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LNG PRODUCTION IN CRYOGENIC NATURAL GAS PROCESSING PLANTS

机译:低温天然气处理厂中的LNG生产

摘要

1. A process for liquefying a natural gas stream containing; methane and heavier hydrocarbon components wherein (a) said natural gas stream is withdrawn from a cryogenic natural gas processing plant recovering natural gas liquids; (b) said natural gas stream is cooled under pressure sufficiently to partially condense it; (c) a distillation stream is withdrawn from said plant to supply at least a portion of said cooling of said natural gas stream; (d) said partially condensed natural gas stream is separated into a liquid stream and a vapor stream, whereupon said liquid stream is directed to said plant; (e) said vapor stream is expanded to an intermediate pressure and further cooled at said intermediate pressure to condense it; (f) said condensed expanded stream is directed to a distillation column at a mid-column feed point; (g) a liquid distillation stream is withdrawn from a lower region of said distillation column and directed to said plant; (h) a vapor distillation stream is withdrawn from an upper region of said distillation column and cooled under pressure to condense at least a portion of it and form a condensed stream; (i) said condensed stream is divided into at least two portions, with a first portion directed to said distillation column at a top feed position; (j) a second portion of said condensed stream is expanded to lower pressure to form said liquefied natural gas stream; and (k) me temperature of said partially condensed natural gas stream and the quantities and temperatures of said feed streams to said distillation column are effective to maintain the overhead temperature of said distillation column at a temperature whereby the major portion of said heavier hydrocarbon components is recovered in said liquid stream and said liquid distillation stream.
机译:1.一种液化天然气流的方法,其包含:甲烷和重烃组分,其中(a)所述天然气流从回收天然气液体的低温天然气加工厂中抽出; (b)将所述天然气流在压力下充分冷却以使其部分冷凝; (c)从所述设备中抽出蒸馏流以提供所述天然气流的所述冷却的至少一部分; (d)将所述部分冷凝的天然气流分离成液体流和蒸气流,随后将所述液体流导向所述设备; (e)使所述蒸汽流膨胀至中压,并在所述中压下进一步冷却以使其冷凝; (f)将所述冷凝的膨胀物流在塔中进料点引入蒸馏塔; (g)从所述蒸馏塔的下部区域抽出液体蒸馏流并引向所述设备; (h)从所述蒸馏塔的上部抽出蒸汽蒸馏流,并在压力下冷却以冷凝至少一部分,并形成冷凝流; (i)将所述冷凝物流分成至少两部分,第一部分在顶部进料位置处指向所述蒸馏塔; (j)将所述冷凝流的第二部分膨胀至较低压力以形成所述液化天然气流; (k)所述部分冷凝的天然气物流的温度以及进入所述蒸馏塔的所述进料物流的数量和温度可有效地将所述蒸馏塔的塔顶温度维持在这样的温度,其中所述重烃组分的大部分为回收在所述液体流和所述液体蒸馏流中。

著录项

  • 公开/公告号IN2003KN01321A

    专利类型

  • 公开/公告日2009-08-14

    原文格式PDF

  • 申请/专利权人

    申请/专利号IN1321/KOLNP/2003

  • 申请日2003-10-14

  • 分类号F25J3/00;

  • 国家 IN

  • 入库时间 2022-08-21 19:27:36

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