NONLINEAR MODEL-BASED CONTROL USING 2ND-ORDER VOLTERRA MODELS

被引:201
作者
DOYLE, FJ
OGUNNAIKE, BA
PEARSON, RK
机构
[1] E. I. DuPont deNemours and Co., Inc., Experimental Station El, Wilmington
[2] School of Chemical Engineering, Purdue University, West Lafayette
关键词
NONLINEAR CONTROL SYSTEMS; PROCESS CONTROL; PROCESS MODELS; PREDICTIVE CONTROL; INVERSE SYSTEMS;
D O I
10.1016/0005-1098(94)00150-H
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
A nonlinear controller synthesis scheme is presented that retains the original spirit and characteristics of conventional (linear) model predictive control (MPC) while extending its capabilities to nonlinear systems. The scheme employs a Volterra model-a simple and convenient nonlinear extension of the linear convolution model employed by conventional MPC-and gives rise to a controller composed of a conventional linear controller augmented by an auxiliary loop of nonlinear 'corrections'. Simulation case studies involving two different examples representative of the typical spectrum of nonlinear behavior in real chemical processes-an industrial polymerization reactor and an isothermal reactor exhibiting inverse response-are used to demonstrate the practical utility of the control scheme and to evaluate its performance.
引用
收藏
页码:697 / 714
页数:18
相关论文
共 34 条
[1]  
ALBAIYAT S, 1986, 25TH P IEEE C DEC CO, P1306
[2]  
ALBAIYAT SA, 1986, THESIS U NOTRE DAME
[3]  
[Anonymous], 1980, VOLTERRA WIENER THEO
[4]  
BARTEE J, 1992, P AM CONTROL C
[5]  
BENDAT JS, 1990, NONLINEAR SYSTEM ANA
[6]  
BENISRAEL A, 1974, GENERALIZED INVERSES
[7]  
Berger M.S., 1977, PURE APPL MATH
[8]  
BIEGLER L, 1991, 4TH P INT C CHEM PRO
[9]   FADING MEMORY AND THE PROBLEM OF APPROXIMATING NONLINEAR OPERATORS WITH VOLTERRA SERIES [J].
BOYD, S ;
CHUA, LO .
IEEE TRANSACTIONS ON CIRCUITS AND SYSTEMS, 1985, 32 (11) :1150-1161
[10]   FEEDFORWARD AND FEEDBACK-CONTROL OF A SOLUTION COPOLYMERIZATION REACTOR [J].
CONGALIDIS, JP ;
RICHARDS, JR ;
RAY, WH .
AICHE JOURNAL, 1989, 35 (06) :891-907