A METHOD FOR INCORPORATING PROCESS NONLINEARITIES IN MODEL PREDICTIVE CONTROL CALCULATIONS

被引：0

作者：

GUPTA, YP ^{[1
]}

机构：

[1] TECH UNIV NOVA SCOTIA,DEPT CHEM ENGN,HALIFAX B3J 2X4,NS,CANADA

来源：

COMPUTERS IN INDUSTRY | 1991年 / 16卷 / 04期

基金：

加拿大自然科学与工程研究理事会;

关键词：

NONLINEAR CONTROL; MODEL PREDICTIVE CONTROL; NONLINEAR PREDICTIVE CONTROL; PROCESS CONTROL; CHEMICAL ENGINEERING;

D O I：

10.1016/0166-3615(91)90076-L

中图分类号：

TP39 [计算机的应用];

学科分类号：

081203 ; 0835 ;

摘要：

A method for incorporating process nonlinearities in predictive control calculations is proposed. It involves approximating the dynamic response of nonlinear processes through explicit expressions which are then used in the calculations of control action. The methodology is applicable to a class of nonlinear problems encountered in chemical process control. Simulation results obtained on single-input single-output (SISO) and multi-input multi-output (MIMO) stirred tank reactors show the improved control performance that the methodology offers over linear controller models.

引用

页码：367 / 375

页数：9

共 8 条

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[4] GUPTA YP, 1987, SIMPLIFIED MODEL PRE
[5] MARCHETTI JL, 1982, THESIS U CALIFORNIA
[6] PRETT DM, 1980, P JOINT AUTOMATIC CO
[7] RAY WH, 1981, ADV PROCESS CONTROL, P119
[8] VENUGOPAL S, 1989, 39TH CAN CHEM ENG C

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