1080 THE COLLIERY GUARDIAN. June 8, 1917. CURRENT SCIENCE AND TECHNOLOGY. Estimation of Benzene and Toluene in Coal Gas. Mr. B. P. Rothkopf (Gas World) has been carrying out a series of tests with various oils to determine their relative capacity for benzol extraction, employing the apparatus illustrated, which can be constructed in the works, only requires glass apparatus of a kind that is generally available, and enables 100 cu. ft. of gas to be completely washed in less than 24 hours without necessitating attention after the test has once been started. 3Y In order to obtain a regular flow of oil, a three-litre aspirator A is employed, fitted with a '1 in. delivery pipe and stop cock, the oil dripping from the end of this pipe into the open top of the oil- inlet syphon to the scrubber. The top of the aspirator is closed with a perfectly fitting rubber stopper through which passes a narrow glass tube B open at both ends and reaching to within J in. of the bottom of the aspirator, so that the oil pressure on the delivery pipe remains constant as the level of the oil in the aspirator becomes lower. To regulate the rate of flow of the oil, a cork, fitted with a length of capillary glass tube of about 1 mm. diameter, is placed in the inner end of the s in. delivery tube G. The length of capillary tube required to give a delivery of about 100 c.c. per hour must be found experimentally for the oil used, as this varies according to the viscosity of the oil. This is done by fitting a piece of capillary tube of, say, 4 in. in length in the outlet tube and ascertaining the amount of oil delivered by this, the oil reservoir being as full as possible and the rate of delivery being measured as soon as air enters the bottle from the bottom of the tube B. The length of the capillary tube is then shortened or increased accoi ding as the rate is too slow or too fast, until a length is found with which the rate is not less than 100 c.c. per hour, or 10 c.c. in six minutes. To prevent the capillary tube becoming blocked, the oil used should always be strained before use to remove any solid particles. If this is done, t he flow of oil keeps constant without supervision. The most suitable form of scrubber for the purpose consists of a piece of 2 in. pipe 24 in. long, filled with J in. Raschig rings. (These may be made by culling off pieces of | in. metal pipe § in. long; or by cutting off J iii. lengths from a tube of metal obtained by bending thin sheet metal round a t in. pipe.) A scrubber of these dimensions and filled with these rings is capable of effecting the complete removal of the con- densable vapours from coal gas passing at the rate of 5 cu. ft. per hour, by the use of an oil flow of about 100 c.c. per hour, if creosote or green oil is employed as the absorbing oil. This figure applies to a gas contain- ing not more than 2 g Js. of crude benzol per ton of coal carbonised. With a richer gas the oil supply must be slightly increased or- the rate of flow of the gas decreased. To the bottom of the scrubber is fitted a 2 in. to J in. diminishing socket, in which a perforated plate D is placed prior to fixing. The plate should be about 1A in. diameter, and its function is to support the rings used as scrubber filling. A piece of tube is screwed into the side of the D socket, and bent upwards as shown, serving as the gas inlet (after the meter), and a syphon of “ m compo ” pipe is fixed into the end of the D socket to form the oil outlet. Before using the apparatus it is preferable to solder all joints at the bottom to render them oil-tight. The top of the 2 in. pipe is closed by a good cork, through which pass the inlet oil syphon G and the gas outlet pipe H, from which the scrubbed gas may be led direct to a burner, the appearance of the flame giving an approximate guide to the completeness with which the extraction is proceeding. The whole of the 2 in. pipe is filled with Rasehig rings, which are ponied in indiscriminately, so that they occupy irregular positions throughout the scrubbing space. The oil used may be creosote, green oil or gas oil. The oil should be previously distilled until a thermometer in the vapour registers 230 degs. 0., the residue being employed after good cooling and filtering off from naphthalene or other separated solid matter. Gas oil, if used, must be passed into the scrubber at the rate of about 140 c.c. per hour. In commencing a test the oil is first turned on, and when this drips from the end of the oil outlet syphon the gas is turned on. The gas is regulated to a rate of 5 cu. ft. per hour and passes through a governor and meter before entering the scrubber. At the conclusion of the test the gas is shut off and the oil allowed to flow for another hour. The gas passed is determined from the meter readings at the commencement and end of the test, the usual temperature and barometer observa- tions being made. If the test has to be carried out at a place where the temperature is high, the scrubber should be provided with a water jacket for cooling purposes. The resulting benzolised oil is distilled and the amounts of benzene, toluene, etc., ascertained in the usual manner. Effect of Burning Coal on Overlying Strata. According to the U.S. Geological Survey Press Bulletin No. 314, many coal beds in the great coal fields of the Western States have at some time taken fire and burned along their outcrops, baking and reddening the overlying strata so that they have become a kind of natural brick or terra-cotta. The fires were in places hot enough to fuse and recrystallise the overlying shale and sandstone so as to form natural slag. At some places this slag resembles true igneous rock ; at others it consists largely of rare minerals. Thoroughly fused slag seems to occur chiefly in crevices or chimneys through which the hot gases generated in the burning escaped through the overlying strata to the surface. The chimney-shaped masses of slag are harder than the surrounding baked rock and, after that has weathered away, form the curious pinnacles that surmount many clinker bluffs or buttes in the west. Some of the coal beds, especially those exposed on the higher hills, were perhaps ignited by lightning; others, according to well-authenticated reports, were ignited by prairie fires or camp fires; but as burning on the outcrop has been so common as to affect most of the coal beds in an area of more than 200,000 square miles, much of it has probably been due to spontaneous combustion. Coal beds are now burning at or near the surface at many places in the west, where the burning of the bed is disclosed by the smoke and fumes that rise from it and by the heat at the surface of the earth near the outcrop or above the bed—heat so intense that it kills all vegetation. As the coal burns out, the overlying rock or earth generally caves in so as to form large fissures in the ground. As the burning works back from the outcrop, the heat acts on the overlying rocks, but finally combustion is smothered for the lack of oxygen. It is difficult to say how far back from the outcrop the burning may extend. Field studies made by the United States Geological Survey, Department of the Interior, indicate that a bed lying beneath 20 ft. or less of cover may burn out completely under large areas, and even where the cover is several hundred feet thick the burning may extend 500 ft. back from the outcrop. A brief account by G. S. Rogers of the burning of coal beds in place, with a discussion of the causes and a petrologic and chemical description of some of the baked and fused rock formed, has also been published by the United States Geological Survey as Professional Paper 108—A. Zirconia Crucibles. The possibilities of zirconia as refractory material have been much urged of late, and expei imenting with zirconia is going on in various quarters. The account of the recent continued work of Prof. O. Ruff and his collaborators at Danzig (Zeitsehrift fur anorganische Chemie, abstracted in Engineering) is encouraging. The new crucibles made of zirconia, with small additions of other oxides, could be r temperatures of 2,200 and even 2,400 degs. Cent. But there are difficulties caused by the affinity of zirconia for carbon and by other factors, and the temperature at which the zirconia bad been baked proved to be a factor of con- siderable influence. In their new researches, Ruff and G. Lauschke had at disposal a crude zirconia (83 5 per cent, of Zr2O3, 11'5 SiO2, 4’6 Fe2O3) and a purified zirconia (98’75 Zr„O3. 0'95 SiO2, 0’27 Fe2O3). Various samples of the latter had been baked at five tempera- tures, ranging from 750 to 1,400 degs. Cent., and these samples, ranging in density from 5’7 down to 4’99, were kept separate during the expei iments. Small cylinders were prepared by mixing the zirconia with water (9 or 10 per cent.), and sometimes also with 1 per cent, starch. Melting-pointde’.erminationsof the materials were made in the Ruff vacuum electric carbon tube furnace, at pressures from 5 mm. of mercury upward, sometimes in a hydrogen atmosphere. The following temperatures indicate visible melting of the cylinders:—Zirconia, 2,563 degs. Cent —this point was the same for all the samples, also in hydrogen at low pressures, a high hydrogen pressure lowered the melting-point; silica, SiO2, 1,850 (fused to a white bead); glucina (beryllium oxide BeO), 2,410 (no vapours ; this point is lower- than that previously found by Ruff) ; magnesia could not be melted, it evaporated completely when heated above 2,000 to 2,690 degs.; A1.2O3, 2,005 to 2,008 (very little vapour); thoria, ThO.2 gave white mists above 2,400, but was not melted at 2,780 (formerly melted at 2,425 or 2,470); yttria, Y2O3, 2,410 (vapours above 2,350) degs. The addition of any of these oxides to zirconia lowered the melting-point, but raised it in the case of ThO2 and Y2O3. Crucibles were then made of zirconia, to which 1, 3, or 6 per cent, of the other oxides were added, the mixture containing also water and starch, as stated. The crucibles were straight cylinders, 45 or 30 mm. high, 28 or 15 mm. external diameter, and 3 or 1’5 mm. wall thickness. They were baked in a Hessian crucible, and then heated in the electric furnace for 70 minutes up to 2,400 degs. maximum. In strength the soft and baked zirconia crucibles resembled clay. To reduce the formation of carbide, the crucibles were placed within covered crucibles of crude zirconia, which suffered in their turn; some oxides, volatilised from the outer crucible, then condensed on the inner. During the baking the crucibles altered their shape slightly ; they became coloured (yellow, green, reddish, blue, grey. sometimes mottled), turned crystalline, increased in strength (especially if previously baked at low temperature), and lost up to 20 per cent, in weight (moisture, chemical reduction, volatilisation), but. on the other hand, gained in weight by the condensation aforesaid. There was also shrinkage, and the porosity increased, owing to the volatilisation, especially of the added oxides. The porosity was determined by evacuating the pores and then letting water soak into them ; the deduced porosities, 4 to 39 per cent., were probably too high. This treatment was followed by heating the crucibles in the oxidising blowpipe flame, when the colour turned yellow-red (iron oxide). Many of the crucibles crumbled in this flame, because the carbides and lower oxides formed in the reducing atmosphere of the carbon furnace weie reoxidised; those baked at 2,000 degs. stood the oxidation better than those baked at 2,400, and the crucibles containing 6 per cent, of alumina proved strongest. The surviving crucibles were finally heated to the highest tempera- tures in the electric furnace and then analysed. The conclusion is that the addition of oxides to be made sho/uld depend upon the temperature at which the zirfconia is to be baked: if at 2,000 degs. add 1 per cent, of alumina; if at 2,200,1 percent, of thoria; if at2,400, 1 to 3 per cent, of yttria. Higher percentages would only increase the porosity; glucina, magnesia and silica are not recommendable, as too volatile or for other reasons. been modified. This tube A is I "WAI i-:,’ dflr • ■■ A/ - t vZr*' s' THE DAVIS-BRIGGS OXYMETER LAMP. Messrs. John Davis and Son (Derby) Limited, have afforded us the opportunity of examining one of the latest models of the Oxymeter safety lamp, of which they are the sole makers. Dr. Henry Briggs, of Edin- burgh. the inventor, described the lamp at length before the Mining Institute of Scotland (see Colliery Guardian, February 25, 1916, p. 359) ; but since writing that paper, Dr. Briggs has made further improvements that are embodied in the lamp now under consideration, which has been tested at Eskmeals, and “ recommended for approval.” Dr. Briggs’ purpose is to put in the bands of the mine official a safety lamp which will enable him to test, with sufficient accuracy for ordinary purposes, for both firedamp and oxygen—the former by the “ blue cap ” method (improved, if preferred, by the use of the well-known Briggs loop), and the latter by the special lamp-fitting described below. So far as we are aware, the Oxymeter lamp is the only contrivance—short of fragile gas analysis apparatus—which permits of mine ail’ being tested for both these gases ; and, with this lamp, the deputy or the fireman will, for the first time, be able to make sure that the air complies as to purity with all the ventilation standards prescribed in the Coal Mines Act. The accompanying illustration shows the latest and most practical form of the device adapted to the A.H.G. lamp. It will be observed that one of the four upright inlet tubes cut off 1A in. above the lamp base, and is given an exter- nal screw thread, on which travels a hollow screw- thimble B. A solid rod C, of a diameter slightly less than the bore of A, is fitted so that its lower extremity (which is pointed) is at the same level as the top of A. The other three inlet tubes. are stopped at their upper ends, but one has a side opening D. Nor- mally, the lamp takes its air supply partly through D and partly down A, the thimbletlien being at the bottom of its run so as to impede the air stream as little as possible. When it is de- sired to test for oxygen or blackdamp, the operator coiers the hole D with his thumb, after reducing the flame to about half working size. He then turns the thimble to make it advance up the screw. This has the effect of lengthening the inlet passage, and increasing the friction impeding the ingoing air. In due course, all white light disappears from the flame. The thimble is now turned more slowly until quivering is noticed in the flame, whereupon the hole D is at once uncovered. The flame revives, and after it has been raised to normal height, the position of the thimble is read against the scale on the brass strip E, both sides of which are graduated. The reading gives the percentage of oxygen present, the graduationslanging from.16 to 21. In the lamp illustrated, the top of the milled portion of the thimble serves as a reading index. A recent improvement consists in providing a scale of blackdamp percentages under the oxi gen scale; and now the top of the thimble reads off the oxygen figure, and the bottom of the thimble the equivalent blackdamp pro- portion. As some misapprehension still exists, it is as well to note that by “ blackdamp ” is meant nitrogen plus carbon dioxide, and not merely the latter gas. The “ blackdamp ” here referred to is the whole of the ex- tinctive gas. or mixture of gaces, polluting the air. In British coal mines that mixture invariably contains considerably more nitrogen than carbon dioxide. Another point woithy of remark is that the lamp automatically takes into account the watery vapour always present to a considerable amount in mine air. This vapour occupies a definite volumetric proportion depending on temperature and degree of saturation, and Dr. Briggs holds that it is as incorrect to neglect it (as is done in ordinary analysis) as to disregard the presence of any other constituent of the air. The lamp, in other words, gives the oxygen percentage actually existing, and not that which would exist had the air been dry. Humidity has an important influence on a flame, especially with hot saturated air. So marked does this influence become that, if the lamp is intended to be used in an underground district whose temperature exceeds 70 degs. Fahr., it is advisable to have the scale calibrated accordingly. The scale as ordinarily supplied is sufficiently exact for practical purposes for temperatures up to 70 degs. Firedamp, if present in such an amount as to make a visible cap on the lowered flame, causes the oxygen