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Method for separating a hydrocarbon mixture containing hydrogen, separating device, and olefin plant

机译:分离含氢烃混合物的方法,分离装置和烯烃装置

摘要

A method for separating a hydrogen-containing hydrocarbon mixture (C2minus), which in addition to the hydrogen essentially contains hydrocarbons with two carbon atoms and methane, using a distillation column (10). Fluid (a, c, e) of the hydrocarbon mixture (C2minus) is cooled stepwise at a first pressure level, during which time first condensates (b, d) are separated from the fluid (a, c, e). Fluid (e) from the hydrocarbon mixture (C2minus) which remains gaseous after this is fed at the first pressure level into a C2 absorber (7), to which a liquid reflux (r) is added at the top, while a second condensate (f) is drawn off from the sump of the C2 absorber (7) and a gaseous top stream (g) containing predominantly methane and hydrogen is drawn off at the top of the C2 absorber (7). Fluid of the above-mentioned gaseous top stream (g) from the top of the C2 absorber (7) is cooled to a third temperature level and transferred at the first pressure level into a hydrogen separator (8) in which a methane-rich third condensate (i) is separated from the fluid of the gaseous top stream (g), leaving behind a gaseous, hydrogen-rich stream (h). Fluid of the first condensates (b, d) and fluid of the second condensate (f) is depressurized from the first pressure level to a second pressure level below the first pressure level and fed into the distillation column (10) which is operated at the second pressure level. Fluid (e) of the third condensate (i) which is separated in the hydrogen separator (8) from the fluid of the gaseous top stream (g) from the top of the C2 absorber is used as the reflux (r) added at the top of the C2 absorber (7) and transferred from the hydrogen separator to the C2 absorber solely by gravity. The invention also relates to a corresponding separating unit and a corresponding olefin apparatus.
机译:一种使用蒸馏塔( 10 )分离含氢烃混合物(C2减)的方法,该混合物除氢之外还主要包含具有两个碳原子的烃和甲烷。烃混合物(C2负)的流体(a,c,e)在第一压力水平下逐步冷却,在此期间,第一冷凝物(b,d)与流体(a,c,e)分离。来自碳氢化合物混合物(C2负)的流体(e)在此之后仍保持气态,在第一压力级下被送入C2吸收器( 7 ),并在第二吸收器中加入液体回流(r)。从C2吸收塔的集液槽( 7 )中抽出第二个冷凝液(f),并在塔顶排出主要含甲烷和氢的气态塔顶流(g)。 C2吸收器( 7 )。将来自C2吸收塔( 7 )顶部的上述气态塔顶流(g)的流体冷却至第三温度水平,并在第一压力水平下转移到氢气分离器( 8 ),其中将富含甲烷的第三冷凝液(i)与气态塔顶流(g)的流体分离,留下了气态富氢流(h)。将第一冷凝液(b,d)的流体和第二冷凝液(f)的流体从第一压力级减压到低于第一压力级的第二压力级,然后供入蒸馏塔( 10 ),其在第二压力水平下运行。在氢气分离器( 8 )中从C2吸收塔顶部的气态塔顶流(g)的流体中分离出的第三冷凝液(i)的流体(e)被用作在C2吸收塔( 7 )的顶部添加回流(r),仅靠重力将其从氢分离器转移到C2吸收塔。本发明还涉及相应的分离单元和相应的烯烃设备。

著录项

  • 公开/公告号US10677525B2

    专利类型

  • 公开/公告日2020-06-09

    原文格式PDF

  • 申请/专利权人 LINDE AKTIENGESELLSCHAFT;

    申请/专利号US201415109960

  • 发明设计人 HELMUT FRITZ;TORBEN HÖFEL;

    申请日2014-12-17

  • 分类号F25J3/02;C07C7/04;C07C7/09;C07C7/11;B01D53;C10G70/06;C10G70/04;B01D53/14;B01D3/14;C07C4/04;

  • 国家 US

  • 入库时间 2022-08-21 11:26:58

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