An algorithmic method for the selection of multivariable process control structures

被引:30
作者
Kookos, IK [1 ]
Perkins, JD [1 ]
机构
[1] Univ London Imperial Coll Sci Technol & Med, Dept Chem Engn & Chem Technol, Ctr Proc Syst Engn, London SW7 2BY, England
关键词
control structure selection; algorithmic methods; multivariable output feedback control;
D O I
10.1016/S0959-1524(00)00063-9
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
In process systems, the selection of suitable sets of manipulated and controlled variables and the design of their interconnection, known as the control structure selection problem, is an important structural optimisation problem. The operating performance of a plant depends on the control structure selected as well as the characteristics of the disturbances acting on the plant. The economic penalty associated with the variability of main process variables close to active constraints is used in this work in order to develop a quantitative measure for the ranking of alternative control structures. Based on this measure, a general methodology is presented for the generation of promising control structures where general centralised, linear time invariant, output feedback controllers are used to form the closed loop system. The special case of optimal static output feedback controllers is further investigated in this paper. Furthermore, the problem of selecting proper weights in forming quadratic integral performance indices in designing optimal multivariable controllers is addressed. The validity and usefulness of the method is demonstrated through a number of case studies. (C) 2001 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:85 / 99
页数:15
相关论文
共 33 条
[1]   Operability assessment in chemical plants [J].
Bahri, PA ;
Bandoni, A ;
Romagnoli, J .
COMPUTERS & CHEMICAL ENGINEERING, 1996, 20 :S787-S792
[2]   Plantwide design and control of processes with inerts. 3. Intermediate inerts [J].
Belanger, PW ;
Luyben, WL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (02) :535-546
[3]  
Brenan K. E., 1989, NUMERICAL SOLUTION I
[4]  
Bryson A. E., 1975, APPL OPTIMAL CONTROL
[5]  
Buckley P., 1964, TECHNIQUES PROCESS C
[6]   FLEXIBILITY ANALYSIS OF DYNAMIC-SYSTEMS [J].
DIMITRIADIS, VD ;
PISTIKOPOULOS, EN .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (12) :4451-4462
[7]   A PLANT-WIDE INDUSTRIAL-PROCESS CONTROL PROBLEM [J].
DOWNS, JJ ;
VOGEL, EF .
COMPUTERS & CHEMICAL ENGINEERING, 1993, 17 (03) :245-255
[8]  
DOWNS JJ, 1994, IFAC WORKSH INT PROC, P100
[9]   Economic impact of disturbances and uncertain parameters in chemical processes - A dynamic back-off analysis [J].
Figueroa, JL ;
Bahri, PA ;
Bandoni, JA ;
Romagnoli, JA .
COMPUTERS & CHEMICAL ENGINEERING, 1996, 20 (04) :453-461
[10]  
GEORGIOU A, 1989, CHEM ENG RES DES, V67, P600