首页> 外国专利> COAL HYDROGENATION PROCESS USING THERMAL COUNTERCURRENT FLOW REACTION ZONE

COAL HYDROGENATION PROCESS USING THERMAL COUNTERCURRENT FLOW REACTION ZONE

机译:热逆流反应区的煤加氢过程

摘要

ABSTRACTThermal hydrogenation of coal to produce hydrocarbonliquid and gas products is performed in a thermal reactionzone, in which a coal/oil slurry flows generally downwardlycountercurrent to upflowing hydrogen. An effluent streamcontaining light hydrocarbon liquid and gas is withdrawnfrom the thermal reaction zone upper end, and a heavy liquidstream containing unconverted coal and ash is withdrawn fromthe reaction zone bottom end. Both streams are passed tophase separation and distillation steps for recovery ofhydrocarbon gas and liquid products. A portion of the lightliquid effluent is preferably recycled to the reaction zonelower end for upflow therein to help increase coal residencetime and for further hydrogenation reaction. If desired,the heavy liquid bottoms stream from the thermal reactionzone and containing unconverted coal and ash can be passedwith additional hydrogen to a second catalytic reaction stepfor further hydrogenation reaction to increase the yield oflower-boiling hydrocarbon liquid products.
机译:抽象煤热加氢生产碳氢化合物液体和气体产物在热反应中进行煤/油浆通常向下流动的区域与向上流动的氢气逆流。废水含有轻烃液体和气体的气体被抽出从热反应区上端开始,有重液体含有未转化的煤和灰的物流从反应区底端。这两个流都传递到相分离和蒸馏步骤回收碳氢化合物气体和液体产品。一部分光液体流出物优选再循环至反应区下端向上流动,以帮助增加煤的保留时间并用于进一步的氢化反应。如果需要的话热反应产生的重质液体塔底物流可以通过含有未转化煤和灰分的区域与额外的氢气一起进行第二个催化反应步骤进行进一步的氢化反应以提高产率低沸点烃类液体产品。

著录项

  • 公开/公告号CA1194443A

    专利类型

  • 公开/公告日1985-10-01

    原文格式PDF

  • 申请/专利权人 HYDROCARBON RESEARCH INC.;

    申请/专利号CA19820417085

  • 发明设计人 SCHULER PAUL D.;JOHANSON EDWIN S.;

    申请日1982-12-06

  • 分类号C10G1/06;

  • 国家 CA

  • 入库时间 2022-08-22 08:05:03

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