Shortest-prediction-horizon non-linear model-predictive control

被引:22
|
作者
Valluri, S
Soroush, M [1 ]
Nikravesh, M
机构
[1] Drexel Univ, Dept Chem Engn, Philadelphia, PA 19104 USA
[2] Univ Calif Berkeley, Lawrence Berkeley Lab, Div Earth Sci, Berkeley, CA 94720 USA
关键词
non-linear control; model-predictive control; constrained control; input-output linearization; model-based control; windup compensation;
D O I
10.1016/S0009-2509(97)00284-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This article concerns non-linear control of single-input-single-output processes with input constraints and deadtimes. The problem of input-output linearization in continuous time is formulated as a model-predictive control problem, for processes with full-state measurements and for processes with incomplete state measurements and deadtimes. This model-predictive control formulation allows one (i) to establish the connections between model-predictive and input-output linearizing control methods; and (ii) to solve directly the problems of constraint handling and windup in input-output linearizing control. The derived model-predictive control laws have the shortest possible prediction horizon and explicit analytical form, and thus their implementation does not require on-line optimization. Necessary conditions for stability of the closed-loop system under the constrained dynamic control laws are given. The connections between (a) the developed control laws and (b) the model state feedback control;and the modified internal model control-are established. The application and performance of the derived controllers are demonstrated by numerical simulations of chemical and biochemical reactor examples. (C) 1997 Elsevier Science Ltd.
引用
收藏
页码:273 / 292
页数:20
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