首页> 外国专利> Process and apparatus for the recovery of oils, bituminous matter, tar, and resin from bituminous shale, oil-bearing sands, bleaching earths, peat, brown coal, coal and wood

Process and apparatus for the recovery of oils, bituminous matter, tar, and resin from bituminous shale, oil-bearing sands, bleaching earths, peat, brown coal, coal and wood

机译:从沥青页岩,含油砂,漂白土,泥煤,褐煤,煤和木材中回收油,沥青质,焦油和树脂的方法和设备

摘要

198,705. Plauson's (Parent Co.), Ltd., (Plauson, H.). Dec. 2, 1921. Mineral oils, extracting and purifying.- Oils, bitumens and resins are obtained from shale, oil-bearing sands, bleaching earths, peat, lignite, coal, or wood, by effecting distillation of the materials in a current of steam or inert gas, such as carbon dioxide, moving at a high velocity of the order of 100 meters per second and upwards. The temperature is below the ordinary temperature of decomposition of the materials. A small quantity of solvent such as benzine, benzol &c. may be added to the steam or inert gas. The material, for example oil shale, may be passed down a vertical cylinder H, Fig. 1, from a feed device C to a discharge-worm G. Steam, which may be superheated to about 350‹ C. and under a pressure of 3-5 atmospheres, is fed through a ring-shaped device having nozzles F such as are used in steam turbines, and expands to form a stream moving at about 500 metres per second. Steam and entrained matters pass away through slits K protected by wire netting. The lower part of the cylinder H is surrounded by a cooling- jacket in which water is preheated for use as boiler feed. A horizontal cylinder through which the material is fed by a worm, may be used. Steam is supplied through a single nozzle near the outlet, and passes with the material from the outlet. In a complete installation shown in Fig. 3, steam, generated in a boiler 1 under a pressure of 15-20 atmospheres, is passed through a superheater 3 to an engine A from which it passes by a pipe 9 at a pressure of about 10 atmospheres. The steam is heated in a superheater 10 to 400- 500‹ C. and is expanded in a nozzle 11 to form a stream of high velocity which passes downwards through the shale &c. in a cylinder 13. Part of the oil separates in a space 14 and passes through a cooling-coil 16 to a collecting vessel 18. The steam and remaining vapours pass to a separator 21 through a nozzle 20 which causes a rotary motion of the gases, and to which reagents, for example a solution of a lead salt to remove sulphuretted hydrogen, may be supplied by a pipe 31. The oil &c. passes through a cooling-coil 16a to a vessel 18a. The steam passes by a pipe 23 and superheater 24 to a compressor B and thence again to the engine A. Bituminous coal yields a product containing montan wax and a petroleum jelly. In treating peat at 375-400‹ C., tar, oils, wax, methyl alcohol, acetic acid and acetone are obtained. In treating roots and resinous woods under vacuum at about 220‹ C. turpentine, resin, and a small amount of resin oil are obtained. The wood may be afterwards treated with steam at about 300-380‹ C. to yield methyl alcohol, acetic acid, acetone and tar oils.
机译:198,705。 Plauson's(Parent Co.),Ltd.(Plauson,H.)。 1921年12月2日,矿物油,提取和提纯。-油,沥青和树脂是从页岩,含油砂,漂白土,泥煤,褐煤,煤炭或木材中获得的,方法是在当前物流中进行蒸馏蒸汽或惰性气体(例如二氧化碳)以每秒约100米的速度向上移动。温度低于材料分解的常温。少量溶剂,例如汽油,苯甲酸酯和苯甲醚。可以添加到蒸汽或惰性气体中。材料,例如油页岩,可以从进料装置C向下流到图1所示的垂直圆筒H上,到达排出蜗杆G。蒸汽,在压力为250°C的条件下会过热至约350℃。 3-5个大气压被送入具有喷嘴F的环形装置中,例如在蒸汽轮机中使用的喷嘴,并膨胀形成以每秒约500米的速度运动的流。蒸汽和夹带物通过金属丝网保护的缝隙K逸出。气缸H的下部被冷却套包围,在冷却套中将水预热以用作锅炉给水。可以使用卧式圆柱体,蜗杆将物料输送通过卧式圆柱体。蒸汽通过出口附近的单个喷嘴供应,并与来自出口的物料一起通过。在图3中所示的完整设备中,在锅炉1中在15-20个大气压的压力下产生的蒸汽通过过热器3到达发动机A,该蒸汽通过压力为约10的管道9从中通过。气氛。蒸汽在过热器10中加热到400-500°C,并在喷嘴11中膨胀,形成高速流,该流向下穿过页岩&c。一部分油在空间14中分离,并通过冷却盘管16到达收集容器18。蒸汽和剩余蒸气通过喷嘴20进入分离器21,该分离器使气体旋转运动。可以通过管道31向其提供试剂,并且例如可以使用铅盐溶液去除硫磺化氢的试剂。通过冷却盘管16a到达容器18a。蒸汽通过管道23和过热器24到达压缩机B,然后再次到达发动机A。烟煤产生的产品含有褐煤蜡和凡士林。在375-400℃处理泥炭时,获得了焦油,油,蜡,甲醇,乙酸和丙酮。在约220℃的真空下处理根和树脂木材时,松节油可得到树脂和少量树脂油。然后可以在约300-380℃下用蒸汽处理木材,得到甲醇,乙酸,丙酮和焦油。

著录项

  • 公开/公告号GB198705A

    专利类型

  • 公开/公告日1923-01-04

    原文格式PDF

  • 申请/专利权人 HERMANN PLAUSON;

    申请/专利号GB19210032336

  • 发明设计人

    申请日1921-12-02

  • 分类号C10G1/02;C10G1/04;

  • 国家 GB

  • 入库时间 2022-08-24 11:46:53

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