ON THE CALORIFIC POWER OF FUEL, AND ON THOMPSON'S CALORIMETER.

By J.W. THOMAS, F.C.S., F.I.C.

A simple experiment, capable of yielding results which shall be at least

comparative, has long been sought after by large consumers of coal and

artificial fuel abroad in order to ascertain the relative calorific

power possessed by each description, as it is well known that the

proportion of mineral matter and the chemical composition of coal differ

widely. The determination of the ash in coal is not a highly scientific

operation; hence it is not surprising that foreign merchants should

have become alive to the importance of estimating its quantity. While,

however, the nature and quantity of the ash can be determined without

much difficulty, the determination of the chemical composition of

coal entails considerable labor and skill; hence a method giving the

calorific power of any fuel in an exact and reliable manner by a simple

experiment is a great desideratum. This will become more obvious when

one takes into consideration the many qualities and variable characters

of the coals yielded by the South Wales and North of England coal

fields. Bituminous coals--giving some 65 per cent, of coke--are

preferred for some manufacturing purposes and in some markets.

Bituminous steam coals, yielding 75 per cent, of coke, are highly prized

in others. Semi-bituminous steam coals, yielding 80 to 83 per cent, of

coke, are most highly valued, and find the readiest sale abroad; and

anthracite steam coal (dry coals), giving from 85 to 88 per cent, of

coke (using the term "coke" as equivalent to the non-volatile portion of

the coal) is also exported in considerable quantity. Now the estimation

of the ash of any of these varieties of coal would afford no evidence

as to the class to which that coal belongs, and there is no simple test

that will give the calorific power of a coal, and at the same time

indicate the degree of bituminous or anthracitic character which it

possesses.

In order to obtain such information it is necessary that the percentage

of coke be determined together with the sulphur, ash, and water, and

these form data which at once show the nature of a fuel and give some

indication of its value. To ascertain the quantity of the sulphur, ash,

and water with accuracy involves more skill and aptitude than can

be bestowed by the non-professional public; the consequence is that

experiments entailing less time and precision, like those devised by

Berthier and Thompson, have been tried more or less extensively.

In France and Italy, Berthier's method--slightly modified in some

instances--has been long used. It is as follows:

70 grammes of oxide of lead (litharge) and 10 grammes of oxychloride of

lead are employed to afford oxygen for the combustion of 1 gramme of

fuel in a crucible. From the weight of the button of lead, and taking

8,080 units as the equivalent of carbon, the total heat-units of the

fuel is calculated. This experiment is very imperfect and erroneous upon

scientific grounds, since the hydrogen of the fuel is scarcely taken

into account at all. In the first place, hydrogen consumes only one

quarter as much oxygen as carbon, and, furthermore, two-ninths only of

the heating power of hydrogen is used as the multiplying number,

viz., 8,080, while the value of hydrogen is 34,462. In other words,

one-eighteenth only of the available hydrogen present in the fuel is

shown in the result obtained. Apart from this my experience of the

working of Berthier's method has been by no means satisfactory. There

is considerable difficulty in obtaining pure litharge, and it is almost

impossible to procure a crucible which does not exert a reducing action

upon the lead oxide. Some twelve months ago I went out to Italy to test

a large number of cargoes of coal with Thompson's calorimeter, and since

then this apparatus has superseded Berthier's process, and is likely to

come into more general use. Like Berthier's method, Thompson's apparatus

is not without its disadvantages, and the purpose of this paper is to

set these forth, as well as to suggest a uniform method of working by

means of which the great and irreconcilable differences in the results

obtained by some chemists might be overcome. It has already been

observed that a coal rich in hydrogen shows a low heating power by

Berthier's method, and it will become evident on further reflection that

the higher the percentage of carbon the greater will be the indicated

calorific power. In fact a good sample of anthracite will give higher

results than any other class of coal by Berthier's process. With

Thompson's calorimeter the reverse is the case, as the whole of the

heating power of the hydrogen is taken into account. In short, with

careful working, the more bituminous a coal is the more certain is it

that its full heating power shall be exerted and recorded, so far as the

apparatus is capable of indicating it; for when the result obtained is

multiplied by the equivalent of the latent heat of steam the product is

always below the theoretical heat units calculated from the chemical

composition of the coal by the acid of Favre and Silbermann's figures

for carbon and hydrogen. On the other hand, when the heating power of

coal low in hydrogen is determined by Thompson's calorimeter, much

difficulty is experienced in burning the carbon completely; hence a low

result is obtained. From a large number of experiments I have found that

when a coal does not yield more than 86 per cent, of coke, it gives its

full comparative heating power, but it is very questionable if equal

results will be worked out if the coke exceeds the above amount although

I have met with coals giving 87 per cent. of coke which were perfectly

manageable, though in other cases the coal did not burn completely. It

will be noted that the non-volatile residue of anthracite is never as

low as 86 per cent., and this, together with the very dry steam coals

and bastard anthracite (found over a not inextensive tract of the South

Wales Coal field), form a series of coals, alike difficult to burn in

Thompson's calorimeter. Considerable experience has shown that in no

single instance was the true comparative heating power of anthracite

or bastard anthracite indicated. With a view to accelerate the perfect

combustion of these coals, sugar, starch, bitumen, and bituminous

coals--substances rich in hydrogen--were employed, mixed in varying

proportions with the anthracitic coal, but without the anticipated

effect. Coke was also treated in a like manner. Without enlarging

further upon these futile trials--all carefully and repeatedly

verified--the results of my experiments and experience show that for

coals of an anthracitic character, yielding more than 87 per cent. of

coke, or for coke itself, Thompson's calorimeter is not suited as an

indicator of their comparative calorific power, for the simple reason

that some of the carbon is so graphitic in its nature that it will not

burn perfectly when mixed with nitrate and chlorate of potash. A sample

of very pure anthracite used in the experiments referred to, gave 90.4

per cent. of non-volatile residue, and only 0.84 per cent. of ash. This

coal was not difficult to experiment with, as combustion started with

comparative ease and proceeded quite rapidly enough, but in every

instance a portion of the carbon was unconsumed, and consequently

instead of about 13° of rise in temperature only 10° were recorded.

Since the calorific power of a coal is determined by the number of

degrees Fahrenheit which a given quantity of water is raised in

temperature by a known weight of fuel, it follows that every care should

be taken that the experiment be performed under similar atmospheric

conditions. The oscillation of barometric pressure does not appear to

affect the working, but the temperature of the room in which the

work was done, and especially that of the water, are most important

considerations. It has been observed by some who have used this

apparatus--and I have frequently noticed it myself--that the lower the

temperature of the water is under which the fuel is burnt the higher is

the result found. This has been explained on the assumption that the

colder the water used, the greater is the difference between the

temperature of the room and that of the water; hence it would be

expedient that in all cases when such experiments are made the same

difference of temperature between the air in the room and the water

employed should always exist. For example, if the temperature of the

room were 70°, and the water at 60°, then the same coal would give a

like result with the water at 40° and the room at 50°. This has been

regarded as the more evident, because the gases passing through

the water escape under favorable conditions of working at the same

temperature as the water, and are perfectly deprived of any heat in

excess of that possessed by the water. Under these circumstances it

would seem only reasonable that this assumption should be correct. It

was, however, found after a large number of experiments upon the same

sample of coal that this was not the case. 30 grammes of coal which

raises the temperature of the water 13.4°, when the water at starting

was 60° and the room at 70°, gives 13.7° rise of temperature with the

water at 40° and the room at 50°. Conversely, when the water is at 70°

and the room at 80°, a lower result is obtained. The explanation appears

to be this: The gas which escapes from the water was not in existence in

the gaseous form previous to the experiment, and the heat communicated

to the gas being a definite quantity it follows that the more the gas

is cooled the greater the proportion of chemical energy in the shape of

heat will be utilized and recorded as calorific power.

In order, therefore, to make the experiment more simple and workable

at all temperatures, a sample of coal was selected, which should be

perfectly manageable and readily consumed. Appended is an analysis of

the coal employed (from Ebbw Vale, Monmouthshire):

Composition per cent.

Carbon...............................88.33

Hydrogen............................. 5.08

Oxygen............................... 3.28

Nitrogen............................. 0.55

Sulphur.............................. 0.70

Ash.................................. 1.26

Water (moisture)..................... 0.80

-----

100.00

In the following experiments the standard temperature of the water was

taken as 60° F., and as the coal gave 13.4° of rise of temperature, 67°

F. was selected as the standard room temperature. The reason for this

room temperature is obvious, for, whatever heating effect the higher

temperature of the room may have upon the water in the cylinder during

the time occupied by the first half of the experiment, would be

compensated for by the loss sustained during the second half of the

experiment, when the temperature of the water exceeded that of the room.

The mean of numerous trials gave 13.4° F. rise of temperature, equal to

14.74 lb. of water per lb. of coal. When the water was at 50° and

the room at 57°, the mean of several experiments gave 13.5° rise of

temperature. When the water was 40° at starting and the room at 47°,

13.65° was the average rise of temperature. Trials were made at

intermediate temperatures, and the results always showed that higher

figures were recorded when the water was coldest. With a view of getting

uniformity in the results it was thought well to make experiments, in

order to find out what temperature the room should be at, so that this

coal might give the same result with the water at 50°, 40°, or at

intermediate temperatures. Without going much into detail, it was found

that when the temperature of the room was at 40° and that of the water

40°, and the experiment was rapidly and carefully performed, 13.4° rise

of temperature was given; but this result could be obtained without

special effort when the room was 42° and the water 40° at starting. It

is evident that the cooling effect of the air in the room upon the water

cylinder is very appreciable when the water has reached 13° above that

of the room. When the water was at 50° and the room at 55°, the coal

gave 13.4° rise with ease and certainty, and it would not be out of

place to remark here that with those coals which burn well in Thompson's

calorimeter, the results of several trials are remarkably uniform when

properly performed. With the water at 70° and the room at 80°, a like

result was worked out. Experiments at intermediate temperatures were

also carried out (see table in sequel). It is true that the whole

difference of temperature we are dealing with in making these

corrections is only 0.25, but 0.2 in the result, when multiplied by 537

to bring it into calories, as is done by the authorities in Italy, makes

more than 100 heat units--a serious difference when 5d. per ton fine is

attached to every 100 calories lower than the number guaranteed.

Taking the latent heat of steam as 537° C., and multiplying this number

by 14.74, the evaporative power of the coal used in these experiments,

its equivalent in calories is 7,915. From the analysis of this coal,

disregarding the nitrogen and deducting an equivalent of hydrogen

for the oxygen present, the _total heat units_ given by Favre and

Silbermann's figures for carbon (8,080) and hydrogen (34,462) will

be 8,746. It will be seen, therefore, that the calorific power, as

determined by Thompson's apparatus, gives a much lower result when

multiplied by 537 than the heat units calculated from the chemical

composition of the coal. When I used Thompson's apparatus in the

chemical laboratory at Turin to determine the evaporative power of

various cargoes of South Wales coal, it was agreed by mutual consent

that the temperature of the water at starting should be 39° F. (the

temperature at which the _heat unit_ was determined). The temperature

of the room was about 60°, but this varied, as the weather was somewhat

severe and changeable. Under these conditions, with the water at 39° and

room 60°, the coal which gives 14.74 lb. of water per lb. of coal,

will give as high as 15.88 lb. of water per lb. of coal. This result

multiplied by 537=8,496 calories, approaching much more nearly to the

theoretic value. This method of working is still practiced abroad, but

experience has shown that very widely differing results follow when

working in this manner, especially if the temperature of the room is

changeable, as it naturally is where ash determinations and other

chemical work is proceeding simultaneously. The time the experiment

lasts, taking the reading on a quickly rising thermometer and other

considerations, render the experiments anything but trustworthy when

0.2 of a degree makes a difference of more than 100 calories. In the

instructions supplied with Thompson's calorimeter nothing is said as to

the temperature of the room in which the experiment is performed, but

simply that the water shall be at 60° F. If, with the water at 60°, a

room were at 50°, as it often is in winter, a good coal would give 14

lb. of water per lb. of coal as the evaporative power; but if in summer,

the room were at 75° and the water at 60°, the same coal would give 15

lb. of water per lb. of coal. If further evidence were needed of the

effect of temperature consideration of the experiments already referred

to will show how necessary it is that some general rule shall be

adopted. Considerable stress is laid (in the instructions) upon the

quantity of oxygen mixture used being determined by rough experiments.

This I have found leads to erroneous conclusions unless a number of

experiments are tried in the calorimeter, as it often happens that the

quantity which appears to be best adapted is not that which yields a

trustworthy result. There are many samples of South Wales coal, 30

grains of which will require 10 parts of oxygen mixture in order to burn

completely, but since a little oxygen is lost in drying and grinding,

and few samples of chlorate are free from chloride, it is not safe to

use less than 11 parts of oxygen mixture, but this amount is sufficient

in _all_ cases, and never need be exceeded. I have made numerous

experiments with various coals (anthracite, steam, semi-bituminous, and

bituminous, including a specimen of the ten yard coal of Derbyshire),

and find that with 11 parts of chlorate and nitrate of potash, they are

all perfectly manageable and yield the best results. It is quite clear

that the excess of chlorate is decomposed in all instances, and the

latent heat of the oxygen evolved, but those coals which are best to

experiment with did not yield results that differed when the quantity of

oxygen mixture was reduced to nearly the limit required for combustion

of the coal. Under these circumstances, therefore, the constant use

of 11 parts of oxygen mixture--a suitable quantity for all coals

exported--would enable operators to obtain similar figures, and make the

test uniform in different hands.

The following is a brief outline of the method of procedure recommended:

Sample the coal until an average portion passes through a sieve having

64 meshes to the square inch. Take about 300 grains (20 grammes) of this

and run through a brass wire gauze having 4,600 meshes to the square

inch, taking care that the whole sample selected is thus treated. One

part of nitrate of potash and 3 parts of chlorate of potash (dry) are

separately ground in a mortar, and repeatedly sifted through another

wire gauze sieve, having 1,000 meshes to the square inch, in order that

the oxygen mixture shall _not_ be ground to an impalpable powder, as

this is very undesirable. It absorbs moisture rapidly, and interferes

with the regularity of the combustion when very fine. 330 grains of the

powder are weighed out (after drying), and intimately incorporated

with 30 grains of coal--better with a spatula than by rubbing in a

mortar--and then introduced into a copper cylinder (3½ inches long by ¾

inch wide, made from a copper tube), and pressed down in small portions

by a test-tube with such firmness as is required by the nature of the

coal, not tapped on the bottom, since the rougher portions of the oxygen

mixture rise to the surface. As the temperature of a room is almost

invariably much higher than the water supply, a little hot water is

added to that placed in the glass cylinder, until the difference of

temperature between the water and the room is about the mark indicated

in the following table:

Scientific American Supplement, No. 288, July 9, 1881 · 第 16 / 64 题