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476 TRANSACTIONS OF TH E A.S.M.E. AUGUST, 1941<br />
J. E. T o b e y . 1’ Ash has always been the chief mischief-maker<br />
in the burning of coal on both stokers and pulverizers. Troubles<br />
from the other properties of coal have gradually been solved.<br />
While splendid progress has been made with ash, this has been<br />
partially offset by new critical conditions arising from the increase<br />
in boiler pressures and temperatures. The authors have<br />
forged another great link in the chain of priceless contributions<br />
Mr. Bailey has made in the solution of combustion problems.<br />
As indicated in the paper, the major importance of iron in ash<br />
and slag must be recognized and provisions made to do more exhaustive<br />
research on the problem in both plant and laboratory.<br />
Recent work by Bailey and Nicholls on ash properties furnish an<br />
excellent springboard from which to launch a comprehensive research<br />
program. It is believed that the interested technical<br />
groups should immediately set in motion the necessary machinery<br />
to carry through such a program.<br />
A u t h o r s ’ C l o s u r e<br />
The authors wish to express their thanks for the several<br />
discussions offered on this paper and for thp active interest shown<br />
in further investigation of the behavior and influence of ash and<br />
slag. They acknowledge the many limitations in the data presented<br />
on a subject of such complexity and agree with Dr. Fieldner<br />
that, for ultimate solution, the problem must be resolved into<br />
its fundamentals. This will require the efforts of many investigators<br />
along different but coordinated lines.<br />
The work of the Bureau of Mines on slag viscosities with relation<br />
to the phase of tapping, and of Gould, Brunjes, and others,<br />
as cited10 by Mr. Julsrud, in regard to the effects of separable constituents<br />
of the ash at its source, are examples of great importance.<br />
In the meantime, much practical value may be gained<br />
from a more complete recognition of such over-all gross characteristics<br />
as can be determined from simple established tests, and from<br />
a study of their relation to conditions existing in the operating<br />
boiler furnace.<br />
Prof. Estep has brought out one point which we wish to clarify<br />
at once by stating that all of the authors’ slag samples, referred<br />
to in the paper, were taken from furnace or boiler heating surfaces<br />
and not from the thermal probe. A great many probe<br />
samples have of course been obtained, and have yielded data of<br />
rather special interest but, in the present discussion, the data are<br />
restricted to furnace or tube-bank samples. In procuring the<br />
samples, care was taken to prevent contamination, by using stainless-steel<br />
tools that were cooled intermittently by dipping them<br />
in water. The condition of these tools over extended periods of<br />
use indicates a negligible deterioration.<br />
Laboratory fusion tests were made with standard-cone specimens<br />
heated in a gas-fired muffle furnace. For the “reducing<br />
condition,” A.S.T.M. specifications were followed, by which a<br />
reducing atmosphere was maintained through the use of an excess<br />
of fuel gas, as evidenced by yellowish flame extending from the<br />
opening in the cover of the furnace for a distance of 6 to 7 in.<br />
The “oxidizing condition” was produced in the same furnace by<br />
using an excess of combustion air, controlled by means of orifices<br />
installed in the gas and air,lines supplying the burner. Orsat<br />
analyses of gases within the cone chamber have shown the<br />
following composition:<br />
C 02, o 2, CO,<br />
per cent per cent per cent<br />
Reducing condition........... 8 .2 to I 0 0 2 to 4.8<br />
Oxidizing condition........... 10.0 to 11 1.6 to 2.8 0<br />
The final state of oxidation of the fused-cone sample, as checked<br />
*• Vice-President in Charge of Engineering, Appalachian Coals,<br />
Inc., Cincinnati, Ohio. Mem. A.S.M.E.<br />
in one case, after being specially mounted on a platinum plaque,<br />
was found to be:<br />
Fusing temperatures<br />
Total Reducing Oxidizing<br />
Ferric iron atmos atmospercent<br />
(as Fe), phere, phere,<br />
age per cent deg F deg F<br />
2000 2380<br />
Original slag sample... 60.4 25.3 2110 2490<br />
2360 2610<br />
Fused in reducing atmosphere<br />
at 2360 F 4.6<br />
Fused in oxidizing atmosphere<br />
at 2610 F 73.0<br />
It is realized that some variation in test-furnace control, and<br />
its influence upon the final state of the sample, may add materially<br />
to the scattering of points in Figs. 5 and 6 of the paper, in addition<br />
to the effects of undetermined fluxes such as lime and magnesia,<br />
as mentioned by Mr. Nicholls. Dr. Fieldner’s suggestion of establishing<br />
an A.S.T.M. standardized procedure for tests in the<br />
oxidizing condition is appropriate and is greatly needed.<br />
The rather startling comparisons cited by Mr. Powell, in Table<br />
2 of his discussion, may find a partial explanation in the early investigations<br />
of Dr. Fieldner, reference (1), where atmospheres of<br />
CO and C 02 (and H2 and H20) were used in various proportions.<br />
Higher softening temperatures were observed for the 100 per<br />
cent CO or the 100 per cent C 02 atmospheres than for intermediate<br />
proportions of mixture, and this was attributed, respectively,<br />
to a predominance of metallic iron, ferric iron, and ferrous<br />
iron, as shown by final analysis of the samples.<br />
The comparison of Mr. Powell’s samples C and D, and of these<br />
with samples A and B is not at all clear, and it would be interesting<br />
to know the further composition of the ash, and whether these<br />
results are confirmed by duplicate test. It has been pointed out<br />
by Reid20 that extremely low concentrations of oxygen, in an<br />
otherwise neutral atmosphere of unpurified nitrogen are nearly<br />
as effective as air in oxidizing molten slag. It may be possible<br />
that sample C would be found as high in ferric percentage as<br />
sample D, but there is still no apparent explanation for their relation<br />
to samples A and B.<br />
By a somewhat opposite process, the softening temperatures of<br />
different ash samples, mentioned by Mr. Sherman, would tend to<br />
be similar to one another in spite of initially different ferric percentages,<br />
because of the reducing action of the test furnace when<br />
ran according to A.S.T.M. specifications.<br />
We are in complete agreement with Mr. Nicholls’ recommendation<br />
of using the term “ferric percentage” instead of the authors’<br />
“per cent oxidation,” for reasons which he mentions. This term<br />
becomes practical as an inverse index of the fluxing power, on the<br />
consideration that the content of metallic iron is usually negligible.<br />
We believe, however, that the expression for total iron content,<br />
and percentages of its oxide forms, is more readily grasped in<br />
terms of elemental Fe.<br />
In the determination of iron forms, it is important that analysis<br />
methods be developed for identifying all forms individually.<br />
Digesting in HC1, or in H2S04 and HF solutions has in some cases<br />
failed to dissolve more than 30 per cent of the total iron in the<br />
slag and, if the state of the undissolved portion is accepted, by<br />
difference, as being FesOs the resulting value of ferric percentage<br />
may be considerably misleading.<br />
In the paper, the presentation of data from laboratory work<br />
stressed the contrast between oxidizing and reducing atmospheres<br />
because that was the only controllable change in test procedure.<br />
It was not intended to imply that the atmosphere was the only<br />
20 “Control of Forms of Iron in the Determination of Fusion Temperatures<br />
of Coal Ash,” by W. T. Reid, Industrial and Engineering<br />
Chemistry, Analytical edition, vol. 7, 1935, pp. 335-338.