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Improved process for the treatment of solid carbonaceous substances, mineral oils and heavy hydrocarbons by heat and high pressure with or without hydrogen

机译:改进的方法,可以在有或没有氢气的情况下通过加热和高压处理固体碳质物质,矿物油和重烃

摘要

192,850. Bergius, F., and L÷ffler, S. Nov. 30, 1921. Mineral oils, extracting, purifying, etc.-In preparing light hydrocarbons by heating mineral oils or heavy hydrocarbons, which may be mixed with coal, brown coal, lignite, turf &c. under a pressure of about 100 atmospheres with or without hydrogen, as described in Specifications 25510/13. 4574/14, and 18232/14, [Class 32, Distilling &c.], the materials are heated to about the reaction temperature before being introduced into the reaction chamber. The reaction chamber 1, which may be made with thin walls is heated by hot gases, such as carbon dioxide, circulating in a jacket 2 under a pressure about equal to that used in the reaction chamber. The gas is circulated by a pump 3 through a heater 4. A slight difference of pressure, shown by a water column 7, is maintained between the reaction chamber and the jacket. Liquid materials from a tank 24 are forced by a pump 25 into a mixing-chamber 21 supplied with solid materials from a tank 22. The mixture is forced by a pump 35, supplied with liquid from a tank 31, through a pipe 17, in which it is heated by a jacket of hot gases circulated by a pump 20 through a heater 19. Hydrogen may be supplied from a container 12 through a heater 13. The product from the reaction chamber is passed through a cooler 36 before passing through a valve 37 by which the speed of discharge is controlled. Heavy mineral oils which tend to form pitch may be mixed with inert solid substances, such as diatomite, coke powder, coal ashes, &c., or with sulphur-binding reagents, such as diatomite or bog iron ore impregnated with alkali, before passing into the reaction chamber. The product obtained by the treatment may be mixed with a further quantity of coal &c. and again passed through the reaction chamber.
机译:192,850。 Bergius,F。和L÷ffler,S.,1921年11月30日。矿物油,提取,提纯等-在加热矿物油或重烃的过程中制备轻烃,这些轻烃可能与煤,褐煤混合,褐煤草皮如规格25510/13中所述,在约100个大气压的压力下,有或没有氢。在第4574/14号和第18232/14号,[Class 32,蒸馏等]中,将物料加热到大约反应温度,然后将其引入反应室。可以由薄壁制成的反应室1由热气体如二氧化碳加热,该热气体在夹套2中在大约等于反应室所用压力的压力下循环。气体由泵3穿过加热器4循环。在反应室和夹套之间保持有轻微的压差,如水柱7所示。来自罐24的液体材料通过泵25被压入混合室21,该混合室21被提供有来自罐22的固体材料。混合物被泵35通过管道17被压入,该泵35被提供了来自罐31的液体。氢气通过由加热器20在泵20中循环的热气夹套加热。氢气可以通过加热器13从容器12供应。来自反应室的产物在通过阀之前先通过冷却器36。 37,通过它控制放电速度。倾向于形成沥青的重质矿物油可在进入之前,先与惰性固体物质(如硅藻土,焦炭粉,煤灰等)混合,或与硫结合剂(如硅藻土或浸有碱的沼泽铁矿石)混合。反应室。通过处理获得的产物可以与更多量的煤和c混合。并再次通过反应室。

著录项

  • 公开/公告号GB192850A

    专利类型

  • 公开/公告日1923-02-15

    原文格式PDF

  • 申请/专利权人 FRIEDRICH BERGIUS;STEPHAN LOFFLER;

    申请/专利号GB19210032147

  • 发明设计人

    申请日1921-11-30

  • 分类号C10G1/06;

  • 国家 GB

  • 入库时间 2022-08-24 11:47:46

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