Advanced Control of a Reactive Distillation Column

被引：0

作者：

Nagy, Zoltan K. ^{[1
]}

Klein, Reinhardt ^{[2
]}

Kiss, Anton A. ^{[3
]}

Findeisen, Rolf ^{[2
]}

机构：

[1] Loughbborough Univ, Dept Chem Engn, Loughborough LE11 3TU, Leics, England

[2] Univ Stuttgart, Stuttgart, Germany

[3] Akzo Nobel Chemicas, Arnhem, Netherlands

来源：

17TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING | 2007年 / 24卷

关键词：

reactive distillation; nonlinear model predictive control;

D O I：

暂无

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

The paper presents a detailed analysis of the dynamic behavior of a reactive distillation column. A control relevant dynamic model is derived using first-principles modeling and it is used to study the dynamic behavior of the process at high and low purity operating regimes. The results are used to analyze the performance of linear and nonlinear model predictive control in comparison to coupled PID control.

引用

页码：805 / 810

页数：6

共 4 条

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[3] Two-point control of a reactive distillation column for composition and conversion
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[J]. JOURNAL OF PROCESS CONTROL, 1999, 9 (01) : 19 - 31
[4] Modelling reactive distillation
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[J]. CHEMICAL ENGINEERING SCIENCE, 2000, 55 (22) : 5183 - 5229

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