Some issues in the design and operation of a batch distillation column with a middle vessel

被引：26

作者：

Barolo, M ^{[1
]}

Guarise, GB ^{[1
]}

Ribon, N ^{[1
]}

Rienzi, S ^{[1
]}

Trotta, A ^{[1
]}

Macchietto, S ^{[1
]}

机构：

[1] UNIV LONDON IMPERIAL COLL SCI TECHNOL & MED,CTR PROC SYST ENGN,LONDON SW7 2BY,ENGLAND

来源：

COMPUTERS & CHEMICAL ENGINEERING | 1996年 / 20卷

基金：

英国工程与自然科学研究理事会;

关键词：

batch distillation; complex column; pilot plant; optimal control;

D O I：

10.1016/0098-1354(96)00017-8

中图分类号：

TP39 [计算机的应用];

学科分类号：

081203 ; 0835 ;

摘要：

Some issues in the design and operation of a batch distillation column with a middle vessel are addressed. Simulation results indicate that operation at infinite reflux and reboil ratios may be more profitable than conventionally considered finite reflux and reboil ratios policies. From an experimental point of view, the possibility of running a pre-existing continuous pilot plant column in a complex batch mode is investigated. Practical suggestions for column design and process control are given.

引用

页码：S37 / S42

页数：6

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