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Process for the low-temperature separation of air in an air separation plant and air separation plant

机译:在空分设备中进行空气的低温分离的方法及空分设备

摘要

The invention relates to a process for the separation of air (AIR), in which cooled air (AIR) at a first separation pressure is separated in a first separation column (S1) at least into a nitrogen-enriched top fraction and an oxygen-enriched bottom fraction, and in which further cooled air (AIR) in a mixing column (M) is liquefied at a mixing column pressure by means of direct heat exchange against a liquid oxygen-enriched stream, which is at least partly obtained from the oxygen-enriched bottom fraction from the first separation column (S1), to form a mixing column bottom fraction. According to the invention further cooled air (AIR) at a second separation pressure is likewise separated in a second separation column (S2) into a nitrogen-enriched top fraction and an oxygen-enriched bottom fraction, wherein the nitrogen-enriched top fraction from the second separation column (S2) is at least partly cooled by using the mixing column bottom fraction from the mixing column (M). To this end, the nitrogen-enriched top fraction from the second separation column (S2) is at least partly guided through the liquefaction chamber of a top condenser (E2) of the second separation column (S2), which is constructed as a condenser evaporator and the evaporation chamber of which is operated at an evaporation chamber pressure which lies between the mixing column pressure and a third separation pressure, at which the liquid oxygen-rich stream is obtained in a third separation column (S3), and in which at least part of the mixing column bottom fraction from the mixing column (M) is fed in in liquid form at the evaporation chamber pressure. The invention further relates to a corresponding air separation plant.
机译:用于分离空气的方法技术领域本发明涉及一种用于分离空气的方法,其中在第一分离压力下将冷却的空气在第一分离塔S1中至少分离成富氮的塔顶馏分和氧分离塔。富集的塔底馏分,其中混合塔(M)中的进一步冷却的空气(AIR)在混合塔压力下通过与至少部分从氧气中获得的液态富氧流直接换热而液化-从第一分离塔(S1)富集塔底馏分,以形成混合塔塔底馏分。根据本发明,在第二分离压力下的另外的冷却的空气(AIR)同样在第二分离塔(S2)中被分离成富氮的顶部馏分和富氧的底部馏分,其中氮富集的顶部馏分从通过使用来自混合塔(M)的混合塔底部馏分,至少部分冷却第二分离塔(S2)。为此,将来自第二分离塔(S2)的富氮顶部馏分至少部分地引导通过第二分离塔(S2)的顶部冷凝器(E2)的液化室,该顶部冷凝器构造为冷凝器蒸发器。并且其蒸发室在蒸发室压力下操作,该蒸发室压力在混合塔压力和第三分离压力之间,在该压力下,在第三分离塔(S3)中获得液态富氧流,并且其中至少来自混合塔(M)的一部分混合塔底部馏分在蒸发室压力下以液体形式进料。本发明还涉及相应的空气分离设备。

著录项

  • 公开/公告号AU2013339789A1

    专利类型

  • 公开/公告日2015-04-30

    原文格式PDF

  • 申请/专利权人 LINDE AKTIENGESELLSCHAFT;

    申请/专利号AU2013339789A1

  • 发明设计人 LAUTENSCHLAGER TOBIAS;

    申请日2013-10-31

  • 分类号F25J3/04;

  • 国家 AU

  • 入库时间 2022-08-21 15:09:54

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