Simultaneous design and control optimisation under uncertainty

被引：91

作者：

Bansal, V

Perkins, JD

Pistikopoulos, EN ^{[1
]}

Ross, R

van Schijndel, JMG

机构：

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

[2] Proc Syst Enterprise Ltd, London W6 9DA, England

[3] Shell Int Chem BV, NL-1030 BN Amsterdam, Netherlands

来源：

COMPUTERS & CHEMICAL ENGINEERING | 2000年 / 24卷 / 2-7期

关键词：

process design; process control; uncertainty; mixed-integer dynamic optimization;

D O I：

10.1016/S0098-1354(00)00475-0

中图分类号：

TP39 [计算机的应用];

学科分类号：

081203 ; 0835 ;

摘要：

This paper demonstrates how the design and control of processes described by large-scale, complex, mixed-integer dynamic models can be simultaneously optimised in the face of time-varying disturbances and parametric uncertainties. A rigorously modelled distillation example is used for this purpose, where the number of trays, feed location, column diameter, surface areas of the heat exchangers and tuning parameters of the controllers are selected in order to minimise the total annualised cost of the system, while satisfying a large number of feasibility constraints. (C) 2000 Elsevier Science Ltd. All rights reserved.

引用

页码：261 / 266

页数：6

共 16 条

[1] The interactions of design and control; double-effect distillation [J].