December 1, 1916. THE COLLIERY GUARDIAN. 1059 the pre-heater. It has also been found that the same design is a good thing in a condenser. Gilled steam pipes should be avoided in the construction of pre- heaters, as they afford ready lodgment for solid matter deposited from the oil, which soon interferes greatly with their efficiency. Experiences in Distillation and Refining. The corrosion occurring on some benzol plants appears to be due chiefly to ammonia in various forms of com- bination, such as sulphide and chloride; the water in the wash oil containing (at Staveley) as much as 5-5 per cent, ammonia. An interesting but ominous occurrence is the undoubted occasional conversion of some of this ammonia to oxide of nitrogen, revealed by both smell and appearance at the water and benzol outlets of the separator. The distillation of the crude benzol, before washing, is effected by working two fractions, the first—the light oil—embracing all that comes over up to direct steam being required. The heavy oil which follows is col- lected until naphthalene makes its appearance at the outlet of the condenser. The residue is then run out into the usual cooling pans. A short time ago the manufacture of pure benzol was taken up at Staveley, a still designed for this purpose was put on order; but in the meantime, as the aniline plant was about ready for starting up, and, conse- quently, would be requiring supplies of pure benzol, an attempt was made to produce it with the plant already installed. The first trouble occurred with the washing process. The mixers -are of 4,000 gals, capacity, the usual charge being 3,600 to 3,800 gals. After the initial troubles at the starting up of the plant had been overcome, no further difficulty was experienced in the washing of the ordinary products. The mixers are fitted with inverted cone agitators, running at 60 to 80 revolutions per minute. The cones are set just low enough to ensure the acid being picked up from the bottom of the vessel. There is, consequently, with the full charge, a con- siderable depth of benzol—roughly, 4^ ft.—above the top of the cone; with the result that the agitation, though quite sufficient for the washing of the light and heavy oils, proved utterly inadequate for the much more drastic washing required in the preparation of pure benzol. It was found quite impossible to wash out the thiophene, even with the most liberal use of acid, except by working with a half-charge in the mixer, when the benzol just about covered the top of the cone. Working in this way, the agitation was all that could be desired, though even then prolonged washing was required to achieve .satisfactory results. The practice is to give two washes with d.o.v., the acid used being 3| per cent, by volume, and numerous experiments in the way of varying the amounts of acid used, and the time of agitation, have failed to bring this figure any lower. The distillation of the washed product, pending the erection of the new still, was carried out in one of the old plate column stills, which had only been designed for the production of ordinary 90’s. It was, however, thought possible that by working at a very slow rate, and with severe dephlegmation, a fairly pure benzol might be obtained. At the outset it was found that the column would only pass back a strictly limited amount of benzol without choking, and even with taking several days over the distillation of 3,800 gals., it proved impossible to obtain anything like a pure article, the best results being 44 per cent, of benzol, testing as follows :—Specific gravity at 60degs. Fahr., 0*884; drop, 79*4 degs. Cent.; 90 per cent, at 80-6degs. Cent.; 95 per cent, at 81-4degs. Cent.; dry point, 82-8 degs. Cent. The “ pure ” still, which has now been at work for some time, has the bell type of column, with the usual dephlegmator, and an analyser of the Coupler pattern. A series of tests has been made to determine the work done by this particular form of analyser, and the results are given below. In addition to the water it takes, which perhaps with many would be a small matter, the analyser has the drawback of causing a lot more steam to be required for distillation. Three charges Three charges with analyser. without analyser.* As charged. As charged. Drop, 79-6° C. Drop, 78*7° C. Dry point, 99*5° Dry point, 101° Distillate Gals. Gals. Total forerunnings... 960 ... 1,106 Pure benzol ....... 9,101 ... 8.718 To re-work ............ 516 ... 746 90*s toluol ........... 156 ... 195 Per cent pure benzol in total distillate... 84’75 ... 81T0 * The analyser con’d not be by-passed, but the term “ without” is justified, as the water was cut off and the siphons conveying the condensates back to the column were all blanked off, >o that anything condensing in the analyser was obliged to find its v\ay down the vapour pipe to the condenser. Note.—The dephlegmator, under both sets of conditions, was worked at the same temperature. The general experience at Staveley with perforated plates a