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Process and apparatus for separating C3 and heavier components from hydrocarbon gases

机译:从烃类气体中分离出C3和更重组分的方法和设备

摘要

In a process for separating a hydrocarbon gas into a fraction (38) containing a predominant portion of the ethane and lighter components and a fraction (31) containing a predominant portion of the C3 and heavier components, the feed gas is treated in one or more heat exchangers (110, 111, 112), and expansion steps (114, 116) to provide a partly condensed hydrocarbon gas (25) comprising a first residue vapour and a C3-containing liquid which liquid also contains lighter hydrocarbons; the partly condensed feed gas (25) is directed into a separator (118) wherein the first residue vapour is separated from the C3-containing liquid; and the C3-containing liquid (26), at substantially the pressure of separation, is directed into a distillation column (115) wherein said liquid is separated into a second residue (30) containing lighter hydrocarbons and a C3-containing product. In accordance with the present invention the process is improved by cooling said second residue (30) in a heat exchanger (117) to partially condense it; directing the partially condensed second residue (30) into said separator (118) forming thereby a liquid portion and a vapour portion; intimately contacting at least the first residue vapour of the feed gas (25) with at least the liquid portion of the partly condensed second residue (30) in at least one contacting stage within said separator (118), and thereafter separating the vapours and liquids from said contacting stage; supplying the liquids (26) thereby recovered to the distillation column (115) as a top liquid feed thereto: and directing the vapours (37) thereby recovered to the heat exchanger (117) for heat exchange with the second residue (30) from the fractionation column (115), thereby to partly condense the second residue, and thereafter discharging said residue gases (37).
机译:在将烃气分离成主要包含乙烷和较轻组分的馏分(38)和主要包含C 3 和较重组分的馏分(31)的方法中,进料气在一个或多个热交换器(110、111、112)和膨胀步骤(114、116)中进行处理,以提供包含第一残留蒸气和C 3 的部分冷凝的烃气(25)。含亚液体,该液体还包含较轻的烃;将部分冷凝的进料气(25)导入分离器(118),其中第一残留蒸气与含C 3 的液体分离。在基本上分离的压力下,将含有C 3 的液体(26)导入蒸馏塔(115),在该蒸馏塔中,所述液体被分离成含有较轻烃的第二残余物(30)。包含C 3 的产品。根据本发明,通过在热交换器(117)中冷却所述第二残留物(30)以使其部分冷凝来改进该方法。将部分冷凝的第二残留物(30)导入所述分离器(118),从而形成液体部分和蒸气部分;在所述分离器(118)内的至少一个接触阶段中,使进料气(25)的至少第一残余蒸气与部分冷凝的第二残余物(30)的至少液体部分紧密接触,然后分离蒸气和液体从所述接触阶段开始;将由此回收的液体(26)作为塔顶液体进料供应至蒸馏塔(115):并将由此回收的蒸气(37)引导至热交换器(117)以与第二残留物(30)进行热交换分馏塔(115),从而部分冷凝第二残余物,然后排出所述残余气体(37)。

著录项

  • 公开/公告号EP0182643A3

    专利类型

  • 公开/公告日1986-07-23

    原文格式PDF

  • 申请/专利权人 THE ORTLOFF CORPORATION;

    申请/专利号EP19850308383

  • 发明设计人 BUCK LOREN L.;

    申请日1985-11-18

  • 分类号C07C7/04;F25J3/02;

  • 国家 EP

  • 入库时间 2022-08-22 07:35:23

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