Composition of air--

by volume 0.788 N + 0.197 O + 0.001 CO2 + 0.014 H2O

----------------------------------------------------

by weight 0.771 N + 0.218 O + 0.009 CO2 + 0.017 H2O

This law is, however, subject to some apparent exceptions. Carbon

burned in protoxide of nitrogen, or laughing gas, N_{2}O, produces

about 38 per cent. more heat than the same substance burned in pure

oxygen, notwithstanding that the work of decomposing the protoxide of

nitrogen has to be performed. In marsh gas, or methane, CH_{4}, again,

the energy of combustion is considerably less than that due to the

burning of its carbon and hydrogen separately. These exceptions

probably arise from the circumstance that the energy of chemical

action is absorbed to a greater or less degree in effecting molecular

changes, as, for example, the combustion of 1 pound of nitrogen to

form protoxide of nitrogen results in the absorption of 1,157 units of

heat. Berthelot states, as one of the fundamental principles of

thermochemistry, "that the quantity of heat evolved is the measure of

the sum of the chemical and physical work accomplished in the

reaction"; and such a law will no doubt account for the phenomena

above noted. The equivalent heat of combustion of the compounds we

have practically to deal with has been experimentally determined, and

therefore constitutes a secure basis on which to establish

calculations of the caloric value of fuel; and in doing so, with

respect to substances composed of carbon, hydrogen, and oxygen, it is

convenient to reduce the hydrogen to its heat-producing equivalent of

carbon. The heat of combustion of hydrogen being 62,032 units, that of

carbon 14,544 units, it follows that 4.265 times the weight of

hydrogen will represent an equivalent amount of carbon. With respect

to the oxygen, it is found that it exists in combination with the

hydrogen in the form of water, and, being combined already, abstracts

its combining equivalent of hydrogen from the efficient ingredients of

the fuel; and hence hydrogen, to the extent of 1/8 of the weight of

the oxygen, must be deducted. The general formula then becomes:

Heat of combustion = 14,544 {C + 4.265 (H-(O/8))},

and water evaporated from and at 212°, taking 966 units as the heat

necessary to evaporate 1 pound of water,

lb. evaporated = 15.06 {C + 4.265 (H-(O/8))},

carbon, hydrogen, and oxygen being taken at their weight per cent. in

the fuel. Strictly speaking, marsh gas should be separately

determined. It often happens that available energy is not in a form in

which it can be applied directly to our needs. The water flowing down

from the mountains in the neighborhood of the Alpine tunnels was

competent to provide the power necessary for boring through them, but

it was not in a form in which it could be directly applied. The

kinetic energy of the water had first to be changed into the potential

energy of air under pressure, then, in that form, by suitable

mechanism, it was used with signal success to disintegrate and

excavate the hard rock of the tunnels. The energy resulting from

combustion is also incapable of being directly transformed into useful

motive power; it must first be converted into potential force of steam

or air at high temperature and pressure, and then applied by means of

suitable heat engines to produce the motions we require. It is

probably to this circumstance that we must attribute the slowness of

the human race to take advantage of the energy of combustion. The

history of the steam engine hardly dates back 200 years, a very small

fraction of the centuries during which man has existed, even since

historic times.

The apparatus by means of which the potential energy of fuel with

respect to oxygen is converted into the potential energy of steam, we

call a steam boiler; and although it has neither cylinder nor piston,

crank nor fly wheel, I claim for it that it is a veritable heat

engine, because it transmits the undulations and vibrations caused by

the energy of chemical combination in the fuel to the water in the

boiler; these motions expend themselves in overcoming the liquid

cohesion of the water and imparting to its molecules that vigor of

motion which converts them into the molecules of a gas which,

impinging on the surfaces which confine it and form the steam space,

declare their presence and energy in the shape of pressure and

temperature. A steam pumping engine, which furnishes water under high

pressure to raise loads by means of hydraulic cranes, is not more

truly a heat engine than a simple boiler, for the latter converts the

latent energy of fuel into the latent energy of steam, just as the

pumping engine converts the latent energy of steam into the latent

energy of the pumped-up accumulator or the hoisted weight.

If I am justified in taking this view, then I am justified in applying

to my heat engine the general principles laid down in 1824 by Sadi

Carnot, namely, that the proportion of work which can be obtained out

of any substance working between two temperatures depends entirely and

solely upon the difference between the temperatures at the beginning

and end of the operation; that is to say, if T be the higher

temperature at the beginning, and _t_ the lower temperature at the end

of the action, then the maximum possible work to be got out of the

substance will be a function of (T-_t_). The greatest range of

temperature possible or conceivable is from the absolute temperature

of the substance at the commencement of the operation down to absolute

zero of temperature, and the fraction of this which can be utilized is

the ratio which the range of temperature through which the substance

is working bears to the absolute temperature at the commencement of

the action. If W = the greatest amount of effect to be expected, T and

_t_ the absolute temperatures, and H the total quantity of heat

(expressed in foot pounds or in water evaporated, as the case may be)

potential in the substance at the higher temperature, T, at the

beginning of the operation, then Carnot's law is expressed by the

equation:

/ T - t \

W = H( ------- )

\ T /

I will illustrate this important doctrine in the manner which Carnot

himself suggested.

[Illustration: THE GENERATION OF STEAM. Fig 2.]

Fig. 2 represents a hillside rising from the sea. Some distance up

there is a lake, L, fed by streams coming down from a still higher

level. Lower down on the slope is a millpond, P, the tail race from

which falls into the sea. At the millpond is established a factory,

the turbine driving which is supplied with water by a pipe descending

from the lake, L. Datum is the mean sea level; the level of the lake

is T, and of the millpond _t_. Q is the weight of water falling

through the turbine per minute. The mean sea level is the lowest level

to which the water can possibly fall; hence its greatest potential

energy, that of its position in the lake, = QT = H. The water is

working between the absolute levels, T and _t_; hence, according to

Carnot, the maximum effect, W, to be expected is--

/ T - t \

W = H( ------- )

\ T /

/ T - t \

but H = QT [therefore] W = Q T( ------- )

\ T /

W = Q (T - t),

that is to say, the greatest amount of work which can be expected is

found by multiplying the weight of water into the clear fall, which

is, of course, self-evident.

Now, how can the quantity of work to be got out of a given weight of

water be increased without in any way improving the efficiency of the

turbine? In two ways:

1. By collecting the water higher up the mountain, and by that means

increasing T.

2. By placing the turbine lower down, nearer the sea, and by that

means reducing _t_.

Now, the sea level corresponds to the absolute zero of temperature,

and the heights T and _t_ to the maximum and minimum temperatures

between which the substance is working; therefore similarly, the way

to increase the efficiency of a heat engine, such as a boiler, is to

raise the temperature of the furnace to the utmost, and reduce the

heat of the smoke to the lowest possible point. It should be noted, in

addition, that it is immaterial what liquid there may be in the lake;

whether water, oil, mercury, or what not, the law will equally apply,

and so in a heat engine, the nature of the working substance, provided

that it does not change its physical state during a cycle, does not

affect the question of efficiency with which the heat being expended

is so utilized. To make this matter clearer, and give it a practical

bearing, I will give the symbols a numerical value, and for this

purpose I will, for the sake of simplicity, suppose that the fuel used

is pure carbon, such as coke or charcoal, the heat of combustion of

which is 14,544 units, that the specific heat of air, and of the

products of combustion at constant pressure, is 0.238, that only

sufficient air is passed through the fire to supply the quantity of

oxygen theoretically required for the combustion of the carbon, and

that the temperature of the air is at 60° Fahrenheit = 520° absolute.

The symbol T represents the absolute temperature of the furnace, a

value which is easily calculated in the following manner: 1 lb. of

carbon requires 2-2/3 lb. of oxygen to convert it into carbonic acid,

and this quantity is furnished by 12.2 lb. of air, the result being

13.2 lb. of gases, heated by 14,544 units of heat due to the energy of

combustion; therefore:

14,544 units

T = 520° + ------------------ = 5,150° absolute.

13.2 lb. X 0.238

The lower temperature, _t_, we may take as that of the feed water, say

at 100° or 560° absolute, for by means of artificial draught and

sufficiently extending the heating surface, the temperature of the

smoke may be reduced to very nearly that of the feed water. Under such

circumstances the proportion of heat which can be realized is

5,150° - 560°

= --------------- = 0.891;

5,150°

that is to say, under the extremely favorable if not impracticable

conditions assumed, there must be a loss of 11 per cent. Next, to give

a numerical value to the potential energy, H, to be derived from a

pound of carbon, calculating from absolute zero, the specific heat of

carbon being 0.25, and absolute temperature of air 520°:

Units.

1 lb. of carbon X 0.25 X 520 = 130

12.2 of air X 0.238 X 520 = 1,485

Heat of combustion = 14,544

------

16,159

Deduct heat equivalent to work of \

displacing atmosphere by products of }

combustion raised from 60° to 100°, } 32

or from 149.8 cubic feet to 161.3 }

cubic feet, /

------

Total units of heat available 16,127

Equal to 16.69 lb. of water evaporated from and at 212°. Hence the

greatest possible evaporation from and at 212° from a lb. of carbon--

16,159 u. X 0.891 - 32 u.

W = --------------------------- = 14.87 lb.

966 u.

I will now take a definite case, and compare the potential energy of a

certain kind of fuel with the results actually obtained. For this

purpose the boiler of the eight-horse portable engine, which gained

the first prize at the Cardiff show of the Royal Agricultural Society

in 1872, will serve very well, because the trials, all the details of

which are set forth very fully in vol. ix. of the _Journal_ of the

Society, were carried out with great care and skill by Sir Frederick

Bramwell and the late Mr. Menelaus; indeed, the only fact left

undetermined was the temperature of the furnace, an omission due to

the want of a trustworthy pyrometer, a want which has not been

satisfied to this day.[2]

[Footnote 2: In the fifty-second volume of the _Proceedings_

(1887-78), page 154, will be found a remarkable experiment on the

evaporative power of a vertical boiler with internal circulating

pipes. The experiment was conducted by Sir Frederick Bramwell and

Dr. Russell, and is remarkable in this respect, that the quantity

of air admitted to the fuel, the loss by convection and

radiation, and the composition of the smoke were determined. The

facts observed were as follows:

Steam pressure 53 lb................................... = 300.6° F.

lb.

Fuel--Water in coke and wood........................... 26.08

Ash.............................................. 10.53

Hydrogen, oxygen, nitrogen, and sulphur.......... 7.18

------

Total non-combustible..................... 43.79

Carbon, being useful combustible................. 194.46

------

Total fuel................................ 238.25

Air per pound of carbon................................ 17-1/8 lb.

Time of experiment..................................... 4 h. 12 min.

Water evaporated from 60° into steam at 53 lb. pressure 1,620 lb.

Heat lost by radiation and convection.................. 70,430 units.

Mean temperature of chimney............................ 700° F.

" " " air................................ 70° F.

No combustible gas was found in the chimney.

Scientific American Supplement, No. 441, June 14, 1884. · 第 20 / 60 题