Nonlinear model-based predictive control of control nonaffine systems

被引:32
|
作者
Mutha, RK
Cluett, WR
Penlidis, A
机构
[1] UNIV TORONTO,DEPT CHEM ENGN & APPL CHEM,TORONTO,ON M5S 3ES,CANADA
[2] UNIV WATERLOO,DEPT CHEM ENGN,WATERLOO,ON N2L 3G1,CANADA
关键词
model-based control; nonlinear control; predictive control; process control; polymer reactor control;
D O I
10.1016/S0005-1098(96)00220-8
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
This paper proposes a new nonlinear model-based predictive control (NLMPC) algorithm, designed to handle control nonaffine systems (nonlinear in the manipulated variable), which is based on a reinterpretation of the prediction equation as a Taylor series expansion. They key feature of this algorithm lies in the use of a process output prediction that accounts for changes in process dynamics as a function of the operating point as well as of the magnitude of the process input change. From this algorithm, a suboptimal NLMPC algorithm is derived to improve computational efficiency for real-time applications. The performance improvement of the new algorithm is illustrated by comparing it with a standard nonlinear model-based predictive control algorithm using three examples. The first two examples are simulations of simple static nonlinear systems, and the third example is a simulation of a semibatch acrylonitrile-butadiene (NBR) emulsion polymerization process. (C) 1997 Elsevier Science Ltd.
引用
收藏
页码:907 / 913
页数:7
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