mines. The experimental results were on the whole satisfactory. We obtained some charges of metal that was decidedly steel, but unfortunately, the roof of the furnace soon melted down, and the company who had undertaken the erection of this furnace were so much disheartened, that they, for the time at least, abandoned the idea of following up the trials. After two or three very similar disappointments, I decided to erect experimental works at Bir- mingham, where the processes of producing steel on the open hearth have been gradually matured, until they were sufficiently advanced to entrust them into the hands of others. But another French manufacturer, MM. Martin of Sereuil, undertook to erect a regenerative gas furnace that could be used for making steel on the open hearth, but which, in the first place, was to be used as a furnace for heating wrought iron. While I was engaged at Birmingham with experiments to produce steel of good quality by my process, MM. Martin also succeeded in obtaining results with the furnace I had designed for them. At the time of the French Exhibition, in 18G7, MM. Martin brought forward their excel- lent exhibits, for which they soon got a considerable name. I also sent samples of steel produced by me at Birmingham, differ- ing from those sent by MM. Martin, as regards the material used in the process ; they had turned their attention to the production of steel by dissolving wrought-iron in a bath of cast iron, whereas my efforts were directed, from the first, to the use of cast iron and ore for the production of open-hearth steel. In the process as it is now carried on at the Landore and other works, both scrap metal and ore are employed, in conjunction S/ff WILLIAM SIEMENS, F.R.S. 389 with pig metal and such other ingredients as serve finally to adjust the quality of the steel. The process may be described as follows : — The furnace having been heated up to the steel-melting point, or say, 3,500° F., the first duty of the steel-melter is to see that the silica bottom and tapping hole are in the proper condition for work. If, in consequence of wear caused by previous charges, the surface-bed should be pitted, white sand, previously calcined, is introduced in such quantities as to fill up the inequalities, and heat is allowed to act for eight or ten minutes with the furnace doors closed, by the end of which time the silica or white sand introduced will be partially melted and consolidated with the older portion of the furnace-bed. The tapping hole is filled up with white sand mixed with powdered anthracite or coke, which serves to prevent its entire consolidation, and thus facilitates the tapping of the furnace at the end of the operation. These preliminary operations completed, the furnace is charged with say six tons of pig metal, mixed with two tons of such iron or steel scrap, as gits, spillings of previous operations, old iron or steel rails, that may be available. The furnace doors are there- upon closed, and heat is allowed to act upon the charge for two hours and a half, when it will be found to have fused, and analysis would prove the metal to be an intermediate condition between pig iron and steel, its percentage of both carbon and silicon being greatly reduced. The subsequent work of oxidation of these ingredients consists in the introduction, at intervals of about half-an-hour, of rich ores or oxides of iron, in charges of about 5 cwt. each ; the immediate effect of the introduction of each charge is an active ebullition, through the reaction of the oxide of the ore upon the carbon of the metal, producing carbonic oxide. This gas escapes to the surface, whereas the iron contained in the ore or oxide becomes metallic, and is added to the bath. "When about 25 cwt. of ore have been thus added, a sample is taken from the bath, by means of a small iron ladle, and subjected to a simple mechanical test, whereby the percentage of carbon remaining in the metal is readily, though somewhat roughly, ascertained. If it appears from the test that the carburization is nearly completed, no more ore is added, but 3 or 4 cwt. of limestone are thrown into the lurnace, which has the effect of combining with the silicon con- tained in the slag, and of liberating ferrous oxide from the same, 390 THE SCIENTIFIC PAPERS OF which latter, being thus set free from its combination with silicon, continues the action of decarburization of the metallic bath. Samples are again taken, until the steel-melter finds that, upon breaking the sample, the peculiar silky fibre is obtained which is indicative of a reduction of the carbon in the metal to O'l per cent. The metal is now ready for final adjustment, according to the strength or temper of the steel required. If it is intended to produce ordinary rail metal, from 7 to 8 cwt. of spiegeleisen, containing 20 per cent, of manganese, previously heated to redness, are charged in, the bath is stirred by means of a rabble, and, after being allowed to rest for a few minutes, is tapped either into a ladle or directly into ingot moulds, arranged in groups, whilst the slag that followed the metal through the tap- hole is collected in a pit or mould prepared for its reception. The amount of slag produced depends chiefly upon the percentage of silicon in the pig metal used, and also upon the degree of purity of the ore employed in effecting the reduction, and amounts gene- rally to 2 tons in an 8-ton charge. The yield of metal should be within 1 or 2 per cent, of the total amount of pig metal and scrap (if of a solid description) charged into the furnace, because, although the pig metal would contain some 7 or 8 per cent, of carbon and silicon, which have to be expelled, this loss of weight is made up by the metallic iron given up by the ore. The lime added near the end of the operation is useful in taking up some of the other impurities, such as sulphur and phosphorus, from the metal, although the amount so taken up is only small. After tapping, the steel-melter again inspects his furnace-bed, repairing any slight defects that may have arisen, fills up the tapping-hole, and introduces the next charge. The time each charge occupies is from seven to nine hours, according to its character and to the heat of the furnace. When pig metal and scrap alone are used, a charge can be worked in from six to seven hours, and the proportion of pig metal employed can be reduced to from 10 to 15 per cent, of the total charge, whereas when no scrap at all is used, the amount of pig metal charged must be equal to the total amount of steel to be produced, and the reaction between the ore and pig metal extends the time of each operation by about three hours. In this respect, then, the scrap or Siemens-Martin process has an advantage over the ore SIR WILLIAM SIEMENS, F.R.S. 391 process, which is compensated for, however, by the correspond! ug advantage in favour of the ore process, that it is not dependent up' in the irregularities appertaining to scrap metal, and upon the purifying action produced upon the fluid metal first by the oxide and thereafter by the lime. It has been found generally that for small applications the scrap or Siemens-Martin process is the more advantageous, while for large applications the ore process has the advantage. For the production of steel of special quality, such as is em- ployed for boiler and ship plates and castings, the process is different only towards the eud of the operation from that already described. The reduction is carried to a still lower degree than O'l per cent, of carbon, and in order to make sure that the right degree of carburization is attained, chemical analysis of a sample is resorted to. Instead of spiegeleisen, a rich ferro-inanganese is employed, together with a small proportion of silica iron (a pig metal containing about 10 per cent, of silicon), which latter metal has the effect of taking up oxygen from the fluid iron, and thus preventing blow-holes in the casting. Another method of con- solidating steel is that which has been introduced and so success- fully carried out by Sir Joseph Whitworth. The steel upon which he operates is made upon the open hearth of the furnace in the manner I have described ; but steel when it is poured from the ladle into the moulds shrinks, and during shrinkage little air- spaces or hollows are formed, which break the continuity of the steel, although the cavity may afterwards be closed. Sir Joseph Whitworth, by applying great pressure through hydraulic agency to the steel while in the fused condition, closes up these cavities, and steel is thus produced perfectly continuous in its nature, and of such great hardness and tenacity combined, that when put, for instance, into the form of shells, some of these shells have gone three or four times through thick iron armour, and have been quite fit to go into the gun again. The rich ferro-manganese now introduced into the market affords the steel-maker great facility for producing sound metal, notwithstanding its admixture with a considerable amount of impurities, notably of sulphur and phosphorus. By its means such inferior irons as the Cleveland can be rendered suitable for the production of steel rails, and large contracts have been carried 392 THE SCIENTIFIC PAPERS OF into effect by some of my licensees for converting old iron rails of mixed or doubtful parentage into steel rails. The facility thus offered to steel manufacturers introduces, however, a danger upon which the steel user will have to fix his attention. A steel rail containing from 1 to 1| per cent, of manganese may look well and resist the tests for toughness and strength which are usually applied, and may yet contain more than \ per cent, of phosphorus or sulphur, or both these sub- stances. It is only at temperatures below the freezing-point that the presence of phosphorus will make itself felt by symptoms of cold shortness, and it would therefore certainly not be advisable to put down rails of this description in cold climates. For the construction of ordnance and other high class purposes, more than a trace of manganese in the metal is, in my opinion, decidedly objectionable. Manganese, though very efficacious in hiding impurities in the steel, is in itself an impurity inconsistent with high quality of the material produced. Its admixture with the metal is purely mechanical, and upon analysis of different portions of the same ingot it is found that its distribution is very irregular. Being more oxidizable than iron, a metal containing a considerable percentage of manganese cannot be re-heated without deterioration ; is pitted by exposure to sea-water ; and its strength and toughness are also found to be below those of really pure metal when subjected to crucial tests. It is important, therefore, that steel for war purposes where high temper and great tensile strength is required, should be practically free from manganese, as well as from all other admixtures, with the sole exception of carbon. Extra mild steel, which is so remarkable for its extreme ductility, should contain in 100 parts 99*75 parts of metallic iron, and only 0'25 per cent, of all foreign substances put together. It is for the production of these special qualities of steel that the open^hearth process has come into extensive use, being employed, either wholly or partially, by many of the leading works both in this country and abroad. The total production of open- hearth steel (both the Siemens-Martin and Siemens variety) amounted in 1877 to 275,000 tons, since which time its produc- tion has gone on increasing, notwithstanding the extreme depres- sion which continues to prevail in the iron and steel trades. The French Admiralty were the first to take up the subject of WILLIAM SIEMENS, F.R.S. 393 constructing ships of very mild steel, and the British Admiralty n«'\v use it largely in naval construction, with such results as I k'lu-vc will shortly be placed before another Institution by their chit f constructor, Mr. Barnaby. Although I have described the open-hearth process, as dealing with pig metal and ore — or, when it can be had, pig and scrap metal — my attention has been directed for many years to the accomplishment of a process, in which the ore used is put through a preparatory pro- cess of reduction and precipitation, and only a minimum quantity of pig metal is employed to impart fluidity to the mass in the melting- furnace. In my early experiments in this direction I followed the lead of Chenot and others in producing what is called spongy iron, or iron deprived of its oxygen by heating it to redness, in com- Mi.ation with carbonaceous material. I soon convinced myself, however, that no practical results could be obtained by this means, inasmuch as the spongy iron contains, bound up with it, the gangue of the ore, which can with difficulty be separated from the metal, and afterwards encumbers the melting-furnace with excessive slag. All the hurtful impurities contained in the ore, such as sulphur, phosphorus, arsenic, &c., remain, moreover, in the spongy iron ; and, as regards sulphur, its quantity is much increased on account of a powerful absorbing action, exercised by the spongy iron upon the sulphurous acid contained in the flame of the furnace. It was necessary, therefore, to devise some plan by which the metallic iron could be simultaneously separated both from the ore and its impurities. This object I have succeeded in accomplishing by means of a rotating furnace, which has, however, hitherto received only a limited application. The furnace, which is represented in Plate 47, consists of a gas-producer, the air-regenerator, a reversing- valve, and the revolving drum. No gas regenerators are employed in this furnace, but the gas passes from the pro- ducers through an oblong channel continuously into the revolving chamber, where it is brought into contact with the heated current of air passing in from one or the other of the air regenerators. The flame thus produced rushes forward into the heating chamber, and after heating the material therein, passes back again towards the inlet side, whence the products of combustion pass through the second air regenerator and the reversing valve into the chimney stack. By this arrangement the front of the rotatory furnace is 394 THE SCIENTIFIC PAPERS OF left free for access, and is provided with a charging and discharging door placed eccentrically, for the convenience of withdrawing masses or balls of iron from the furnace on a level with the lining when the furnace is stopped with the aperture in its lowest position. The lining of the furnace is made of highly aluminous or bauxite bricks covered on the inside with a certain thickness of iron oxide produced by melting hammer scale and rich ores in the furnace, which set while the furnace is kept slowly rotating. The rotation of the furnace is effected by means of a small Brother- hood or other engine, and suitable gearing. The modus operandi is as follows : — The furnace being already lined and heated, a batch of ore mixed with fluxing and reducing materials, in a proportion depending upon the chemical con- stitution of the ore employed, is charged from an elevated platform in front, the rotator being stopped for this purpose with the charging orifice in its upper position. From :30 to 40 cwt. of batch is thus charged, upon which the door is closed, and the furnace chamber is made to rotate at the very slow rate of six or eight revolutions per hour. A high temperature is produced within the chamber by the combination of the gas with the highly heated air from the generator, causing the mass rapidly to become hot, whilst slowly rotating, so as to present continually new surfaces to the heat. No chemical action takes place under these circumstances until the temperature of the mass is raised to a full red heat, when reaction between the carbonaceous matter and the ore will take place, giving rise to the development of carbonic oxide, which, meeting the heated air proceeding from the re- generators, is burned, and thus adds to the heating action of the flame. When this reaction has fully set in, the supply of producer gas may be almost entirely stopped, and thus no sulphurous gas is admitted into the furnace during this critical interval. The heat now rises rapidly, and fusion of the earthy constituents of the ore occurs simultaneously with a continuance of the reducing action. In the course of an hour and a half after starting, the charge consists of metallic iron in a more or less agglomerated condition, found on analysis to be almost chemically pure, and of a liquid mass of cinder containing the earthy constituents of the ore and other foreign matter. The rotation of the furnace is now stopped with the tapping-hole in its lowest position, and the bulk of WILLIAM SIEMENS, F.R.S. 395 tlir finder is discharged ; the tapping-hole is thereupon closed again, and the furnace made to rotate somewhat more rapidly with a \ ifw of facilitating the agglomeration of the metallic iron ; by tin- timely introduction of a rabble, the agglomeration of the mass can be so regulated as to induce the formation of two or three balls of convenient size for handling. The balls being formed, the furnace is stopped with the large door in its lowest* position, which, upon being removed, admits of the charge being withdrawn. This is effected by the introduction of tongs supported by pulleys running upon overhead rails for transferring the balls in rapid succession from the furnace to a squeezer (which has for its purpose to expel adhering cinder), and from the squeezer to the bath of such a steel melting-furnace as already described. The great purity of the metal thus reduced from the ore, and the rapid and comparatively inexpensive nature of the reducing process, are conditions highly favourable to the production of steel of high quality by this method at reasonable cost ; and it is my intention gradually to complete the open-hearth process of pro- ducing steel by combining with it the mode of preparing the material to be melted just described. What I also wish on this occasion to call attention to are certain properties of steel which are of importance in considering its applicability to engineering and military construction. We know that steel varies between very large limits in its hardness and in its ductility, but it is not so generally known that steel up to a certain point is of the same strength to resist strain when it is mild as when it is hard, and I have prepared a table of results which shows very clearly the nature of both mild steel and hard steel if compared under different strains. Upon reference to the table it will be seen that loads from G to 15 tons per square inch affected all the bars equally, whether hard or soft, annealed or unannealed, and with the exception of one bar only this uniformity holds good up to 18 tons ; up to this limit, the elastic elongation of all the samples was equal ; but with the strain of 18| tons, the mild steel has become permanently elongated, whereas the harder steel shows a normal increase of elastic elonga- tion. With the hard bars experiments were continued, and 21 tons to the square inch was applied, producing an elastic elonga- tion '108, which is entirely normal, and no permanent set is pro- 396 THE SCIENTIFIC PAPERS OF P !.' ^ § S K) fe ^ O CC(MOC(NCO 1J IO tO O IO 15 «ff (M CO