The interactions of design, control and operability in reactive distillation systems

被引：76

作者：

Georgiadis, MC

Schenk, M

Pistikopoulos, EN

Gani, R

机构：

[1] Ctr Res & Technol Hellas, Chem Proc Engn Res Inst, Thessaloniki 57001, Greece

[2] Univ London Imperial Coll Sci Technol & Med, Ctr Proc Syst Engn, Dept Chem Engn, London SW7 2BY, England

[3] Tech Univ Denmark, CAPEC, Dept Chem Engn, DK-2800 Lyngby, Denmark

来源：

COMPUTERS & CHEMICAL ENGINEERING | 2002年 / 26卷 / 4-5期

关键词：

reactive distillation; process design; process control; dynamic optimization;

D O I：

10.1016/S0098-1354(01)00774-8

中图分类号：

TP39 [计算机的应用];

学科分类号：

081203 ; 0835 ;

摘要：

In this work the design and control of a reactive distillation column, described by a rigorous dynamic model, is tackled via two different optimization approaches. In the first, the steady-state process design and the control system are optimized sequentially. It is shown that operability is a strong function of the process design and potential operability bottlenecks are identified. In the second approach, the process design and the control system are optimized simultaneously leading to a more economically beneficial and better controlled system than that obtained using the sequential approach. (C) 2002 Elsevier Science Ltd. All rights reserved.

引用

页码：735 / 746

页数：12

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