Integration of reaction and separation in a batch extractive distillation column with a middle vessel

被引：0

作者：

Espinosa, J ^{[1
]}

机构：

[1] INGAR, RA-3000 Santa Fe, Argentina

来源：

EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING - 12 | 2002年 / 10卷

关键词：

D O I：

暂无

中图分类号：

TP31 [计算机软件];

学科分类号：

081202 ; 0835 ;

摘要：

In this work, the integration of reaction and separation in a batch extractive distillation column with a middle vessel/reactor is analyzed for azeotrope-forming mixtures. This equipment configuration has the potential to promote complete conversion of reactants and therefore, the main process characteristics are investigated. A mixture showing several azeotropes and suffering an esterification reaction was selected as an academic example.

引用

页码：187 / 192

页数：6

共 12 条

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