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

被引：75
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
收藏
页码：735 / 746
页数：12
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