A multiple model, state feedback strategy for robust control of non-linear processes

被引:25
作者
Wang, F. Y. [1 ]
Bahri, P.
Lee, P. L.
Cameron, I. T.
机构
[1] Univ Queensland, Div Chem Engn, Brisbane, Qld 4072, Australia
[2] Murdoch Univ, Sch Engn, Murdoch, WA 6150, Australia
[3] Univ S Australia, Adelaide, SA 5001, Australia
基金
澳大利亚研究理事会;
关键词
chaos; localised models; min-max optimisation; model modification; robust control; OPERATION;
D O I
10.1016/j.compchemeng.2006.05.008
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
The major limitation of reported multiple model approaches is that robustness against process/controller disturbances cannot be addressed for processes consisting of hybrid stable/unstable regimes, or with chaotic dynamics. In this paper, a significantly modified multiple model approach is developed to achieve robust control with global stability. The new advances include: (1) stabilization of open-loop unstable plants using a state feedback strategy, (2) incorporation of an adjustable pre-filter to achieve offset-free control, (3) implementation of a Kalman filter for state estimation, and (4) connection of the multiple model approach with non-linear model predictive control to achieve a precise control objective. The improved controller design method is successfully applied to two non-linear processes with different chaotic behaviour. Compared with conventional methods without model modifications, the new approach has achieved significant improvement in control performance and robustness with a dramatically reduced number of local models. (c) 2006 Elsevier Ltd. All rights reserved.
引用
收藏
页码:410 / 418
页数:9
相关论文
共 14 条
[1]  
[Anonymous], 2016, Process dynamics and control
[2]  
[Anonymous], P AM CONTR C
[3]  
Balas G.J., 1995, MU ANAL SYNTHESIS TO
[4]   Continuation methods for robust controller design for plants with operating-point-dependent behaviour [J].
Bartholomäus, R .
CONTROL ENGINEERING PRACTICE, 2002, 10 (09) :941-950
[5]   Control and operations: when does controllability equal profitability? [J].
Edgar, TF .
COMPUTERS & CHEMICAL ENGINEERING, 2004, 29 (01) :41-49
[6]  
Maciejowski J. M., 1989, Multivariable Feedback Design
[7]   The incidence of oscillatory behavior in the continuous fermentation of Zymomonas mobilis [J].
McLellan, PJ ;
Daugulis, AJ ;
Li, JH .
BIOTECHNOLOGY PROGRESS, 1999, 15 (04) :667-680
[8]  
MurraySmith R., 1997, Multiple model approaches to nonlin- ear modelling and control
[9]   Control of multi-unit processing plants - A systematic methodology [J].
Samyudia, Y ;
Lee, PL ;
Cameron, IT ;
Green, M .
COMPUTERS & CHEMICAL ENGINEERING, 1996, 20 :S919-S924
[10]  
Shorten R, 1999, INT J CONTROL, V72, P620, DOI 10.1080/002071799220812