Running batch distillation in a column with a middle vessel

被引：38

作者：

Barolo, M ^{[1
]}

Guarise, GB ^{[1
]}

Rienzi, SA ^{[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：

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH | 1996年 / 35卷 / 12期

关键词：

D O I：

10.1021/ie960268s

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The practical feasibility of batch distillation in a column with a middle vessel is analyzed. Experimental runs have been carried out in a pilot plant scale continuous distillation column, whose setup has been arranged in such a way as to allow batch operations to be carried out. Practical guidelines are provided for the startup and the operating sequence of the batch column. The implementation of different control configurations is discussed, and the effect of some operating parameters on column performance is shown by experiments.

引用

页码：4612 / 4618

页数：7