T T T "» IT -K T T i -r- CHIMNEYS — FOR — FURNACES, FIRE-PEACES, — AND — STEAM BOILERS. By R. ARMSTRONG, C. E. f SECOND AMERICAN EX5ITI03ST. TO WHICH 18 APPENDED AN ESSAY ON HIGH CHIMNEYS. ,. By, Prof. - L. PI^ZGER,- , \ Qf L'EafU Poipt-chnique at AiX-la>Chc~ppelh. 23 Murray and '27 Warren Street. 1883. CHIMNEYS FOR FURNACES FIRE-PLACES, AND STEAM BOILERS. PRACTICAL THERMODYNAMIC S. Fornaces, or closed fire-places, which it is the main design of this essay to treat upon, arff^essentiaHy.different in .principle and. cons'tim^tiCtfi !to* the. o'sthjaaiy :o}}eA fire-places of dwelling-houses, as they are exceedmgly^iffereirt, ih'.the jgeji.eraj. scope and object, «an=9.88 , New Const. =1 15 Answer 51 H. P. Example 3.— Another new chimney erected the same year, in the same works (Thomas Hoyle & Sons), was 3| ft. diam- eter by 40 yards high. Required the horse power it is equal to. 5S SOLUTION. Diam. 3^ ft. I 2 = m\ Const, number 1* Vht. (120) =11 I Horse power 90 The chimney in this example (3) was erected in November of the same year? and by the same builder as that in Ex- ample 2. It was built with similar ma- terials in the same manner like the pre- ceding 1 chimney. The shaft was octagonal, but higher in proportion to its area than the former, for the purpose of carrying away the smoke from contact with some adjacent buildings, and the cost was about double that of the experimental chimney. By which it will be seen that we had arrived at a fair average cost of chimney. building in proportion to the power capable of being produced in that way, so far as chimneys of this character, and from 30 to 40 yards high, are con- cerned—namely, about £2 per horse power. The very many practical tests of vari- ous kinds that were applied to these two chimneys, during several successive years, such as finding that the second chimney 59 was equally applicable to two as the first or experimental chimney was to one boil- er of similar size, not much over or under 45 or 50 horse power each, convinced us that we had approximated near to the data we were in quest of. The Duckinfield Bleach Works, Chim- ney and Furnaces. — The subject of our next example in chimney building serves still further to corroborate our Mayfield experiments in all respects except as to cost, which of course greatly diminished as the scale of our operations became larger. This chimney was erected early in the spring of the year following the comple- tion of those last named, at Messrs. Hoyle & Sons' New Bleach W orks, then erecting at Sandy Lane, between Duckin- field and Staleybridge. In the planning of the chimney and flues, and furnishing the designs, with all their details, and four large boilers, for which the writer was more especially en- gaged, and which were expected to furnish from 200 to 300 horse power of steam* CO we had the valuable assistance of Mr. John Graham,* afterwards a member of the firm, and whose eminent talents as a scientific and practical chemist are gener- ally known — as we also previously had the cordial assistance, general concur- rence and approval of the late Mr. Alfred Binyon, the then managing partner. Example 4. — The Duckenfield Bleach Works chimney was made 45 yards high by 6 ft. inside diameter at the top. Re- quired the horse power it is equal to. SOLUTION. A I Diam. 6 ft. | 8 =36 [ New constan t=lj[ 0 | 0it. (135 ft.)=11.6]Horse power^378| Milne's Const. 2 208 * See a valuable paper by this gentleman in vol. xv. of the "Transactions of the Literary and Philosophi- cal Society of Manchester," for the years 1857-8. A portion of it was also republished in the Engineer newspaper for March 12, 1858, which gave an account of a series of evaporating experiments, made for the purpose of testing the economy of fuel and manage- ment effected at these boilers and furnaces through a series of successive years, which will well repay pe- rusal, and will be further adverted to in a subsequent part or appendix to this work. 61 The above slide-rule solution for the power of this chimney gives two answers to the question — namely, 278 and 208 horse power, respectively, according as the new constant 1{, or Milne's old con- stant 2, are used as gauge points. In this case the latter was preferred, as giving the most correct result, by reason of the kind of fuel intended to be con- sumed being of the same or similar in- ferior quality to that already referred to as being in general use within the parish of Oldham, to which these Avorks were nearly adjoining. Facility in obtaining this cheap fuel— known as " burgey " and " slack" — being one of the chief reasons for erecting the works in this particular locality. THE EXPERIMENTAL BOILERS. In the collection of data for steam-en- gine chimneys, it would be a great omis- sion to leave out the particular dimen- sions of the boiler, to cause the efficient working of which is, in fact, the only profitable work the chimney has to do. 62 The boiler, for which the Mayfield ex- perimental chimney was erected, was de- signed by the writer, as was also the chimney, as already stated, specially for experimental purposes, in acquiring all practical information on the subject pre- vious to commencing the construction of Messrs. Hoyle & Sons' new Bleaching and Calico -printing Works at Duckinfield, near Staleybridge. For this purpose I did not hesitate to recommend the plain- est and simplest form of boiler that can be conceived — namely, a plain cylinder, laid hoinz on tally, or nearly so, with the fire to go underneath it at one end, and out to the chimney at the other, which may now be described. This experimental boiler was of the " direct draught " kind, that is, without return flues, and this one had no flues of any kind, either inside or out. The boiler and chimney were, therefore, both of the simplest possible kind, and for that reason made mutual tests of their re- spective capabilities through a long series of very accurate experiments relative to 63 economy of fuel, as well as to the effi- ciency of various methods of smoke pre- vention, or smoke burning, as it was then popularly termed, and other matters of interest to the proprietors. Improve- ments in smoke prevention especially were freely invited from all quarters, and this was the boiler at which very many different plans for the purpose were tried. This kind of boiler was fully described in the author's " Essay on the Boilers of Steam Engines " (1839), and the principal dimensions of this one, as there given, need only be shortly referred to here. It was in shape cylindrical, and fully equal to 30 horse power, being 33£ ft. long by diameter, and " set up," or rather hung, by means of cast-iron brack- ets riveted to the sides, and resting on the side walls of the furnace, so that the whole of the lower half of its convex surface, about 32 square yards, was ex- posed to the direct action of the fire and flame. The fire-grate, placed about 22 in. be- 64 low the bottom of the boiler, was 5^ ft. square, or equal to about 30 sq. ft. in area, and was composed of one length of fire-bars, each If in. thick on the face, with air-spaces of T S T to £ of an inch wide between them. This boiler supplied steam to an old Boulton and Watt condensing engine of 16-horse power, by Messrs. Sherratt, of Salford, loaded so as to require seldom less than 24 cubic feet of water to be evaporated per hour at a pressure of ex- actly 4 lbs. per sq. in. It also supplied steam for heating drying cylinders, for boiling water, and for a great variety of other purposes, amounting at times to nearly as much as the engine required it- self. The least average evaporation for a whole day together was 33, and the greatest 45 cubic feet per hour. The lower amount was, of course, obtained at the most economical rate, namely, at about 6 lbs. of water evaporated for each pound of common coal burned. It was* therefore, considered to be full 30-horse power. A cubic foot of water evaporated 65 per hour, being generally considered am- ply sufficient to supply steam for each horse power (nominal) of a Boulton and Watt or low-pressure engine in good order, however it might be at times over- loaded. Although this evaporation of a cubic foot, or a little over six imperial gallons of water, of 10 lbs. each, is what boiler- makers have universally, and practical en- gineers commonly, agreed to consider nominally a boiler horse power, there is no doubt, however, that the same weight of water, as steam, at a higher pressure can easily be, and is frequently, made to work two or three indicated horse power in a modern steam-engine, accordingly as the latter is arranged to work to a greater or less extent expansively. This boiler was made of Low Moor iron j\ in. thick, except the bottom row of plates, which were f in. and the flat ends t \, by Mr. Fairbairn, of Manchester, who had just previously commenced the boiler-making business, ^and was then a staunch advocate for introducing the long 66 Cornish high-pressure boiler, with its one large internal furnace-flue, and single fur- nace-grate. Instead of that kind of boiler, now much less used, except in Wales and Cornwall, I persisted in advis- ing the simple and elementary form of boiler now described. It was also sus- pended by bracket flanges in the cheap and simple manner above mentioned, in accordance with the universal dogma of its strictly utilitarian owners, which in this, as in all other business matters con- nected with the works, was never lost sight of for a moment, — in order that any alterations or improvements that might be found expedient, either in the construction of the boiler, or erection of the brick- work, might be in the shape of additions merely, and therefore capable of being separately proved, both as to first cost and utility, and also that our experiments might be carried on for a sufficient length of time, without the usual liability to interruption from the necessity of cleaning out of flues or otherwise. 67 The last-mentioned particular in the erection of this boiler was of considerable importance in thus attaining the main ob- ject we had in view, as well as in accom- plishing another object greatly desired by the benevolent proprietors of the works, that of doing away with the de- grading practice of sweeping out the flues by means of men, or rather boys, crawling through them. Trifling as a small matter of this kind may appear to some, it is important to show that, in this instance at least, it was attended by considerable economy Cast-iron lugs or brackets, with broad flanges, were riveted along each side of the boiler, a little above the intended surface level of the water, and these brackets rested on the tops of the two vertical side walls of the furnace and flame-bed. The boiler thus suspended between the two side walls was then ad- justed, not quite horizontally, but slight- ly inclined, with a fall of about 8 in. to- wards the front end, so that a greater 68 proportion of the water was brought im- mediately over the fire-grate. This arrangement of the flame-bed and seating, or side walls, of the boiler, formed a chamber or receptacle, large enough to hold all the flue-dust and dirt that could be found from the use of any kind of coal whatever, for a considerable time. In fact, although the boiler was every day at work, the flame-bed did not require any cleaning out, even at the end of nearly two years, — when, as an opportunity occurred, several cart-loads of flue-dust were removed from under the boiler at one time. The occasion of hav- ing this operation performed, discovered to us a circumstance, which is sometimes the cause of great disappointment to the expectations of parties who, for the first time, have boilers erected on this direct draught plan, which requires an explana- tion in this place. At all direct draught boilers, it is usual to have, and highly necessary that there should be, two or more transverse " check'' or flame-bridges, in addition to the ordi- G9 nary fire bridge, carried up to within 6 or 7 in. of the boiler bottom ; but in this case, there was, in the first instance, only one of these additional bridges, and the man employed to get out the flue-dust had, in order to make an easier passage for himself, removed two or three courses of brick-work from the top of the flame- bridge, and neglected to replace them again. The consequence was, that on the boiler commencing work again, a clear loss of 15 per cent, in fuel was de- tected immediately, besides the overheat- ing of the damper- plate and brickwork of the chimney entrance, which evils were, of course, quickly rectified by re- placing the brickwork. Although no very great nicety is required in adjusting the height of these flame-bridges, and an inch or two higher or lower may not make much difference in the economy of fuel ; but the extent of 8 or 9 in. in depth of the air passage over them, when there is already a depth of the same extent in the throat area over the furnace-bridge, will 70 at any time cause an exorbitant waste of fuel. The fact of an error of this kind, which is very liable to be passed over unnoticed by ordinary bricklayers and boiler-setters, unless very carefully supervised, has been frequently the occasion of much error in experiments on the economy of fuel. It is all the more necessary to mention the above circumstances here, because, since my description of the direct draught method of setting boilers was first pub- lished in 1837-8, I have occasionally had complaints from parties who had been in- duced to adopt the direct plan, but had not succeeded in realizing any moderate measure of economy therefrom, and had, in consequence, too readily, or without sufficient examination, given it up, and returned again to the wheel-draught, narrow flue system, with its little army of chimney-sweeps, boiler-menders, and laborers, and all its other disagreeable and expensive accompaniments of Sunday work, over-work, and night- work. It is, however, but fair to state" that extreme 71 cases of this kind have been mostly con- fined to the South of England and the metropolis, where the extravagant use of flaming Newcastle or Hartley coal, with very much unnecessary stoking of the fires, is still continued. These results have been helped not a little, perhaps, by the prognostications of many of the old school of bricklayers, that the direct draught plan would "send all the heat up the chimney," and who too often tes- tify their sincerity in such a belief by tak- ing special care to build their chimneys and flues very narrow and very crooked. The prejudices of some of the attend- ants of engines in London in favor of much stoking and hard firing, which is literally working hard at wasting coal, are difficult to account for, especially when found among persons not notori- ous for working hard at anything else ; but a residence among them of any one whose business is to save fuel, will very soon convince him of the fact. Hence a more careful attention to the condition of all 72 the bridges under a boiler is a necessity which ought never to be neglected. INSTRUCTIONS TO STOKERS. 1. Engineers and firemen who would keep steam with economy, should do with as little stoking or stirring of the fire as possible, if any. In order to do so, they should see before starting that the fur- nace is properly constructed for the pur- pose, and large enough for the quantity of steam required. The fire-grate should have about 1 sq. ft. of effective fire-bar surface for each nominal horse- power of the engine, or for each cubic foot of water required to be boiled away per hour. The fire-bars may be from \ to f in. thick on the face with I to f in. draught spaces between them, and with joggles to keep them asunder nearly the whole depth of the bar. The boiler should have, at least, 8 or 10 sq. ft. of heating surface per horse, and the chim- ney should be of sufficient capacity to create a draught into the furnace equal to the pressure of a column of water § 73 to | in. deep, when the damper is set wide open. 2. In firing, spread the large and small coals (equally mixed) on all parts of the grate, thicker at the back of the grate near the bridge than at the front, because the draught is there the strongest, and the coals burn away the quickest. 3. The fire should never be less than about 3 or four inches thick in the middle of its length, 2 or 3 in. in front, and 6 or 8 in. at the back of the grate. In no case should the fire exceed double the depth here stated ; and never more than two- thirds of the fire-grate should be entirely covered with fresh coals at one time. 4. If a regularly uniform supply of steam is required and the damper quite up, the quantity of fuel on the grate may be gradually increased ; but when an increasing quantity of steam is wanted, the average thickness or quantity of fuel on the grate must not then be increased, but ought rather to be diminished, and supplied by smaller quantities at a time, 7-1 and more frequently. So soon, however, as the supply of steam e'xceeds the de- mand, the coal must again be supplied by larger quantities at a time, regularly in- creasing the quantity of fuel in the grate as before. On the other hand, when a diminished supply of steam is required* close the damper a little, and take the op- portunity of levelling the fire or cleaning the fire-bars, doing one-half of the grate at a time. 5. A steam-engine furnace worked in this way will make very little smoke ; or, if any, it may be prevented when desir- able by opening the fire-door 2 or 3 in. for 1 or 2 min. after each firing. Bearing in mind that the production of steam is commonly lessened by doing so, but so is the consumption of the fuel. 6. Stokers should understand that they are not to make a business of " stok- ing," but to leave it off entirely, except- ing only when preparing to clear out the grate from clinkers and rubbish, which requires to be done generally three or four times a day with average qualities of 75 coal ; convenient times being chosen for the purpose when there is the least de- mand for steam. 7. A fireman's business is, first, to see, before the fire-door is opened, that no coal is left in the heap ready for going on bigger than a man's fist 5 and that very small coal or slack is wetted, or at least damp, as well as a little water always in the ashpit. Then begin by charging into the farther end of the furnace, reaching to about one-third the length of the grate from the bridge, as rapidly as possible, from a dozen to twenty or thirty spade- fuls of coals, until they form a bank reaching nearly or quite up to the top of the bridge, and then shut the fire-door, until the other fires, if there are any, are served in the same way. 8. In firing up, throw the coals over the rest of the grate by scattering them evenly from side to side, but thinner at the front, near the dead plate, than at the middle or back. In this manner keep the fuel moderately thick and level across the bars, but always thicker at the back than 76 the front, not by pushing the fire in, but by throwing the coals on exactly where they are wanted. 9. Never for a moment leave any por- tion of the bars uncovered, which must be prevented by throwing or pitching a spadeful of coals right into any hollow or thin place that appears ; and always remember that three or four spadefuls thrown quickly one on the top of the other, will make no more smoke than one, and generally less. But all depends on doing it quickly ; that being the main, if not the only point in which freedom from smoke and economy of fuel agree. Some firemen only put on three spadefuls, while another can put on four, and make 20 per cent, more steam in the same time by doing it. 10. In replenishing the fire, take every opportunity of keeping up the bank of fuel at the bridge, by re-charging it, one side at a time. Whenever this bank is burnt entirely through, or low, and also when the fire is in a low state generallv, take the rake and draw back the half- 77 burnt fuel, 12 or 18 in. from the bridge, and re-charge fresh coal into its place, upon the bare fire-bars as at first. 11. An engine fire tended in this way will consume its own smoke without difficulty, simply by admitting a very moderate supply of air (which for safety to the boiler should be heated) at the bridge, this being a more certain and economical mode of prevention than that of diluting the smoke by the admission of much cold air at the fire-doors. 12. It may be set down as an axiom that a steam-engine chimney cannot be too large, if only provided with a damper, although ninety-nine in one hundred, at the present time, are decidedly too small. They are unable to create a sufficient draught of air through the furnace, con- sequently a smoky flame is produced, instead of a flame with little or no smoke. 13. Want of chimney draught is a de- fect which no smoke-consuming furnace in the world can remedy, whether using hot air or cold, unless by the application 78 of an artificial blast, which commonly costs as much to work as the heat it creates is worth. 14. It being impossible to consume smoke without great heat, which requires a good draught, and difficult to get aj good draught without a large chimney, I ; here set down a table of chimney pro- portions, which have been practically proved to answer well with the inferior steam coal of the manufacturing and] midland districts for many years past. It is true that some-what smaller dimenj sions might serve where the extravagant use of Newcastle coal is still continued,! as in London ; but even here those di4 mensions and proportions ought to bej adhered to, because of the constant tend4 ency to increase the engine and boileij power, while the same brick chimney reJ mains. For similar reasons I commend with a chimney suitable for a 10-horsd boiler, although a five, or even a 2-horsa engine only, may be required. 79 Nominal Horse-power of boiler. 15. A common low-pressure condens- ing engine is usually overloaded when it has less than 25 circular in. in the cylin- der for each nominal horse-power ; and a high-pressure non -condensing engine ought to have from 10 to 12£, and to be worked at double the effective pressure, at the least, of the former,— say 30 to 40 lbs. per square inch in the boiler. DIMENSIONS —OF— TALL CHIMNEYS. By L. PINZGER. DIMENSIONS OF TALL CHIMNEYS, The formula frequently employed for the determination of the height of a chimney is: u a =P i >Pi>P 3 >P i so as to insure draft. It is necessary then, 1st, to obtain such a pressure p t at the base of the chimney as would be produced by a cur- rent of air required for the combustion ; and 2d, to force the gas to the height of the chimney and discharge it . with suffi- cient velocity. The difference of pressure p 0 —p 1 can- not be determined by theory alone, but the direct measure of it is obtained by the manometer. In stationary furnaces this difference corresponds to a water column of 3 to 20 millimeters, according to the thickness of the layer of fuel. In locomotives it may be as high as 100 millimeters. As the weight of a column of water having a base of one square meter and a height of one millimeter is one kilogram, it follows that p 0 — p^ may be equal from 3 to 20 kilograms per square meter. 87 If we let h t represent the height of a column of air of the temperature T 0 of which the weight upon one square meter of base is p 0 -p„ we shall have B expressing the constant of the equa- tion of gaseous condition, pv=HT. R being equal to 29.3 for atmospheric air, more or less humid. In taking p 0 =1000 fc per square meter under average conditions of barometric pressure, and T=273 + 17=290, a column of air of A 0 =4 m .25 to 17™ will be equal to the pressure above mentioned. The height h 0 will depend upon the quantity of the fuel burned in a unit of time— the thickness of the layer of fuel and upon the weight of the products of combustion. Grashof assumes for the heat of soft coal the value A 0 =25 G, A 2 in which G represents the quantity of gas produced by the combustion of 1 kilogram of fuel, and A the thickness of the layer of fuel. (1) 88 If G 1 = 22 kilograms and A = 0 m .l, we have: ^ o = 25x22x0.01 = 5 m .50. We may by this calculation find with suffi- cient exactness the values of the differences of pressure p, — p„ —p 3 andp 3 —

4 upon the lower and upper bases, and of which the weight measures the pressure jt?,— p 4 on a square meter. Consequently I 8 * h ^Yg\ % + In this equation u 0 represents the velocity with which the heated gas passes the section /of the flues if they have the temperature T t ; T 2 and T a are the temperatures at the escape from the flue ; Tic the absolute temperature (of water in a steam boiler); I the length of the flues ; d their mean diameter (P being the perimeter and / the section) ; F the heated surface of the boiler ; Q the quan- tity of heat transmitted by this surface every hour; k the coefficient of con- ductivity of the surface for heat, which for boilers is about 20; C„ and C 3 the 90 coefficients of correction relating to the sudden changes in diameter and direc- tion ; (in steam boilers £,=1.5 to 25, and C 3 = 0.8 to 1) ; A the coefficient of friction in the flues ( = 0.08). Between the quantities F, Q, T s , T 3 and (A) T t =T k + (T,-T k )e~oc (B) Q=G.(T 2 -T 3 ) in which G expresses the weight of the gases flowing through each section of the flues per second, and c is the specific heat, of which the mean value is 0.25 for bituminous coal fuel. The weight of a column of air of the external temperature T 0 and a height h 0 + Aj, representing the difference of pressure 4 per square meter, the point is to determine the height h above the level of the grate to which the gases can be raised in the atmosphere. This would be the height for the chimney. In this calculation there should be taken into account ; 1st, the diminution of atmospheric pressure due to the height h; 2d, the diminution of the 1)1 pressure of gas for the same height ; 3d, the mechanical work consumed by the ascent of the gas through this height ; 4th, the velocity of the escaping gas at the top of the chimney. This outflow cannot evidently take place unless the pressure on the escaping gas is at least equal to the atmospheric pressure. In order to calculate the upward ve- locity of the gases in the chimney, we make use of the equation in which p is the pressure at the top of the chimney and d m is the mean diameter. If we represent by w 4 T 4 and p t re- spectively, the velocity, the absolute temperature and the pressure of the gas at the base of the chimney; also by xi a T a and p, the same quantities at the upper outlet of the chimney ; the integra- tion of the preceding equation, if we take T TO =^(T 4 + T« ) for the mean tempera- ture of the chimney, also w TO =i (u t + u a ) for the mean velocity, will give for the term relating to the resistance of friction udu 0 -ds-BT ^dp ^ ds i? 92 On the other hand we shall have for the height h of a column of air, at the temperature T and under the upper and lower pressures of /> 0 and p, MS)- A=KT„ P Combining the preceding equations we get: RT o log(^)=A?^_|». \ PJ J-m ■ L 7n Zg d m ' 2g f " The first number of this being only the value of h Q + h x , the height of the chimney will be given by the formula : 0) ^fc+W^+g ( u *)*i?L h M i ) x « \u a l d m \n a J )T m -T in applying which to find approximate values of h, the following hypothesis is employed : 98 From the fundamental equation pv — RT, and from the equation fn=G'v we deduce ™ T G being the weight of gas in kilograms which passes each section of the chimney in a unit of time with the velocity u. The influence of the change of pressure p upon the variation of the velocity u is so small that we may neglect it, while we have to regard the influence of change of temperature and of cross section, and we have with sufficient exactness: We can calculate from equation (3) a first approximate value of h, after having assigned proper values to f a f t and f m , also to T a according to the value of T 4 and according to the material of which the chimney is built. It is necessary also to determine — — — and — Vm , u a T f k and a 94 since in the term y- we substitute the T m approximate value (/?„ + /',) T _ T • J-m -*- 0 From this value of h a more exact value of T a can be deduced by employing the equation Jc F T a -T 0 + (T 4 -T 0 ) e -'G 5 c in which k 8 represents the coefficient of conductivity of heat for the sides of the chimney ; F s the area of the interior sur- face; G 8 the weight of gas per hour passing any section of the chimney; c=0.25, the specific heat of the gaseous mixture. For chimneys of masonry, we take K 8 =1.4 to 2 according to the thickness of the sides. For chimneys in plate or sheet iron k 8 =6; G s =22B n ; B w being the weight of coal consumed per hour on all the grates whose fires lead to the same chimney. From this value of T a we easily deduce more exact values of T m , — 1 and of — — . u a Ha 95 We shall then be able to obtain a second approximate value of h, which may be re- garded as a definite value. We shall have for the magnitude of f a the entrance to the chimney, Ja ~ 3600 u a or /a = 0 .062-^. " 3600 In calculating ~ there are three cases .7 4 to be considered : 1st. The transverse section of the chimney decreases from the bottom up- wards ; / a f 4 . (Fig 3.) When f a is less than/ 4 , the ratio varies from 0.40 to 0.64 for chimneys constructed either in masonry or iron according to height. We may take therefore as a mean value*^-=0.52. J 4 96 The second condition of course gives ta _-i ' f For the third case we take -~ =1.5. J K With regard to the temperatures T 4 and T a we may introduce as first values in the calculation T — 4 =1.06 for chimneys in masonry. J-a T and = r *=1.10 for iron chimneys. For the velocity u a with which the gas ought to escape from the chimney, we should take a rather large value for fear of interference by downward currents of air. The value of u a should never be less than two meters. Suppose that to calculate the dimen- sions of a masonry chimney, we admit T that -=-*- = 1.06. We shall then obtain -*-fl! the following values : For the first type, (Fig. 1) ^-1.06.0.55=0.55; ^=0.775 U a u a 97 \ thus A=(A B + A,) T T ^ T + " A -A . 0.6 + 0.7 1=-^ Wot, 1 J-m for the second type, (Fig. 2) =1.06; ^=1.03 Va Ua then A^^ + AJ^Hf + * 2<7 A A. 1.06 -0.24 LAjr* for the third type, (Fig. 3) -^=1.06.1.5 = 1.59; —=1.3; then (h=h t + h i ) T, /? ) T It is easy to see that for all forms the total height of the chimney depends ; 1st, upon the amount of resistance encount- ered by the gases in the flues and through the fuel ; 2d, upon the velocity of escape 98 of the gases. The second term is veiy small compared with the first, and as the variation of h for one type or the other depends on the second term, it is evident that the employment of type No. 3 can- not lead to a notable diminution of the height which it is necessary to use in JN o. 1. On the contrary the height be- comes even less for the chimney con- tracted in the upper part than for the cylindrical form or for that which en- larges upwards ; if it is demanded that the velocity of escape of the gases it a be the same for the three types, the reason is that for the first form the resistance due to friction is more feeble. The fact should not be lost that in consequence of the large value of t< 4 for the 3d type com- pared with the value of the same function for the 1st type, that the specific pressure p t would be much less in the first case than in the second ; consequently the en- largement of the chimney towards the top would occasion a stronger current of hot gases at the bottom. If on the other hand we desire that the 99 value of w 4 be the same for the three types, for equal ratios of temperatures and pressures, we shall have for the chimneys : Fig. 1, w«=1.82 « 4 , Fig. 2, w o =0.94w 4 , Fig. 3, u a =0 63 m 4 . Let for example, for the 1st form « a =4 meters consequently w 4 = 2 m .2. Let in 2d form v a =2 m .01 and in 3d form v a =l m .S9 With this feeble velocity of escape, the draft of the chimney would be easily re- versed by the wind. Take as an example a brick chimney designed to discharge the products of combustion from three boilers of equal size. Allowing for each boiler a heating surface of 60 square meters, and requir- ing a consumption of 100 kilos of coal pBjoh-.mr ■: the length of: the: flues beh.g 30 taeteite',';£nd ^ their-; meaii 'cross seciio^ 4/ f—0.2 sq. rioter; we have d— 0.^25. 100 LetT 2 = 1300°; Tjfc=420°; G = 2200* we shall have according to (A) 10.60 ~22C0.0,25 „ n _ 0 T 6 =420 + (1300-420) e = 520°; and according to (B) Q=2200 X 0.25(1300 - 520) =429000". (The heat directly radiated not being included.) For T o =280° we shall have: Gv 2200x0.8 "~ 3600/ _ 3600x0.2 and according to equation (2) : , 3X1300 + 1X520 h =0.306 = 2 W .45 280 ' 30 / 4 29000 420 + a08 -0T25\ 20X 60 x 280 + 280 _ 2 1300-520, 3 280 S Assuming A 0 ==B m .5 we shall have: ""Since th^* Heated g'asses • are? 55ooi(5d -m passing through, the # horizontal ^conduit, we iWi*^*? to* 'idnjit'thati ft Je ja*bsolute 101 temperature T 4 is only 500° at the base of the chimney ; whence T„= ^=470° and T m =i(600 + 470) i- 06 =485° We will take the velocity of escape of the gas, u a =& meters, so that when only one boiler is used the velocity will be 2 meters ;' we then have : w a 2 = 1^.835, and equation (4) gives : f a =0.062^ • 1^=0.405 sq. meters, o obO d a — 0.718, or nearly 0.72 meters. In order to provide, in case of need for a fourth boiler, we will take : / 4 =4/=4x 0.2=0.8 sq. meters, then <# 4 =1.0 meter, and d m -\{l.Q + 0.72)=0.86 meters. We now have ^ = 52? _^6 = 0.54 and ^=0.77. v a 470 0.800 u a The first approximate value then is 102 ( 4G nn ) 280 | 0.08. 0.593^+ 0.708 A = 39.665+8. 133 = 47 m . 798, say 48 meters. We obtain more exactly 1.6.180 „ * ~ 6600.0.25 .__ 0 T a =280 + (500-280) e =473°. This result accords so well with the value 470° introduced above in the calcu- lations of T a , that it will not be necessary to make any correction in the estimated height of 48 meters. We have %i= 0.54 X 6=3.24 meters for the velocity with which the gas enters a chimney whose cross section diminishes upward. (Fig. 1.) If a cylindrical chimney be used (Fig. 2) for which the velocity of escape u a — 0.94x3.24=3.046 meters, the height h will be reduced to : A=39.665 + 0.473 0.08^106 - 0.124 ' 280 1.0 |485-280 A =39.665 + 2.221=41™. 886, or 42™. 103 For a chimney, wider at the top than the bottom, for which ^ = 1.5, we have u a =0.6S . 3.24=2 W .04 and /t=39.665 + 0.212 |0.08^ 1.7-1.53 /*=39.665 + 0.999=40 m .664, or 41 m . The employment of the forms repre- sented in figures 2 and 3 leads to a re- duction in the estimated height of 6 or 7 meters, but the velocity of the escaping gases is reduced from 6 to 2 or 3 meters, which might lead to serious inconvenience when only one boiler is at work instead of three. In such a case a chimney of the third type, the velocity of the escaping gases would only be § meter. In order to diminish the downward action of the wind, the chimney may be surmounted by a conical cap. Many con- structors do not approve of the widened top, although it allows of greater width 104 to the orifice and therefore greater facili- ties for changing the direction of the currents of air at the summit of the chimney. »* Any book in this Catalogue sent free by mail on receipt of price. VALUABLE SCIENTIFIC BOOKS PUBLISHED BY D. VAN NOSTRAND, 23 Murray Street and 27 Warren Street, N. Y. ADAMS (J W.) Sewers and Drains for Populous Districts. 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