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Process for recovering hydrogen and hydrocarbons from the effluent stream of a hydrogen-producing hydrocarbon conversion process

机译:从制氢碳氢化合物转化过程的流出物流中回收氢和碳氢化合物的方法

摘要

Hydrogen and hydrocarbons are recovered from the gaseous effluent stream (8) of a hydrogen-producing hydrocarbon conversion process. The effluent stream is partially condensed (9) to remove (10) the bulk of the heavy C6-plus hydrocarbons, which are then sent (12,40) to a fractionation zone (2, 43). The remaining vapor (11) is compressed (14) to a substantially higher pressure. The compressed vapor (17) is then passed into a membrane separation zone (20, 23) in which a hydrogen-rich stream (24) is separated from the compressed vapor (25). The relatively high pressure non-permeate portion of the vapor stream (25) which emerges from the membrane separation zone (20) is partially condensed by autorefrigeration (28, 29, 30). The still high pressure mixed phase fluid is separated (19) into vapor (31) and liquid (32) hydrocarbon portions. The liquid phase material (32) is then flashed (38) to produce coolant (35) used to perform the partial condensation (28, 30).
机译:从产生氢的烃转化过程的气态流出物流(8)中回收氢和烃。将流出物流部分冷凝(9),以除去(10)大部分重质C6 +烃,然后将其送入(12,40)到分馏区(2,43)。剩余的蒸气(11)被压缩(14)到基本上更高的压力。然后将压缩蒸气(17)送入膜分离区(20、23),在其中将富氢流(24)与压缩蒸气(25)分离。从膜分离区(20)出来的蒸气流(25)的较高压力的非渗透部分通过自动制冷(28、29、30)部分冷凝。仍然高压的混合相流体被分离(19)成蒸气(31)和液体(32)烃部分。然后使液相材料(32)闪蒸(38)以产生用于进行部分冷凝(28、30)的冷却剂(35)。

著录项

  • 公开/公告号EP0178172B1

    专利类型

  • 公开/公告日1988-03-02

    原文格式PDF

  • 申请/专利权人 UOP INC.;

    申请/专利号EP19850307249

  • 发明设计人 STEACY PAUL CLAYTON;

    申请日1985-10-10

  • 分类号C07C7/00;C01B3/50;

  • 国家 EP

  • 入库时间 2022-08-22 06:55:46

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