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coal trade bulletin - Clpdigital.org

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28<br />

beat value for graphite carbon is decidedly lower<br />

than that for tbe amorphous form of that element,<br />

and it is probable that a part, at least, of the<br />

carbon in coke is graphite in character. The<br />

value, 13,(ISO B.t.u.. therefore, does not seem un­<br />

reasonably low.<br />

In recent literature there seems to be little which<br />

bears upon the subject of this investigation. One<br />

chemist, however, seems to have made some careful<br />

inquiries along much the same lines, but unfortunately<br />

1 have the account of bis work only in<br />

the form of the brie! summary which appeared in<br />

the Abstract Journal of the American Chemical<br />

Society.© The work is a thesis by Herman Sterit.<br />

entitled "Studies on the Chemical Comiiosition<br />

ancl Heat of Combustion of Cokes Prepared by<br />

Different Methods, and on tbe Determination of<br />

the Heat of Combustion of Coals by Calculation.:<br />

Streit's averages for beat of combustion of coke.<br />

For oven coke 14,310 B.t.u.<br />

For gas coke 14,400 B.t.u.<br />

For crucible coke make by the American<br />

method of analysis 14,580 B.t.u.<br />

These averages are close to the commonly ac­<br />

cepted value for carbon and much higher than tbe<br />

one derived above from Kentucky cokes. Indeed<br />

they seem too high.<br />

One of the author's conclusions is that, with<br />

few exceptions, due to abnormal composition, as<br />

high sulphur, the heat of combustion of cokes can<br />

be calculated within about 1 per cent, by multiplying<br />

the per cent, of combustible matter by tbe<br />

appropriate factor corresponding to these findings.<br />

Thus, for an analysis by the American method, the<br />

factor would be 145.S. Anoter conclusion is that<br />

the heat of combustion of the<br />

TOTAL COMBUSTIBLE .MATTEI!<br />

of coke obtained by tbe same method from<br />

different <strong>coal</strong>s is the same, but differs if different<br />

methods are employed. The author also concludes<br />

that the chemical comiiosition and hence the heat<br />

of combustion of the combustible matter of a <strong>coal</strong><br />

depends on the method of coking.<br />

A paper by H. Bunte, entitled "Notes on the Byproducts<br />

of the Gas Industry,"© an abstract of<br />

which was seen in (he Journal of the Society of<br />

Chemical Industry,© contains data of interest in<br />

this connection. The author reports the chem­<br />

ical analysis and heat of combustion of 12 gas<br />

cokes, mostly German.<br />

Laboratory determination of 12 gas cokes.<br />

Ultimate analysis combustible part of cokes:<br />

Carbon 94.18%<br />

Hydrogen 0.90<br />

Oxygen and nitrogen 3.77<br />

Sulphur 1.13<br />

99.98<br />

THE COAL TRADE BULLETIN.<br />

Proximate of analysis of original <strong>coal</strong>:<br />

Total combustible matter 89.11<br />

Water and ash 10.S9<br />

100.00<br />

Actual and theoretical determinations of<br />

heat values:<br />

B.t.u. per lb. of total combustible matter,<br />

from tbe calorimeter determinations<br />

i-i.ioi<br />

Calculated from the analysis by Dulong's<br />

method 14,006<br />

This value, also, is higher than that obtained<br />

from the Kentucky cokes, but tends to confirm it<br />

because gas cokes are presumably less thoroughly<br />

carbonized than are oven cokes and would be expected<br />

to have a somewhat higher heat of com­<br />

bustion on account of their containing more hy­<br />

drocarbons.<br />

Having decided upon a value for the heat of com­<br />

bustion of tbe combustible matter in coke, we<br />

may determine, by difference, what the heat of<br />

combustion of tbe volatile combustible matter in<br />

a <strong>coal</strong> should be, if we have<br />

THE PROXIMATE ANALYSIS<br />

of the <strong>coal</strong> and its heating value as determined<br />

by tbe calorimeter.<br />

In order to get the total combustible matter in<br />

applying this method, I have decided to subtract<br />

not only the ash and moisture but in addition a<br />

further lo tier cent, of the ash, which is an allow­<br />

ance made for the combined water contained in<br />

the ash constituents before heating.<br />

The ash of <strong>coal</strong>s is composed largely of clay and<br />

it is evident that this clay must have contained its<br />

proper amount of combined water before the <strong>coal</strong><br />

was burned. This water would be driven off with<br />

tbe volatile combustible matter and be counted<br />

with it in the analysis. Kaolin contains about<br />

13 per cent, of combined water, but as the ash<br />

is not all clay I have assumed 10 per cent, of the<br />

weight of the ash as approximately representing<br />

tlie original amount of water in combination.<br />

Accordingly, in tbe following calculations, onetenth<br />

of the ash has been, in each case, deducted<br />

from the amount of volatile combustible matter<br />

shown in the analysis of the <strong>coal</strong>. The percentage<br />

of fixed carbon multiplied by 136.8 gives the<br />

heat of combustion of the fixed carbon. This de­<br />

ducted from tbe heat of combustion of the original<br />

<strong>coal</strong> gives the heat of combustion of the volatile<br />

combustible matter, which, divided by the weight<br />

of that matter, corrected as already explained for<br />

combined water, gives the heat of combustion per<br />

pound of tbe volatile combustible matter.<br />

These calculations have been made upon the<br />

©"riicmic.nl Abstracts," Vol. _ (1908), p. 1040.<br />

©Herman Streit, Dissertation, 1'niv. Zurich. 1000, p.<br />

©J. fur Gasbelencht, 40, 1807. pp. 405-407<br />

©J. Soc. Chem. lnd., xvi (1897), pp. 661-662.

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