Argon production from air distillation: Use of a heat pump in a ternary distillation with a side rectifier

R. Agrawal, D.W. Woodward, T.F. Yee
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引用次数: 9

Abstract

A ternary feed mixture ABC can be separated into individual components through the use of a main distillation column with a thermally linked side rectifier. To enhance such a separation, a heat pump can be implemented to transfer heat from the condenser at the top of the side rectifier to the reboiler at the bottom of the main column. In this paper, one such heat pump is described and applied to an air distillation system separating the ternary mixture containing nitrogen, oxygen and argon. The separation is performed by a conventional double column with a crude argon side column. When this system is operated at an elevated pressure to obtain higher product pressures, the separation of oxygen and argon becomes very difficult and leads to reduced argon recovery. The proposed heat pump enhances the separation by providing a supplementary crude argon condensing duty through the vaporization of a liquid oxygen stream from the bottom of the low pressure (LP) column. This scheme improves the liquid/vapour ratio (L/V) in the bottom section of the LP column and, more importantly, increases the vapour feed to the crude argon column. This increased feed rate leads to a substantial increase in argon recovery for the elevated pressure air distillation process.

空气蒸馏制氩:在带侧整流器的三元蒸馏中使用热泵
三元进料混合物ABC可以通过使用带有热联侧整流器的主精馏塔分离成单独的组分。为了加强这种分离,可以采用热泵将热量从侧整流器顶部的冷凝器传递到主塔底部的再沸器。本文介绍了一种热泵,并将其应用于分离含氮、氧、氩三元混合物的空气蒸馏系统。采用常规双柱分离,侧柱为粗氩柱。当该系统在高压下运行以获得更高的产品压力时,氧气和氩气的分离变得非常困难,导致氩气回收率降低。所提出的热泵通过从低压(LP)塔底部汽化液态氧流来提供补充的粗氩冷凝任务,从而增强了分离。该方案提高了低压塔底部的液气比(L/V),更重要的是增加了粗氩塔的汽进给量。这种进料速率的增加导致了高压空气蒸馏过程中氩气回收率的大幅增加。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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