首页> 外国专利> PROCEDURE OF SPLITTING ETHYL BENZENE AND STYRENE BY DISTILLATION OF A LIQUID MIXTURE COMPRISING PREDOMINANTLY STYRENE AND ETHYL BENZENE

PROCEDURE OF SPLITTING ETHYL BENZENE AND STYRENE BY DISTILLATION OF A LIQUID MIXTURE COMPRISING PREDOMINANTLY STYRENE AND ETHYL BENZENE

机译:通过蒸馏主要由苯乙烯和乙基苯组成的液体混合物来裂解乙基苯和苯乙烯的方法

摘要

The invented separation process of ethyl benzene and styrene employs vapor compression. Waste vapors of low-boiling components are partially compresses and generated heat is employed for heating a distillation mixture in a distillation column (1) reboiler (4). A portion of condensed liquid of the low-boiling components leaving a superheater (2) is separated into two partial flows. The first partial flow is conducted via a reboiler (5) into a distillation column (6) with a cylinder charge that operates under reduced pressure and is filled with a liquid of high-boiling components from the column (1) bottom section back to the column (1) upper section. So the first partial flow serves as a heat source for the distillation column (6) with pure styrene. Styrene contained in the column (6) is separated by distillation from components exhibiting higher boiling point. The first partial flow can be alternatively conducted even via another handy receiver of suitable temperature and then supplied back into the column (1) upper section. The second partial flow is conducted back to the column (1) upper section.
机译:发明的乙苯和苯乙烯的分离方法采用蒸气压缩。低沸点组分的废气被部分压缩,产生的热量被用于加热蒸馏塔(1)再沸器(4)中的蒸馏混合物。离开过热器(2)的一部分低沸点组分冷凝液被分成两个部分流。第一部分流通过再沸器(5)进入蒸馏塔(6),并在减压下运行并装有高沸点组分液体的圆筒装料从塔(1)的底部部分回流到塔顶。 (1)上部。因此,第一部分流用作带有纯苯乙烯的蒸馏塔(6)的热源。通过蒸馏将塔(6)中包含的苯乙烯与表现出较高沸点的组分分离。第一分流甚至可以通过另一个合适温度的方便接收器进行引导,然后再送回塔(1)的上部。第二部分流被导回到塔(1)的上部。

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