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Process for separating an intake flow consisting essentially of hydrogen, methane and C3/C4 hydrocarbons

机译:分离主要由氢气,甲烷和C3 / C4烃组成的进气流的方法

摘要

PCT No. PCT/EP93/01182 Sec. 371 Date Apr. 14, 1995 Sec. 102(e) Date Apr. 14, 1995 PCT Filed May 12, 1993 PCT Pub. No. WO94/08923 PCT Pub. Date Apr. 28, 1994Process for separating a feedstock stream essentially consisting of hydrogen, methane and C3/C4-hydrocarbons, which first passes through a pretreatment, such as, e.g., dehydrogenation, after which the feedstock stream undergoes an at least one-stage partial condensation and separation into a C3/C4-hydrocarbon-rich fraction and into an H2/CH4 fraction, after which a partial stream of the H2/CH4 fraction is mixed in the not yet pretreated feedstock stream. The H2/CH4 gas fraction drawn off from first separator (S1) is divided into two partial streams (10, 17), and first partial stream (10) together with liquid fraction (11) of first separator (S1) is fed to a second separator (S2) after partial condensation (W2), C3/C4-hydrocarbon-rich liquid fraction (16), drawn off at the bottom of second separator (S2), together with the second partial stream of H2/CH4 gas fraction (17) from first separator (S1) is conveyed to a stripping column (S3), an H2-rich gas fraction with high purity (13) is drawn off at the top of second separator (S2), and after evaporating in heat exchange (W2) with the process streams to be cooled is mixed with feedstock stream (2, 2a, 2b) before its pretreatment, and a C3/C4-rich product fraction (20) is drawn off at the bottom of stripping column (S3) and an H2-rich gas fraction with less high purity (18) is drawn off at the top of stripping column (S3).
机译:PCT号PCT / EP93 / 01182秒371日期1995年4月14日102(e)日期1995年4月14日PCT 1993年5月12日提交PCT Pub。 PCT公开号WO94 / 08923。日期1994年4月28日,用于分离基本由氢气,甲烷和C3 / C4烃组成的原料流的方法,该原料流首先经过预处理,例如脱氢,此后原料流经历至少一个阶段部分缩合并分离成富含C3 / C4烃的馏分和H2 / CH4馏分,然后将部分H2 / CH4馏分混合在尚未预处理的原料流中。从第一分离器(S1)排出的H2 / CH4气体馏分被分成两个分流(10、17),并且第一分流(10)与第一分离器(S1)的液体馏分(11)一起送入在部分冷凝(W2)后的第二分离器(S2)中,从第二分离器(S2)底部排出的富含C3 / C4-烃的液体馏分(16)与H2 / CH4气体馏分的第二部分流( 17)从第一分离器(S1)输送到汽提塔(S3),在第二分离器(S2)的顶部抽出高纯度的富H2气体馏分(13),并在热交换中蒸发后( W2)以及待冷却的工艺物流在预处理之前与原料物流(2、2a,2b)混合,然后在汽提塔(S3)的底部排出富含C3 / C4的产物馏分(20),在汽提塔(S3)的顶部排出纯度较低的富氢气体馏分(18)。

著录项

  • 公开/公告号AU662982B2

    专利类型

  • 公开/公告日1995-09-21

    原文格式PDF

  • 申请/专利权人 LINDE AKTIENGESELLSCHAFT;

    申请/专利号AU19930040674

  • 发明设计人 HEINZ BAUER;

    申请日1993-05-12

  • 分类号C07C5/327;C07C7/04;C07C7/09;

  • 国家 AU

  • 入库时间 2022-08-22 04:15:29

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