May 24, 1918. THE COLLIERY GUARDIAN. 1049 overtime was worked. Trade unions with 315,036 members (mostly in skilled occupations) reported 0'1 per cent, unemployed at the end of April, compared with 0’1 per cent, a month ago and 0T per cent, a year ago. Tinplate.—The number of tinplate mills working at the end of April showed an increase of 16 on a year ago. Difficulties in securing supplies of raw material were still reported. Wages.—In the four months, January-April, a net increase of £500 in wages was granted, affecting 21,500 workpeople connected with coal mining. The net increase in iron mining was £2,200 per week, affecting 8,000 persons, and in pig iron manufacturing £6,100, affecting 32,000 persons. Disputes.—Two new disputes occurred in April. One near Worksop affected 1,990 miners and others, and lasted for two days. It was settled by an agree- ment that post-war miners were not to re-enter the pits unless medically examined and passed into Grade 3. The other dispute (near Newport) affected 1,588 workpeople, relative to the alleged non-payment of war wage to certain men, and other grievances. Work was resumed pending negotiations. Fatalities.—In the four months the fatalities in mines totalled 582, compared with 427 in 1917. The mining fatalities (underground and surface) at mines in April numbered 106, an increase of two on the number in April 1917. RECOVERING AMMONIA AT TAR- DISTILLING PLANTS.* By C. R. Woodward. Although it has long been known to tar-distillers that a certain amount of ammonia is present in the water contained in ordinary coke-oven, gas-house or vertical retort tars, very little has been done in the way of experimenting to find the actual state in which the ammonia is present, its strength or the possibilities of recovery. The writer has spent considerable time working on this subject at the plant of a large tar distiller, and has obtained results showing that not only can ammonia be easily recovered, but that its recovery at these distilling plants can be accomplished very profitably. Sources of Ammonia. At the tar works there are two sources from which ammonia can be recovered—the liquor which settles out on the top of the crude tar storage tanks, and the liquor which conies over with the light oil in the process of distilling the tar. As the storage tanks are both filled and emptied from the bottom, this liquor, settling on top of the tanks, is commonly allowed to accumulate undisturbed until such time as the amount begins to take valuable storage space, when it is run to waste. The distilled liquor is by far the most profitable source, due to its great volume and strength; but, as is the case with the settled liquor, it has usually been allowed to run to waste. At the particular plant at which the experiments to be described were made, the coal tar received in the course of a year consisted of about 9,000,000 gals, coke- oven tar, 4,000,000 gals, gas-house tar and 600,000 gals, vertical-retort tar. About two-thirds of this tar was distilled at the plant, the remainder being disposed of in a crude state for road-building purposes, under trade names tending to disguise its true composition. Laboratory Tests. Before any large scale operations were attempted, laboratory tests for ammonia were made on the water settling on the top of the storage tanks and on the water distilled from the different kinds of tars in the laboratory. The results given are expressed in ounces of ammonia per gallon of liquor, and also in the per- centage of anhydrous ammonia, the percentage being obtained by dividing the number of ounces per gallon of liquor by 3'88. Tests of the liquor settling out from the tar in storage are given in Table I. Table I.—Liquors Settling on Tars. Tank No. and Volatile p- d Total Am- class of tar. ammonia. ea* ammonia, monia. Oz. No. 2 coke oven ..... 1*41 No. 3 gas-house ..... 0'705 No. 11 „ „ .... 0'82 No. 12 ,, „ .... 0'69 No. 22 vertical retort No w; Oz. P. cent. 4'39 ... ''80 ... 1'50 1'77 ... 2'48 ... 0'64 1'58 ... 2'40 ... 3'62 2’22 ... 2'81 ... 0'73 settled out. An examination of the liquor distilled in the labora- tory from each of the three different classes of tar, coke oven, vertical retort and gas house, showed an average strength as follows:— Table II.—Liquors Distilled from Tars. Strength ammonia from laboratory Total ammonia. Per cent. 2'52 3'12 0'73 2'19 Class of tar. sample. Oz. Coke oven................. 9'76 Coke oven plus NaOH...... 12’1 Gas-house................. 2'84 Vertical retort ............ 8’5 In the distillation of these tars the condenser was kept at all times absolutely cold, so that never was there any danger of ammonia loss. Under these conditions the strength of the liquor obtained represents the maxi- mum that can be recovered from these tars in practice. The second test with NaOH was made for the purpose of seeing if the fixed ammonia in the tar could be broken up in the process of distilling. Tbe results of the experiments on the settled liquor indicated that with the exception of that on the coke oven tar tbe strength in ammonia was very low. In fact, were it not possible to mix them with stronger liquors, recovery of the ammonia contained in them would not be practicable regardless of the volume avail- able. It should be noted that about 70 per cent, of the * Metallurgical and Chemical Engineering. ammonia in this liquor is fixed and would necessitate using lime in the process of concentrating. The water distilled from the tar, however, is found to be considerably stronger in ammonia than tbe water separated from the tar on standing, and suggests very profitable recovery. The great difference in the strength of these two classes of liquor is noticeable, particularly in the tests of the water from the coke oven tar, which contains 5'80 oz. ammonia in the settled liquor and 9'76 oz. in the distilled liquor. This is probably due to evapora- tion of ammonia from the surface of the water in the storage tanks. The fact that the tar itself contains some ammonium compounds, apart from those in the water with which it is intimately mixed, causes a cor- responding increase in the amount of ammonia in the distilled liquor. The reason why the water distilled from the coke oven tar contains 9'76 oz. of free ammonia while the water separating from tbe same tar on standing contains only 1'41 free ammonia, is that the distilled liquor contains only free ammonia, which passes over with the water, the fixed ammonia remaining behind. In the settled liquor the free ammonia has evaporated. The result of the test with caustic soda indicates that an additional amount of ammonia may be recovered through the breaking up of the fixed ammonia remain- ing in the tar. It was not, however, considered worth while to try out this test on a large scale in view of the difficulties likely to be encountered through the action of the caustic on the tar. Large-Scale Tests. Ammonia tests were made on water obtained from the distillation of tar on a large scale, 10,000 gals, direct- fired stills being used. In making road-building material and pitch it is customary at the plant in question to mix coke oven tar and gas house tar in about equal proportions. Most of tbe tests, therefore, were made on the water distilled from such mixtures. However, to make the experiment more complete, a special still of straight coke oven tar and a still of vertical retort tar were run to fuel pitch for the purpose of obtaining the liquor from these particular tars. The strength of the liquor only differs slightly from the tests obtained in the laboratory. The ailimonia was found to be approximately 99 per cent, free and 1 per cent, fixed, this small amount being probably due to combinations made with the gases in the condenser, or with salt water leaking through the condenser coils. Liquor Recovered in Practice. In order to ascertain if this ammonia liquor could actually be recovered without loss in practice, an 18-day test was run, during which time the liquor from all the stills, instead of being allowed to run to waste, was dumped into ground tanks and from there pumped into a storage tank holding about 5,700 gals. When full this tank was emptied, several samples being taken of the liquor as it ran from the bottom. In this test the liquor obtained was subject to some contamination from rain, water, and from salt water dripping from the con- densers, but the amount was not sufficient to affect the results materially. The average yield of ammonia was 4'17 oz. per gallon. The water was all taken from mixtures of gas-house and coke-oven tars, and it is evident that, if care is used to prevent evaporation, there is very little loss to be anticipated in recovering the ammonia. The average test of 4'17 oz. agrees very closely with the average strength of 4'11 oz. in the liquor as it is given off from the still, and before it is dumped into the ground tanks. The composition of the distilled liquor, containing, as it does, 99 per cent, of its ammonia in a free state, con- stitutes a most favourable condition for concentrating— no lime being required. From these experiments, it appears that tbe bulk of the liquor recovered at the stills when the usual tar products are being made will average 4'11 oz. strength—a liquor considered workable. To obtain a stronger liquor at the expense of the total ammonia recovered, it is only necessary to eliminate the last few tubs of weak liquor. A strong ammonia liquor will always be obtained when straight coke-oven and vertical-retort tars are distilled. Estimate of Profit. Records of the plant show that the total amount of water distilled from the tar in the course of the year averages about 700,000 gals. The water settling out of the coke-oven tar in the course of a year is 76,000 gals, and that on the gas-house tars 256,000 gals. Assuming all the ammonia concentrated to a liquor of 20 per cent, strength, which has at this time a value of about 0 lOdol. a lb. at the works, the total amount and value would be at this plant:— Liquor settling on coke-oven tar: 76,000 X 8'35 x 15 p.c. — 9,520 lb. ammonia Liquor settling on gas-house tar: 256,000 X 8'35 X 0'665p.c. =14,220 lb. ammonia Distilled from tar : • 700,000 x 8'35 x 1058 p.c. = 61,840 lb. ammonia Total ............... 85,580 lb. ammonia Total value of ammonia, 0’10 dol. X 85,580 = 8,558 dols. If any considerable amount of coke-oven tar or vertical-retort tar is distilled without admixture of gas- house tar, as is the case when ordinary fuel or briquette pitch is made, the amount of ammonia recovered will be greatly increased. The only extra apparatus required is an ammonia .concentrator for the weak liquor, a few small tanks and a little additional piping. Tbe cost of the concentrator, together with the tanks and including the labour of setting up, would be about 4,000 do^s. Tbe operating cost of concentrating the liquor per lb. of ammonia recovered is estimated at 2 c. per lb. The total value of the ammonia being approximately 8,558 dols., and the cost of recovering ] ,712 dols., a profit of approximately 6,746 dols. a year is indicated. It is stated that the Road Transport Board is about to take over the whole of the road transport of the country. The scheme arranges for a number of divisions of area. THE SAFE STORAGE OF COAL.* By W. D. Langtry and J. F. Kohout. The storage pile tends to equalise the variable demands for coal, especially for domestic consumption. During the summer months there is but little burned and many retailers start to stock for the winter. In the winter months the demand is heavy and these storage piles enable the dealers to make prompt deliveries. These remarks also apply, in a sense, to power fuel, as the generalisation may be made that the storage pile acts as a reservoir which may be drawn upon or left untouched as the needs and occasion demand. Broadly speaking, the larger sizes of coal store without giving any trouble. This is due principally to the fact that these sizes are drier and offer a smaller surface, in proportion to their mass, to the action of oxygen, than the finer sizes do. Anthracite and semi-bituminous coals store well in any size, but this is probably due to their chemical composition. Oxidation occurs here also, but is much slower in action and, therefore, smaller in amount for any given length of time. The finer sizes of coal, which are used pricipally for power purposes, are generally high in moisture and iron pyrites. These are deleterious ingredients because of the ease of oxidation of the pyrites in the presence of water vapour. The finer sizes, that is, coal passing through 2 in. screen and smaller, expose a great number of small surfaces to the air. These several factors all tend to initiate oxidation and to speed it along once it has started. The methods of storage are three in number: — under-water storage; storage in closed bins; and in open piles. Under water any kind and size of coal may be kept for any length of time without danger of any sort from fire. This method is used by very large consumers of coal, like the Western Electric Company, of Chicago, and the United States Navy Department. This provides a supply of coal which may be safely held for an indefinite period of time. All such concerns also hold coal in open piles for immediate use. Storage in closed bins is generally limited to small quantities of fuel. These may be the winter supplies in homes or stocks in small retail coal yards. Storing in Open Piles. The great bulk of storage coal is kept in open piles. This is intended to be held readily available for use and is seldom on the ground for more than a few months. As a matter of fact, it should not be kept for any great length of time, but the length of time should depend on the kind of coal, since this is the most dangerous form of storage. However, when proper precautions are taken at the time the coal is placed on the ground and maintained while the pile lasts, losses may be eliminated, or, at any rate, reduced to a minimum. These precautions will be taken up later, since from now on only the finer sizes will be considered. The losses which occur may be considered to be due to oxidation. In considering the mechanism of oxidation, the general fact should be borne in mind that the rate of oxidation increases with increase of temperature. Also we must remember that coal is a poor conductor of heat, so that any heat occurring or generated in the interior of the coal pile stays there. These two facts indicate that when oxidation starts, even though at a low temperature, it generates a small amount of heat; this heat is insulated from the outside air, and, being retained, tends to increase the rate of oxidation. Thus one action helps the other, and the oxidation proceeds at a constantly accelerated speed, the more easily oxidisable compounds or constituents being attacked first. Iron pyrites is oxidised in the presence of water to ferrous sulphate and sulphuric acid, according to the equation : —Iron pyrites + oxygen + water = iron sulphate + sulphuric acid -p heat. This reaction takes place with a considerable evolution of heat. It is true that the oxidation really goes farther with the evolution of still more heat, but, to consider this matter from a more conservative viewpoint, this additional heat, and also the heat due to the action of sulphuric acid on lime or alkalies present in the coal, or the heat generated by the dilution of the acid with water are not considered. It must be remembered that the water actually enters into chemical combination with the pyrites and oxygen, unless the water is present in sufficient amount to exclude the air. This is the condition that prevails in under-water storage, and is one of the reasons why that method is best. When coal is stored in the dry state, the equation for the oxidation of the pyrites given above is incomplete, since the moisture component is absent. When it is stored under water the equation is again incomplete, because the air is thus excluded and the oxygen component is absent. In other words, the oxidation in the dry state pro- ceeds very slowly, since the only moisture available is that in the coal and in the air. In dry coal the moisture is very low, so in dry storage one of the necessary constituents of the reaction is lacking to a relatively large extent. Spontaneous Heating. The heat due to the oxidation of pyrites, helped by that coming from external sources, if any, raises the temperature of the pile to the point where the carbon and hydrogen of the coal begin to be attacked. This action is aided by the fact that coal, particularly when freshly mined and when in a fine state of division, has a strong affinity for oxygen. The oxygen is absorbed much as water is taken up by a sponge. This may be considered as the first stage of oxidation. This supplies the oxygen needed for the oxidation of the pyrites, and then of the carbon and hydrogen. This action is not likely to occur until a temperature of about 250 degs. Fahr, is reached. The temperature of the coal is raised by these processes until it reaches * The Black Diamond.