436 THE COLLIERY GUARDIAN... ________________________________________________________________________________ March 2, 1917. CURRENT SCIENCE Benzol Recovery from Coal Gas. In a paper before the Midland Junior Gas Association ? Mr. T. F. E. Rhead discussed from the physico-chemical standpoint the problem of the extraction of crude benzol from coal gas, using creosote oil as a washing medium, and formulated the following practical conclu- sions :—The efficiency of washing is greatly improved by using a cold oil—say, 15 degs. C.—providing the creosote keeps sufficiently fluid. The lighter oils in creosote— 180 degs. to 220 degs.—help the washing process by lessening the viscosity of the creosote, but are objection- able in that they are readily distilled out by steam and contaminate the crude benzol. Naphthalene helps to lessen the viscosity, and thereby helps the washing; but it is very objectionable in that it prevents good extraction of naphthalene from the gas, and may even add some to the gas under certain con litions of quantity and temperature. Creosote fractions boiling above 300 degs. greatly increase the viscosity, and are very objectionable if present to any extent. A good creosote should remain as fluid as possible at 10 degs. to 15 degs., give little oil distillate when steam distilled, and have as low naphthalene content as possible. Greatly improved cooling of debenzolised oil from the crude still is obtained by using a creosote of which the viscosity rises very little when cooled to 10 degs. to 15 degs., and better temperatures are obtained for benzolised oil entering the crude still. The efficiency of washing is greatly improved by increasing the intimacy of contact between the oil and gas. Washers on the spraying or atomising principle appear to offer the best field for development in this direction—namely, an increase of surface per volume of washer and minimum back pressure. When using mixtures of blastfurnace and coal tar creosotes specific gravity is no criterion as to whether a creosote is “ spent ” or not, and its magnitude. Viscosity is the best test, and should be between 8 to 9, with a maximum of 10 (rape oil = 100). A sufficient quantity of creosote should be in circulation to prevent the light oils taken out and contained in the crude benzol in stock leaving a creosote of high viscosity. If light oils are sold with crude benzol, then either the creosote must be changed more frequently or the equivalent quantity of similar light oils added to take the place of those in the crude benzol. Gas and Potash from Cement Kilns. At the Hagerstown works of the Security Cement and Lime Company a Cottrell plant was installed last year for the recovery of potash from the kiln gases by the aid of high-tension current at 70,000 volts. The power supply (Engineering News) is three-phase current at 440 volts and 60 cycles, and the electrical equipment consists of four I5-borse power, 10 k.v.a., 220 volt single phase 60-cycle 1,800 revolutions per minute motor generator sets, each directly connected to the shaft of a rotary rectifier, and four 220 to 70,000 volt 60-cycle 10 k.v.a. transformers of special construction. The volume* of gas handled is approximately 180,000 cu. ft. a minute at a temperature of 900 degs. Fahr., and with two kilns 7 ft. by 100 ft. and three 8 ft. by 125 ft. the production of potash dust averages from 20 to 25 tons a day of 24 hours. The dust contains from 5 to 10 per cent, of potash in the form of potassium sulphate, and being in a very finely divided state, is highly suitable for fertilising purposes. It is noteworthy that the potash plant has been the means indirectly of increasing the production of cement clinker and also the fuel economy. It has brought about more continuous operation of the kilns, because it has required better attention on the part of the kiln operators, and this automatically makes the clinker of more constant quality. It is found also that the best recovery of potash is coincident with the best burned clinker. Oil Washing for Benzene and Toluene. Mr. W. G. Adam (Gas World) reports the result of experiments undertaken to ascertain the effect of oil washing on the illuminating power and calorific value, in addition to the sulphur and naphthalene content of the gas. The work was commenced with a rotary scrubber dealing with about 30 cu. ft. of gas per hour, in which was determined the relative efficiencies of various wash oils. The results obtained were confirmed on a plant dealing with 100,000 cu. ft. daily, in which a number of washing, fluids were used and the effects on the gas recorded. W ith regard to the effect of oil washing on quality of gas, the author states that while the removal of benzol from the gas effects a reduction of about 50 per cent, in the illuminating power, the calorific value is only affected to about 5 per cent. The sulphur content of clean gas consists of thiophene, carbon bisulphide, carbon oxy sulphide and mercaptans, and it is possible to remove all these except the carbon oxysulphide by means of oil washing, and the gas would then test about 10 grains of ■ sulphur per 100 cu. ft. Thorough washing of the gas with oil will remove all but the last one or two grains of naphthalene, and the vaporising (not spraying) of paraffin into the gas in sufficient quantity is an efficient preventive of the deposition of naphthalene from oil-washed gas. The best wash oil is one which is of the maximum boiling point, consistent with sufficient fluidity at ordinary temperatures, treating 100,000 cu. ft. of gas per day, in which the following materials were used as the washing medium: Fluid creosote (containing 8 to 25 per cent, tar acids), cresylic acid and heavy pyridine AND TECHNOLOGY. bases. All gave very similar results both as to quantity of benzol, etc., absorbed and the quality of crude spirit obtained. Various tars were experimented with, but were all found to give low absorption of benzol, etc., and it was determined that to secure efficient extraction a very much larger quantity of tar bad to be used than was produced per ton of coal. A consideration of the conditions prevailing on coke ovens predetermined this point. Coke oven gas frequently contains tar fog. and this is completely absorbed by the oil in the scrubber. The repeated steam distillation of the oil gradually carries away the creosote, leaving behind the tar. The result is that after a time the oil becomes tar, is said to be “ fatigued,” and has to be renewed. A green oil was found to give absorption up t_> 6 and 7 per cent., a crude spirit containing frequently as low as 5 per cent, of heavy oil and a low naphthalene content of the gas. It, was thus found possible to obtain high efficiency in the absorption, less oil having to be circulated. This resulted in an increased capacity of the scrubber, heating, cooling and distilling plant, and economies in both steam and cooling water. The crude spirit contained no tar acids, and thus required no soda wash prior to rectification. A low heavy oil content of the spirit gave economy of acid in the C.O.V. wash, amounting usually to a.50 per cent, saving. With the use of green oil and complete stripping of the gas it was found possible to keep the naphthalene at 4 grains per 100 cu. ft, and interesting results in the distribu- tion of the gas were obtained. It was found that after the old deposits of naphthalene in the mains were removed no stoppages, even in the smallest services, were experienced. The oil washing of coke oven gas is usually carried out in the presence of ammonia, sulphuretted hydrogen and other impurities. In this condition the gas and the wash oil have an energetic action on steel and wrought iron. For this reason the plant has to be made almost entirely of cast iron. This action is possibly influenced by the presence of cyanogen. No corrosion of wrought iron or steel is experienced when clean gas only is scrubbed. __________________________ THE CONTROL OF MINES. The executive of the Miners’ Federation held a meeting, on Tuesday, in London to consider the position of the workmen under the Control Order. It was agreed that in existing conditions the present wages must be continued, that further rises in the cost of living must be followed by corresponding increases in the wage rate, and that the present standard of living of those employed in the coal mining industry must be maintained. After the meeting, one of the men’s leaders stated that the Government, by taking control of the industry, destroyed the economic basis by which wages are fixed. The present wage must be maintained intact, and further rises in the cost of living must be followed by further rises in wages. With high prices, the present wages are only an existence for the workmen. The executive of the Miners’ Federation of Great Britain had an interview on Tuesday with the President of the Board of Trade with a view to .ascertaining tLe position of miners under the Government scheme of control, both as regards their working conditions as trade unionists and on the question of wages. The council also desired to make clear the attitude of the workmen on the question of wages, rise in food prices, and the standard of living. The interview with Sir Albert Stanley, who was accompanied by Mr. Guy Calthrop and Sir Richard Redmayne, lasted about an hour and a-half. The position was discussed by the men’s representatives with complete freedom. Sir Albert Stanley’s reply was sympathetic. It was stated that an Advisory Com- mittee of 10 representatives—five coal owners and five workmen—would be appointed to act with the Coal Controller. The workmen’s representatives have already been chosen—Messrs. Robert Smillie (Scotland), Vernon Hartshorn (South Wales), W. Straker (Northumber- land), H. Smith (Yorkshire) and Stephen Walsh, M.P. Following the interview at the Board of Trade the miners’ executive met at the Imperial Hotel, under the, presidency of Mr. R. , Smillie, and approved of the appointment of the workmen’s representatives. At a meeting of the Coal Conciliation Board on Wednesday the following resolution was adopted :— The owners have considered the application made by the workmen's representatives at a meeting held on the 31st of January, viz. .- — That having regard to the increased cost of living, the existing war bonus be increased from 13'8 to 18’8 per cent., and are willing on this ground, and this ground only, to agree to increase the existing war bonus from 13’8 to 18 per cent., subject to clause 3 of the conditions agreed to on the 24th of May, 1915, and to the further condition that no general application for any further increase, either as bonus or otherwise, be made by the workmen’s representatives throughout the area within the period ending August 31, 1917, and which is accepted by the workmen's repre- sentatives. The increase to accrue from Monday the 19th inst. at those collieries where that is the first working day in the pay week, and where the first working day in the pay week is after the 19th, then the increase to accrue from such day. Whatever arrears are due are to be paid with the week’s pay at the pay date of the week ending 10th March. The increase of 4’2 per cent, means an addition varying from 3d. per day to boys to 6d. per day to coal hewers and higher paid grades of workmen. As the number of workmen employed at the pits of the Federated area is 350,000, this is approximately an increase of £40,000 in the weekly wages bill. ______________ COAL TRAFFIC ON RAILWAYS AkD CANALS IN 1915* The following table shows the coal and coke carried by the various systems of railway, canal, and other inland navigation companies from colliery districts in the United Kingdom in 1915 and 1914 1914. Railways, England ai d Wales Tons. Furness (coal) ............ ............... 153,265 Great Cent'al (coal and coke) ... 13,583,303 Great Northern (coal) ........ ... 7,947,661 Great Western (coal and coke)... 20,521,077 Hull and Barnsley (coal and coke) 2,110,7531 Lancashire and Yorkshire (coal and coke) ................... 8,526,551 London and North-Western (coal) 21,351,2 '4 Maryport and Carlisle (coal and coke) ....................... 330,611 Midland (coal and coke, excepting gas coke) ................... 26,593,971 North-Eastern (coal and coke)... 37,435,639 North Staffordshire (coal and coke) ....................... 3,596,447 South Yorkshire Joint Line Committee (coal and coke)... 831,181 Taff Vale (coal and coke)....... 14,872,879 Railways, Scotland: — Caledonian (coal and coke) ..... 11,989,693 Glasgow and South - Western (coal) ....................... 3,465,686 North British (coal and coke) ... 17,540,201J 1915. Tons. 138,053 ... 13 913,038 ... 8,524,741 ... 21,346,650 ... 1,812,781f ... 8,811,114 ... 20,812,417 339,032 ... 27,477,018 ... 34,413,617 ... 3,374,650 918,735 ... 14,010,930 ... 11,130,211 ... 3,267,430 ... 17,374,699§ 7,034 7,765 Railways, Ireland:— Cavan and Leitrim (coal) ..... 7,282 Great Southern and Western (coal) ...................... 5,743 Canals, England: — Aire and Calder Navigation (coal and coke) ............................. Birmingham Canal Navigations (coal and coke).............. Bridge water Canals (coal, in- cluding a small quantity of coke) ...................... Leeds and Liverpool Canal Com- pany (coal, including a small ■ quantity of coke) ___ ........ Shropshire Union Canal (coal and coke) .................. . Staffordshire and Worcester- shire Canal (coal and coke) ... Trent and Mersey Navigation (coal and coke).............. Canals, Scotland:— Forth and Clyde Canal (coal and coke) ...................... Monkland Canal (coal and coke) Union Canal (coal and coke)... Canal, Ireland:— Grand Canal (coal)............ 2,064,732 ... 1.920,309 3,448,554 ... 3,528,086 375,304 ... 360,733 751,732 ... 765,000|| 16,610 ... 16,218 165,190 ... 162,204 180,912 ... 173,336 116,038 ... 136,345 60,309 ... 57,950 16,908 ... 15,306 Nil ... 161 f Including patent fuel. I 1,823,231 tons of this quantity were conveyed to Burntisland Dock and 2,456,375 tons to Methil Docks for shipment. § 1,211,578 tons of this quantity were conveyed to Burntisland Dock and 1,745,26 i tons to Methil Docks for shipment. || Approximate. * From Part II. of the General Report on Mines and Quarries in 1915, edited by Sir Richard Redmayne, H.M. Chief Inspector of Mines. _________________________________________________ LETTERS TO THE EDITORS. ____________________________________________________ The Editors are not responsible either for the statements made, or the opinions expressed by correspondents. All communications must be authenticated by the name and address of the sender, whether for publication or not. No notice can be taken of anonymous communications. As replies to questions are only given by way of published answers to correspondents, and not by letter, stamped addressed envelopes are not required to be sent. VEMTILATIOM. Sirs,—Will you allow me a short space in your paper to reply to the letter of “ Ventilation.” It would certainly have been much better had he given more details of the sizes of his shafts and the size of the proposed new shaft. However, the difficulty he refers to can easily be got over, and if “ Ventilation ” cares to write me direct and send on the particulars referred to above, I will give him the full benefit of my experience on this subject, which appears to me similar to that I have already gone through. I have a case in mind where increasing the area from 36 ft. to 72 ft. had the desired effect on the ventilation. William Leebetter. Us worth Colliery, co. Durham. February 26, 1917. ____________________________ Coal Trade Benevolent Association.—The annual meeting of the association was held on Monday in the Coal Mer- chants’ Society room of the London Coal. Exchange. Mr. Ernest Oliver presided. The directors’ report and balance- sheet showed net receipts £7,017, and relief grants £3,451. Mr. Joseph Shaw, K.C., was elected chairman for the ensuing year, and Mr. H. Cecil Rickett was elected one of the trustees, in the place of the late Mr. John Lea Smith. A bequest of £1,000 was reported from the executors of the late Mr. F. D. Lambert, and further bequests of £500 each from the late Mr. F. W. Harris and the late Mr. G. Alder