MODEL-PREDICTIVE CONTROL OF CHEMICAL PROCESSES

被引：86

作者：

EATON, JW ^{[1
]}

RAWLINGS, JB ^{[1
]}

机构：

[1] UNIV TEXAS,DEPT CHEM ENGN,AUSTIN,TX 78712

来源：

CHEMICAL ENGINEERING SCIENCE | 1992年 / 47卷 / 04期

基金：

美国国家科学基金会;

关键词：

D O I：

10.1016/0009-2509(92)80263-C

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

This paper discusses model-predictive control, a scheme in which an open-loop performance objective is optimized over a finite moving time horizon. Model-predictive control is shown to provide performance superior to conventional feedback control for nonminimum phase systems or systems with input constraints when future set points are known. Stabilizing unstable linear plants and controlling nonlinear plants with multiple steady states are also discussed.

引用

页码：705 / 720

页数：16

共 33 条

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