APPENDIX.

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[Pg505]
TOCINX

On the Relation between the Temperature, Pressure, and Density of Common Steam.

There is a fixed relation between the temperature and pressure of common steam, which has not yet been ascertained by theory. Various empirical formulÆ have been proposed to express it, derived from tables of temperatures and corresponding pressures which have been founded on experiments and completed by interpolation.

The following formula, proposed by M. Biot, represents with great accuracy the relation between the temperature and pressure of common steam, throughout all that part of the thermometric scale to which experiments have been extended.

Let

a = 5·96131330259
log. a1 = 0·82340688193 - 1
log. b1 = -·01309734295
log. a2 = 0·74110951837
log. b2 = -·00212510583

The relation between the temperature t with reference to the centesimal thermometer, and the pressure p in millimÈtres of mercury at the temperature of melting ice, will then be expressed by the following formula:—

log. p = a - a1b120 + t - a2b220 + t. (1.)

FormulÆ have, however, been proposed, which, though not applicable to the whole scale of temperatures, are more manageable in their practical application than the preceding.

For pressures less than an atmosphere, Southern proposed the following formula, where the pressure is intended to be expressed [Pg506] in pounds per square inch, and the temperature in reference to Fahrenheit's thermometer,—

p = 0·04948 + ( 51·3 + t ) 5·13 .(2.)
155·7256
t = 155·7256 {(p - 0·04948)1/5·13 - 51·3}

The following formula was proposed by Tredgold, where p expresses the pressure in inches of mercury:—

p = ( 100 + t ) 6 .
177

This was afterwards modified by Mellet, and represents with sufficient accuracy experiments from 1 to 4 atmospheres. Let p represent pounds per square inch, and t the temperature by Fahrenheit's thermometer,—

p = ( 103 + t ) 6 .(3.)
201·18
t = 201·18 p 1/6 - 103

M. de Pambour has proposed the following formula, also applicable through the same limits of the scale:—

p = ( 98·806 + t ) 6 . (4.)
198·562
t = 198·562 p 1/6 - 98·806

MM. Dulong and Arago have proposed the following formula for all pressures between 4 and 50 atmospheres:—

p = (0·26793 + 0·0067585 t)5 . (5.)
t = 147·961 p1/5 - 39·644

It was about the year 1801, that Dalton, at Manchester, and Gay-Lussac, at Paris, instituted a series of experiments on gaseous bodies, which conducted them to the discovery of the law mentioned in art. (96.), p. 171. These philosophers found that all gases whatever, and all vapours raised from liquids by heat, as well as all mixtures of gases and vapours, are subject to the same quantity of expansion between the temperatures of melting ice and boiling water; and by experiments subsequently made by Dulong and Petit, this uniformity of expansion has been proved to extend to all temperatures which can come under practical inquiries.

Dalton found that 1000 cubic inches of air at the temperature of melting ice dilated to 1325 cubic inches if raised to the temperature of boiling water. According to Gay-Lussac, the increased volume was 1375 cubic inches. The latter determination has been subsequently found to be the more correct one.[40]

[Pg507]

It appears, therefore, that for an increase of temperature from 32° to 212°, amounting to 180°, the increase of volume is 375 parts in 1000; and since the expansion is uniform, the increase of volume for 1° will be found by dividing this by 180, which will give an increase of 2081/3 parts in 100,000 for each degree of the common thermometer.

To reduce the expression of this important and general law to mathematical language, let v be the volume of an elastic fluid at the temperature of melting ice, and let nv be the increase which that volume would receive by being raised one degree of temperature under the same pressure. Let V be its volume at the temperature T. Then we shall have

V = v + nv (T - 32) = v {1 + n (T - 32)}.

If V' be its volume at any other temperature T', and under the same pressure, we shall have, in like manner,

V' = v {1 + n (T' - 32)}.

Hence we obtain

V = 1 + n (T - 32) ;(6.)
V' 1 + n (T' - 32)

which expresses the relation between the volumes of the same gas or vapour under the same pressure and at any two temperatures. The co-efficient n, as explained in the text, has the same value for the same gas or vapour throughout the whole thermometric scale. But it is still more remarkable that this constant has the same value for all gases and vapours. It is a number, therefore, which must have some essential relation to the gaseous or elastic state of fluid matter, independent of the peculiar qualities of any particular gas or vapour.

The value of n, according to the experiments of Gay-Lussac, is 0·002083, or 1/480.

To reduce the law of Mariotte, explained in (97.) p. 171., to mathematical language, let V, V' be the volumes of the same gas or vapour under different pressures P, P', but at the same temperature. We shall then have

VP = V'P'. (7.)

If it be required to determine the relation between the volumes of the same gas or vapour, under a change of both temperature and pressure, let V be the volume at the temperature T and under the pressure P, and let V' be the volume at the temperature T' and under the pressure P'. Let v be the volume at the temperature T and under the pressure P'.

By formula (7.) we have

VP = vP';

[Pg508]

and by formula (6.) we have

V' = 1 + n(T' - 32)
v 1 + n(T - 32)

Eliminating v, we shall obtain

V = P' · 1 + n(T - 32) ;
V' P 1 + n(T' - 32)

or,

VP = 1 + n(T - 32) ;(8.)
V'P' 1 + n(T' - 32)

which is the general relation between the volumes, pressures, and temperatures of the same gas or vapour in two different states.

To apply this general formula to the case of the vapour of water, let T' = 212°. It is known by experiment that the corresponding value of P', expressed in pounds per square inch, is 14·706; and that V', expressed in cubic inches, the water evaporated being taken as a cubic inch, is 1700. If, then, we take 0·002083 as the value of n, we shall have by (8.),

VP = 1700 × 14·706 × {1 + 0·002083 (T - 32)}
1 + 0·002083 × 180
= 18183{1 + 0·002083 (T - 32)}. (9.)

If, by means of this formula (9.), and any of the formulÆ (1.), (2.), (3.), (4.), (5.), T were eliminated, we should obtain a formula between V and P, which would enable us to compute the enlargement of volume which water undergoes in passing into steam under any proposed pressure. But such a formula would not be suitable for practical computations. By the formulÆ (1.) to (5.), a table of pressures and corresponding temperatures may be computed; and these being known, the formula (9.) will be sufficient for the computation of the corresponding values of V, or the enlargement of volume which water undergoes in passing into steam.

In the following table, the temperatures corresponding to pressures from 1 to 240 lbs. per square inch are given by computation from the formulÆ (2.) to (5.), and the volumes of steam produced by an unit of volume of water as computed from the formula (9.).

The mechanical effect is obtained by multiplying the pressure in pounds by the expansion of a cubic inch of water in passing into steam expressed in feet, and is therefore the number of pounds which would be raised one foot by the evaporation of a cubic inch of water under the given pressure. [Pg509]

Total pressure in Pounds per Square Inch. Corresponding Temperature. Volume of the Steam compared to the Volume of the Water that has produced it. Mechanical Effect of a Cubic Inch of Water evaporated in Pounds raised One Foot.
1 102·9 20868 1739
2 126·1 10874 1812
3 141·0 7437 1859
4 152·3 5685 1895
5 161·4 4617 1924
6 169·2 3897 1948
7 175·9 3376 1969
8 182·0 2983 1989
9 187·4 2674 2006
10 192·4 2426 2022
11 197·0 2221 2036
12 201·3 2050 2050
13 205·3 1904 2063
14 209·1 1778 2074
15 212·8 1669 2086
16 216·3 1573 2097
17 219·6 1488 2107
18 222·7 1411 2117
19 225·6 1343 2126
20 228·5 1281 2135
21 231·2 1225 2144
22 233·8 1174 2152
23 236·3 1127 2160
24 238·7 1084 2168
25 241·0 1044 2175
26 243·3 1007 2182
27 245·5 973 2189
28 247·6 941 2196
29 249·6 911 2202
30 251·6 883 2209
31 253·6 857 2215
32 255·5 833 2221
33 257·3 810 2226
34 259·1 788 2232
35 260·9 767 2238
36 262·6 748 2243
37 264·3 729 2248
38 265·9 712 2253
39 267·5 695 2259
40 269·1 679 2264
41 270·6 664 2268
42 272·1 649 2273
43 273·6 635 2278
44 275·0 622 2282
45 276·4 610 2287
46 277·8 598 2291
47 279·2 586 2296
48 280·5 575 2300
49 281·9 564 2304
50 283·2 554 2308
51 284·4 544 2312
52 285·7 534 2316
53 286·9 525 2320
54 288·1 516 2324
55 289·3 508 2327
56 290·5 500 2331
57 291·7 492 2335
58 292·9 484 2339
59 294·2 477 2343
60 295·6 470 2347
61 296·9 463 2351
62 298·1 456 2355
63 299·2 449 2359
64 300·3 443 2362
65 301·3 437 2365
66 302·4 431 2369
67 303·4 425 2372
68 304·4 419 2375
69 305·4 414 2378
70 306·4 408 2382
71 307·4 403 2385
72 308·4 398 2388
73 309·3 393 2391
74 310·3 388 2394
75 311·2 383 2397
76 312·2 379 2400
77 313·1 374 2403
78 314·0 370 2405
79 314·9 366 2408
80 315·8 362 2411
81 316·7 358 2414
82 317·6 354 2417
83 318·4 350 2419
84 319·3 346 2422
85 320·1 342 2425
86 321·0 339 2427
87 321·8 335 2430
88 322·6 332 2432
89 323·5 328 2435
90 324·3 325 2438
91 325·1 322 2440
92 325·9 319 2443
93 326·7 316 2445
94 327·5 313 2448
95 328·2 310 2450
96 329·0 307 2453
97 329·8 304 2455
98 330·5 301 2457
99 331·3 298 2460
100 332·0 295 2462
110 339·2 271 2486
120 345·8 251 2507
130 352·1 233 2527
140 357·9 218 2545
150 363·4 205 2561
160 368·7 193 2577
170 373·6 183 2593
180 378·4 174 2608
190 382·9 166 2622
200 387·3 158 2636
210 391·5 151 2650
220 395·5 145 2663
230 399·4 140 2675
240 403·1 134 2687

[Pg511]

In the absence of any direct method of determining the general relation between the pressure and volume of common steam, empirical formulÆ expressing it have been proposed by different mathematicians.

The late Professor Navier proposed the following:—Let S express the volume of steam into which an unit of volume of water is converted under the pressure P, this pressure being expressed in kilogrammes per square mÈtre. Then the relation between S and P will be

S = a ,
b + mP

where a = 1000, b = 0·09, and m = 0·0000484.

This formula, however, does not agree with experiment at pressures less than an atmosphere. M. de Pambour, therefore, proposes the following changes in the values of its co-efficients:—Let P express the pressure in pounds per square foot; and let

a = 10000 b = 0·4227 m = 0·00258,

and the formula will be accurate for all pressures. For pressures above two atmospheres the following values give more accuracy to the calculation:—

a = 10000 b = 1·421 m = 0·0023.

In these investigations I shall adopt the following modified formula. The symbols S and P retaining their signification, we shall have

S = a ,(10.)
b + P

where

a = 3875969 b = 164.

These values of a and b will be sufficiently accurate for practical purposes for all pressures, and may be used in reference to low-pressure engines of every form, as well as for high-pressure engines which work expansively.

When the pressure is not less than 30 pounds per square inch, the following values of a and b will be more accurate:—

a = 4347826 b = 618.

On the Expansive Action of Steam.

The investigation of the effect of the expansion of steam which has been given in the text, is intended to convey to those who are not conversant with the principles and language of analysis, some notion of the nature of that mechanical effect to which the advantages attending the expansive principle are due. We shall now, however, explain these effects more accurately. [Pg512]

The dynamical effect produced by any mechanical agent is expressed by the product of the resistance overcome and the space through which that resistance is moved.

Let

P= the pressure of steam expressed in pounds per square foot.
S= the number of cubic feet of steam of that pressure produced by the evaporation of a cubic foot of water.
E= the mechanical effect produced by the evaporation of a cubic foot of water expressed in pounds raised one foot.

Then we shall have E = PS; and if W be a volume of water evaporated under the pressure P, the mechanical effect produced by it will be WPS.

By (10.) we have

SP = a - bS.

Hence, for the mechanical effect of a cubic foot of water evaporated under the pressure P we have

E = a - bS.(11.)

Let a cubic foot of water be evaporated under the pressure P', and let it produce a volume of steam S' of that pressure. Let this steam afterwards be allowed to expand to the increased volume S and the diminished pressure P; and let it be required to determine the mechanical effect produced during the expansion of the steam from the volume S' to the volume S.

Let

E'= the mechanical effect produced by the evaporation of the water under the pressure P' without expansion.
E= the mechanical effect produced during the expansion of the steam.
E= the mechanical effect which would be produced by the evaporation under the pressure P without expansion.
E= the total mechanical effect produced by the evaporation under the pressure P' and subsequent expansion.

Thus we have

E = E' + E.

Let s be any volume of the steam during the process of expansion, p the corresponding pressure, and e the mechanical effect produced by the expansion of the steam. We have then by (10.)

p = a - b;
s
? de = ads - bds.
s

Hence by integrating we obtain

e = a log. s - bs + C;

[Pg513]

which, taken between the limits s = S' and s = S, becomes

E = a log. S - b(S - S').(12.)
S'

But by (11.) we have

E' = a - bS',
E = a - bS;
? E' - E = b(S - S');
? E = a log. S - E' + E;
S'
? E = E + E' = a log. S + E.(13.)
S'

Or,

E = a (1 + log. S ) - bS.(14.)
S'

Hence it appears that the mechanical effect of a cubic foot of water evaporated under the pressure P may be increased by the quantity a log. S/S', if it be first evaporated under the greater pressure P', and subsequently expanded to the lesser pressure P.

The logarithms in these formulÆ are hyperbolic.

To apply these principles to the actual case of a double acting steam engine,

Let

L=the stroke of the piston in feet.
A=the area of the piston in square feet.
n=the number of strokes of the piston per minute.
?2nAL=the number of cubic feet of space through which the piston moves per minute.

Let

cLA=the clearage, or the space between the steam valve and the piston at each end of the stroke.
? The volume of steam admitted through the steam valve at each stroke of the engine will be 2n AL(1 + c).

Let

V = the mean speed of the piston in feet per minute,
? 2nL = V.

The volume of steam admitted to the cylinder per minute will therefore be VA (1 + c), the part of it employed in working the piston being VA.

Let

W=the water in cubic feet admitted per minute in the form of steam through the steam valve.
S= the number of cubic feet of steam produced by a cubic foot of water.

[Pg514]

Hence we shall have

WS=VA (1 + c);
? S= VA(1 + c) .(15.)
W

Since by (10.) we have

P= a - b;
S
? P= Wa - b.(16.)
VA(1 + c)

By which the pressure of steam in the cylinder will be known, when the effective evaporation, the diameter of the cylinder, and speed of the piston, are given.

If it be required to express the mechanical effect produced per minute by the action of steam on the piston, it is only necessary to multiply the pressure on the surface of the piston by the space per minute through which the piston moves. This will give

VAP=W a - VAb;(17.)
1 + c

which expresses the whole mechanical effect per minute in pounds raised one foot.

If the steam be worked expansively, let it be cut off after the piston has moved through a part of the stroke expressed by e.

The volume of steam of the undiminished pressure P' admitted per minute through the valve would then be

VA (e + c);

and the ratio of this volume to that of the water producing it being expressed by S', we should have

S'= VA(e + c) .
W

The final volume into which this steam is subsequently expanded being VA(1 + c), its ratio to that of the water will be

S= VA (1 + c) .
W

The pressure P', till the steam is cut off, will be

P'= Wa - b.(18.)
VA(e + c)

The mechanical effect E' produced per minute by the steam of full pressure will be

E'=P'AVe= Wae - AVbe;
e + c

and the effect E per minute produced by the expansion of the steam will by (12.) be [Pg515]

E=Wa log. 1 + c - bVA(1 - e).
e + c

Hence the total effect per minute will be

E=Wa{ e + log. 1 + c } - bVA.(19.)
e + c e + c

If the engine work without expansion, e=1;

? E'= Wa - bVA,(20.)
1 + c

as before; and the effect per minute gained by expansion will therefore be

E-E'=Wa{ e - 1 +log. 1+c };(21.)
e+c 1+c e+c

which therefore represents the quantity of power gained by the expansive action, with a given evaporating power.

In these formulÆ the total effect of the steam is considered without reference to the nature of the resistances which it has to overcome.

These resistances may be enumerated as follows:—

  1. The resistance produced by the load which the engine is required to move.
  2. The resistance produced by the vapour which remains uncondensed if the engine be a condensing engine, or of the atmospheric pressure if the engine do not condense the steam.
  3. The resistance of the engine and its machinery, consisting of the friction of the various moving parts, the resistances of the feed pump, the cold water pump, &c. A part of these resistances are of the same amount, whether the engine be loaded or not, and part are increased, in some proportion depending on the load.

When the engine is maintained in a state of uniform motion, the sum of all these resistances must always be equal to the whole effect produced by the steam on the piston. The power expended on the first alone is the useful effect.

Let

R=the pressure per square foot of the piston surface, which balances the resistances produced by the load.
mR=the pressure per square foot, which balances that part of the friction of the engine which is proportional to the load.
r=the pressure per square foot, which balances the sum of all those resistances that are not proportional to the load.

The total resistance, therefore, being R + mR + r, which, when the mean motion of the piston is uniform, must be equal to the mean pressure on the piston. The total mechanical effect [Pg516] must therefore be equal to the total resistance multiplied by the space through which that resistance is driven. Hence we shall have

{R(1 + m) + r}VA=Wa{ e + log. 1 + c } - VAb;
e + c e + c
? RVA(1 + m)=Wa{ e + log. 1 + c } - VA(b + r).
e + c e + c

For brevity, let

e'=a{ e +log. 1 + c };
e + c e + c
? RVA(1 + m)=We' - VA(b + r).(22.)

By solving this for VA, we obtain

VA= We' ;
R(1 + m) + b + r
? RVA= We'R .(23.)
R(1 + m) + b + r

This quantity RVA, being the product of the resistance RA, of the load reduced to the surface of the piston, multiplied by the space through which the piston is moved, will be equal to the load itself multiplied by the space through which it is moved. This being, in fact, the useful effect of the engine, let it be expressed by U, and we shall have

U= We'R .(24.)
R(1 + m) + b + r

Or by (22.),

U(1 + m)=We' - VA(b + r).(25.)

The value of the useful effect obtained from these formulÆ will be expressed in pounds, raised one foot per minute, W being the effective evaporation in cubic feet per minute, A the area of the piston in square feet, and V the space per minute through which it is moved, in feet.

Since a resistance amounting to 33,000 pounds moved through one foot per minute is called one-horse power, it is evident that the horse power H of the engine is nothing more than the useful effect per minute referred to a larger unit of weight or resistance; that is to 33,000 pounds instead of one pound. Hence we shall have

H= U .(26.)
33000

Since the useful effect expressed in (24.) and (25.) is that due to a number of cubic feet of water, expressed by W, we shall obtain the effect due to one cubic foot of water, by dividing U by W. If, therefore, U' be the effect produced by the effective evaporation of a cubic foot of water, we shall have [Pg517]

U'= U .(27.)
W

If the quantity of fuel consumed per minute be expressed by F, the effect produced by the unit of fuel, called the DUTY of the engine, will, for like reason, be

D= U .(28.)
F

If the fuel be expressed in hundredweights of coal, then D will express the number of pounds' weight raised one foot by a hundredweight of coal.

By solving (24.) and (25.) for W, we obtain

W= U{R(1 + m) + b + r} ,(29.)
Re'
W= 1 {U(1 + m) + VA(b + r)}.(30.)
e'

By eliminating U, by (26.), we shall have

W= 33000 H{R(1 + m) + b + r} ,(31.)
Re'
W= 1 {33000 H(1 + m) + VA(b + r)}.(32.)
e'

The evaporation necessary per horse power per minute will be found by putting H=1 in these formulÆ.[41]

It will be observed that the quantities A and V, the area of the cylinder and the speed of the piston, enter all these formulÆ as factors of the same product. Other things, therefore, being the same, the speed of the piston will be always inversely as the area of the cylinder. In fact, VA is the volume of steam per minute employed in working the piston, and if the piston be increased or diminished in magnitude, its speed must be inversely [Pg518] varied by the necessity of being still moved through the same number of cubic feet by the same volume of steam.

It has been already stated in the text, that no satisfactory experiments have yet been made, by which the numerical value of the quantity r can be exactly known. In engines of different magnitudes and powers, this resistance bears very different proportions to the whole power of the machine. In general, however, the larger and more powerful the engine, the less that proportion will be.

That part of this resistance which arises from the reaction of the uncondensed vapour on the piston is very variable, owing to the more or less perfect action of the condensing apparatus, the velocity of the piston, and the magnitude and form of the steam passages. M. de Pambour states, that, by experiments made with indicators, the mean amount of this resistance in the cylinder is 21/2 lbs. per square inch more than in the condenser, and that the pressure in the latter being usually 11/2 lb. per square inch, the mean amount of the pressure of the condensed vapour in the cylinder is about 4 lbs. per square inch. Engineers, however, generally consider this estimate to be above the truth in well-constructed engines, when in good working order.

In condensing low pressure engines of forty horse power and upwards, working with an average load, it is generally considered that the resistance produced by the friction of the machine and the force necessary to work the pumps may be taken at about 2 lbs. per square inch of piston surface.

Thus the whole resistance represented by r in the preceding formulÆ, as applied to the larger class of low pressure engines, may be considered as being under 6 lbs. per square inch, or 864 lbs. per square foot, of the piston. It is necessary, however, to repeat, that this estimate must be regarded as a very rough approximation; and as representing the mean value of a quantity subject to great variation, not only in one engine compared with another, but even in the same engine compared with itself at different times and in different states.

In the same class of engines, the magnitude of the clearage is generally about a twentieth part of the capacity of the cylinder, so that c=0·05.

That part of the resistance which is proportional to the load, and on which the value of m in the preceding formulÆ depends, is still more variable, and depends so much on the form, magnitude, and the arrangement of its parts, that no general rule can be given for its value. It must, in fact, be determined in every particular case.

In the practical application of the preceding formulÆ in condensing engines we shall have [Pg519]

a=3875969 b=164 c=0·05;
e'=3875969{ e + log. 1·05 }.
e + 0·05 e + 0·05

In engines which work without condensation, and therefore with high pressure steam, we shall have

a=4347826 b=618 c=0·05;
e'=4347826{ e + log. 1·05 }.
e + 0·05 e + 0·05

To facilitate computation, the values of e' corresponding to all values of e, from e=·10 to e=·90, are given in the following table:—

e Condensing Engines e'. Non-condensing Engines e'. e Condensing Engines e'. Non-condensing Engines e'.
·10 10126265 11359029 ·51 5966367 6692708
·11 9956867 11169008 ·52 5903837 6622565
·12 9793136 10985344 ·53 5842288 6553525
·13 9634926 10807875 ·54 5781693 6485552
·14 9482029 10636364 ·55 5722024 6418619
·15 9334219 10470560 ·56 5663251 6352693
·16 9191251 10310186 ·57 5605353 6287745
·17 9052888 10154978 ·58 5548297 6223742
·18 8918896 10004675 ·59 5492064 6160662
·19 8789043 9859014 ·60 5436628 6098478
·20 8663120 9717760 ·61 5381969 6037166
·21 8540918 9580682 ·62 5328065 5976699
·22 8422242 9447559 ·63 5274896 5917057
·23 8306916 9318193 ·64 5222444 5858219
·24 8194770 9192396 ·65 5170684 5800159
·25 8085644 9069984 ·66 5119605 5742860
·26 7979392 8950796 ·67 5069186 5686304
·27 7875870 8834674 ·68 5019410 5630469
·28 7774952 8721468 ·69 4970263 5575340
·29 7676514 8611048 ·70 4921727 5520894
·30 7580447 8503284 ·71 4873790 5467121
·31 7486640 8398056 ·72 4826434 5414000
·32 7394990 8295250 ·73 4779648 5361519
·33 7305407 8194760 ·74 4733417 5309659
·34 7217807 8096496 ·75 4687728 5258408
·35 7132097 8000352 ·76 4642569 5207751
·36 7048206 7906249 ·77 4597928 5157676
·37 6966058 7814100 ·78 4553794 5108170
·38 6885585 7723832 ·79 4510155 5059218
·39 6806720 7635365 ·80 4466999 5010808
·40 6729408 7548642 ·81 4424317 4962931
·41 6653578 7463580 ·82 4382096 4915569
·42 6579187 7380132 ·83 4340332 4868720
·43 6506174 7298230 ·84 4299010 4822368
·44 6434491 7217822 ·85 4258120 4776500
·45 6364099 7138858 ·86 4217658 4731113
·46 6294944 7061285 ·87 4177613 4686192
·47 6226989 6985058 ·88 4137974 4641728
·48 6160190 6910126 ·89 4098737 4597713
·49 6094510 6836450 ·90 4059893 4554140
·50 6029916 6763992

[Pg520]

In engines which work without expansion we have

e'= a .
1 + c

For condensing engines without expansion, we shall then have

e'= 3875969 =3691399;(33.)
1·05

and for non-condensing engines,

e'= 4347826 =4140787.(34.)
1·05

As the diameters of the cylinders of engines are generally expressed in inches, the corresponding areas of the pistons expressed in square feet are given in the following table, so that the values of A may be readily found:—

Diameter. Area. Diameter. Area.
Inches. Sq. Feet. Inches. Sq. Feet.
10 07545 48 127566
11 07660 49 137095
12 07785 50 137635
13 07922 51 147186
14 17069 52 147748
15 17227 53 157321
16 17396 54 157904
17 17576 55 167499
18 17767 56 177104
19 17969 57 177721
20 27182 58 187348
21 27405 59 187986
22 27640 60 197635
23 27885 61 207295
24 37142 62 207966
25 37409 63 217648
26 37687 64 227340
27 37976 65 237044
28 47276 66 237758
29 47587 67 247484
30 47909 68 257220
31 57241 69 257967
32 57585 70 267725
33 57940 71 277494
34 67305 72 287274
35 67681 73 297065
36 77069 74 297867
37 77467 75 307680
38 77876 76 317503
39 87296 77 327338
40 87727 78 337183
41 97168 79 347039
42 97621 80 347907
43 107085 81 357785
44 107559 82 367674
45 117045 83 377574
46 117541 84 387485
47 127048 85 397406
Diameter. Area. Diameter. Area.
Inches. Sq. Feet. Inches. Sq. Feet.
86 407339 124 837863
87 417283 125 857221
88 427237 126 867590
89 437202 127 877970
90 447179 128 897361
91 457166 129 907763
92 467164 130 927175
93 477173 131 937599
94 487193 132 957033
95 497224 133 967479
96 507265 134 977935
97 517318 135 997402
98 527382 136 1007880
99 537456 137 1027369
100 547542 138 1037869
101 557638 139 1057380
102 567745 140 1067901
103 577863 141 1087434
104 587992 142 1097977
105 607132 143 1117532
106 617283 144 1137097
107 627445 145 1147674
108 637617 146 1167261
109 647801 147 1177859
110 657995 148 1197468
111 677201 149 1217088
112 687417 150 1227719
113 697644 151 1247361
114 707882 152 1267013
115 727131 153 1277676
116 737391 154 1297351
117 747662 155 1317036
118 757944 156 1327732
119 777236 157 1347439
120 787540 158 1367157
121 797854 159 1377886
122 817180 160 1397626
123 827516 161 1417377

[Pg521]

The practical application of the preceding formulÆ will be shown by the following examples.

EXAMPLES.

1. A 36-inch cylinder with 51/2 feet stroke is supplied by a boiler evaporating effectively 60 cubic feet of water per hour, and the piston makes 20 strokes per minute without expansion;—what is the power of the engine and the pressure of steam in the cylinder?

Let it be assumed that r=6 × 144=864 and m=0·1. Since the engine is a condensing engine, we have b=164 and e'=3691399. By the formulÆ (25.) and (26.) we have

H= We' - VA(b + r) ;
33000(1 + m)

and since by the data we have

W=1 A=7·069 V=2nL=40 × 5·5=220,

the formula, by these substitutions, becomes

H= 3691399 - 220 × 1028 × 7·069 ;
33000 × 1·1
? H = 57·6.

Since e=1, the pressure P of steam in the cylinder, by (18.), is

P= We' - b.
VA

Therefore

P= 3691399 - 164=2210;
1555·18

which being the pressure in pounds per square foot, the pressure per square inch will be 151/3 lbs.

2. To find the effective evaporation necessary to produce a power of 80 horses with the same engine. Also, find the pressure of steam in the cylinder, the speed of the piston being the same.

By the formula (32.), with the above substitutions, we have

W= 33000 × 80 × 1·1 + 220 × 7069 × 1028 =1·22.
3691399

The evaporating power would therefore be only increased 22 per cent., while the working power of the engine would be increased nearly 40 per cent.

The pressure P in the cylinder will be given, by (18.), as before.

P= 1·22 × 3691399 - 164=2732;
1555·18

which is equivalent to 19 lbs. per square inch. [Pg522]

3. What must be the diameter of a cylinder to work with a power of a hundred horses, supplied by a boiler evaporating effectively 70 cubic feet of water per hour, the mean speed of the piston being 240 feet per minute, and the steam being cut off at half stroke? Also, what will be the full pressure of steam on the piston?

Taking, as in the former examples, m=0·1, b=164, and r=864, we shall have

H=100 W = 7/6 V=240,

and by the column for condensing engines, in table, p. 519, we have e'=6029916, where e=0·50. Making these substitutions in

We'=33000 H(1 + m) + VA(b + r),

we shall have

(7/6) × 6029916=3300000 × 1·1 + 240 × 1028 × A.

Whence we find

A=13·8;

and by the table, p. 520, the corresponding diameter of the cylinder will be 501/3 inches.

If P' be the full pressure of the steam, we shall have, by (18.),

P'= Wa - b.
VA(e + c)

Making in this the proper substitutions, we have

P'= 7/6 × 3875969 - 164=2318;
240 × 13·8 × 0·55

which being in pounds per square foot, the pressure per square inch will be 161/10 lbs.

[40] M. de Pambour states that the increased volume is 1364 cubic inches.

[41] FormulÆ equivalent to some of the preceding are given, with numerous others, by M. de Pambour, in his Theory of the Steam Engine. These mathematical details contain nothing new in principle, being merely the application of the known principles of general mechanics to this particular machine. M. de Pambour objects against the methods of calculating the practical effects of steam engines generally adopted by engineers in this country. Their estimates of the loss of power by friction, imperfect condensation, and other causes, are, as I have stated in this volume, vague, and can be regarded at best as very rough approximations; but, subject to the restrictions under which their methods of calculation are always applied, they are by no means so defective as M. de Pambour supposes. He proves what he considers to be their inaccuracy, by applying them in cases in which they are never intended to be applied by English engineers. Those who desire to reduce to general algebraical formulÆ the effects of the different kinds of steam engines will, however, find the volume of M. de Pambour of considerable use.

                                                                                                                                                                                                                                                                                                           

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