Distributed Model Predictive Control of Nonlinear Process Systems

被引:181
作者
Liu, Jinfeng [1 ]
Munoz de la Pena, David [3 ]
Christofides, Panagiotis D. [1 ,2 ]
机构
[1] Univ Calif Los Angeles, Dept Chem & Biomol Engn, Los Angeles, CA 90095 USA
[2] Univ Calif Los Angeles, Dept Elect Engn, Los Angeles, CA 90095 USA
[3] Univ Seville, Dept Ingn Sistemas & Automat, Seville 41092, Spain
关键词
distributed model predictive control; nonlinear systems; networked control systems; process control; RECEDING HORIZON CONTROL; STATE; COMMUNICATION; STABILIZATION; CONSTRAINTS;
D O I
10.1002/aic.11801
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This work focuses on a class of nonlinear control problems that arise when new control systems which may use networked sensors and/or actuators are added to already operating control loops to improve closed-loop performance. In this case, it is desirable to design the pre-existing control system and the new control system in a way such that they coordinate their actions. To address this control problem, a distributed model predictive control method is introduced where both the pre-existing control system and the new control system are designed via Lyapunov-based model predictive control. Working with general nonlinear models of chemical processes and assuming that there exists a Lyapunov-based controller that stabilizes the nominal closed-loop system using only the pre-existing control loops, two separate Lyapunov-based model predictive controllers are designed that coordinate their actions in an efficient fashion. Specifically, the proposed distributed model predictive control design preserves the stability properties of the Lyapunov-based controller, improves the closed-loop performance, and allows handling input constraints. In addition, the proposed distributed control design requires reduced communication between the two distributed controllers since it requires that these controllers communicate only once at each sampling time and is computationally more efficient compared to the corresponding centralized model predictive control design. The theoretical results art? illustrated using a chemical process example. (C) 2009 American Institute of Chemical Engineers AIChE J, 55: 1171-1184, 2009
引用
收藏
页码:1171 / 1184
页数:14
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