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Combined separation of heavy - and low boilers from natural gas

机译:天然气重汽和低汽的联合分离。

摘要

It is a method for the separation of heavy - and low boilers from a hydrocarbon - extend feed fraction, preferably made of natural gas, is described wherein the feed fraction (1), partially condensed (e1, e2), by rectification (t1) a high boilers - rich liquid fraction (8) is separated off (1. separating stage), the resulting, on which has been depleted heavies gas (10), partially condensed (e4) and by rectification (t2) in a methane - rich liquid fraction (11) and a low boilers - rich gas (12) is separated, (2. separating stage). According to the invention,– if the 1. separating stage (t1) at a pressure of at least 25 bar,– the depleted heavies is subjected to gas (10) before they are supplied to the separating stage (t2) 2. no pressure increase, and– , the return flow of 2. separating stage (t2) generated by an open cooling circuit,– the refrigeration cycle circulating refrigerant in the open on two different temperature levels barrel against the return currents (14, 15) in the top condenser (e7) and in a side condenser (e8) of the 2. separating stage (t2) is evaporated, and the pressure of the capacitor (e8) in the sides of the vaporized refrigerant (25) is at least three times, is so high as the pressure of the in the top condenser (e7) vaporized refrigerant (22).
机译:描述了一种从烃类中分离重质和低质沸腾物的进料馏分的方法,该进料馏分优选由天然气制成,其中进料馏分(1)通过精馏(t1)进行了部分冷凝(e1,e2)分离出高沸点的富含液体的馏分(8)(1.分离阶段),将其上已耗尽的重气(10),部分冷凝(e4)并通过精馏(t2)在富含甲烷的馏分中分离液体馏分(11)和低沸物-富气(12)被分离,(2。分离阶段)。根据本发明,-如果分离级(t1)处于至少25 bar的压力,-贫化的重烃在被供应到分离级(t2)之前要经受气体(10)2.无压力增加,以及–由开放式冷却回路产生的分离级(t2)的回流。–制冷循环在两个不同温度水平下在开放状态下循环制冷剂在桶中逆着顶部的回流(14、15) 2.分离阶段(t2)的冷凝器(e7)和侧冷凝器(e8)被蒸发,并且蒸发的制冷剂(25)侧的电容器(e8)的压力至少为三倍。如此高的压力使顶部冷凝器(e7)中的气化制冷剂(22)蒸发。

著录项

  • 公开/公告号DE102013013883A1

    专利类型

  • 公开/公告日2015-02-26

    原文格式PDF

  • 申请/专利权人 LINDE AKTIENGESELLSCHAFT;

    申请/专利号DE20131013883

  • 发明设计人 HARTMUT WALZ;HEINZ DR. BAUER;

    申请日2013-08-20

  • 分类号F25J3/02;C07C7/09;

  • 国家 DE

  • 入库时间 2022-08-21 14:55:46

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