首页> 外国专利> METHOD FOR ISOLATING A STREAM OF C2+ HYDROCARBONS CONTAINED IN THE REFINERY RESIDUAL GAS, AND PLANT FOR IMPLEMENTATION THEREOF

METHOD FOR ISOLATING A STREAM OF C2+ HYDROCARBONS CONTAINED IN THE REFINERY RESIDUAL GAS, AND PLANT FOR IMPLEMENTATION THEREOF

机译:用于分离炼油厂残留气体中包含的C2 +烃流的方法,以及用于实施的植物

摘要

FIELD: gas industry.;SUBSTANCE: invention relates to a method for isolating a stream (12) of C2+ hydrocarbons contained in the refinery residual gas (16), including the following stages: forming a residual stream (28) from said refinery residual gas (16); supplying said residual stream (28) to the evaporation tank (30) to form a gaseous overhead stream (32) of the evaporation tank and a liquid bottom stream (34) of the evaporation tank; supplying said bottom stream (34) of the evaporation tank to the distillation column (38); cooling said overhead stream (32) of the evaporation tank in a heat exchanger (36), resulting in a cooled overhead stream (58) of the evaporation tank; separating said cooled overhead stream (58) of the evaporation tank into a liquid lower stream (64) supplied into the distillation column (38) and a gaseous upper stream (80); supplying the lower stream (64) to the distillation column (38) above the inlet of the bottom stream (34) of the evaporation tank; extracting the stream (12) of C2+ hydrocarbons in the bottom part of the distillation column (38); removing the gaseous overhead stream (72) in the head part of the distillation column (38); forming at least one effluent stream (14) from the overhead stream (72) of the distillation column and/or from the upper stream (80); heating said or each effluent stream (14) in the heat exchanger (36) by means of heat exchange with the overhead stream (32) of the evaporation tank. Separation of the cooled overhead stream (58) of the evaporation tank includes supplying the cooled overhead stream (58) of the evaporation tank into an absorber (40) and introducing a methane-rich stream (42) into the absorber (40) to bring the cooled overhead stream (58) of the evaporation tank into contact with the methane-rich stream (42), wherein the molar content of methane in the methane-rich stream (42) is greater than 90 mol.% The invention also relates to a plant (10) for isolating a stream (12) of C2+ hydrocarbons from the refinery residual gas (16).;EFFECT: effective and stable isolation of valuable products from the refinery residual gas, while simultaneously limiting the capital and operating costs of the method.;14 cl, 1 tbl, 1 dwg
机译:田间:气体工业。物质:发明涉及用于分离炼油厂残留气体(16)中所含的C2 +烃的流(12)的方法,包括以下阶段:从所述炼油厂的残留气体中形成残留物流(28) (16);将所述残余物流(28)供应到蒸发罐(30)以形成蒸发槽的气态架空物流(32)和蒸发罐的液体底部流(34);将蒸发罐的所述底部流(34)供应到蒸馏塔(38);在热交换器(36)中冷却蒸发槽的所述顶部流(32),导致蒸发槽的冷却架空物流(58);将蒸发罐的所述冷却的塔顶物流(58)分离成供给蒸馏塔(38)和气态上游(80)的液体下部流(64);将下部流(64)供应到蒸发罐的底部流(34)的入口上方的蒸馏塔(38);在蒸馏塔的底部(38)的底部中提取C2 +烃的流(12);在蒸馏塔的头部(38)中除去气体架空物流(72);从蒸馏塔的顶部流(72)和/或从上游(80)形成至少一个流出物流(14);通过与蒸发槽的架空物流(32)的热交换加热在热交换器(36)中加热所述或每个流出物流(14)。蒸发槽的冷却架空物流(58)的分离包括将蒸发槽的冷却的架空物流(58)供应到吸收器(40)中并将富含甲烷的流(42)引入吸收器(40)以带来蒸发槽的冷却架空物流(58)与富甲烷的流(42)接触,其中富含甲烷流(42)中甲烷的摩尔含量大于90摩尔。%本发明还涉及用于分离炼油厂残留气体(16)的C2 +烃的流(12)的植物(10)。效果:有效且稳定地分离炼油厂残留气体的宝贵产品,同时限制了资本和运营成本方法。; 14 cl,1 tbl,1 dwg

著录项

  • 公开/公告号RU2764176C2

    专利类型

  • 公开/公告日2022-01-14

    原文格式PDF

  • 申请/专利权人

    申请/专利号RU20190136828

  • 申请日2018-05-17

  • 分类号C07C7/04;C07C7/11;F25J3;B01D53;C10G7;

  • 国家 RU

  • 入库时间 2024-06-14 22:41:51

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