Real-Time Economic Model Predictive Control of Nonlinear Process Systems

被引:23
作者
Ellis, Matthew [1 ]
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
基金
美国国家科学基金会;
关键词
process control; process optimization; chemical processes; model predictive control; process economics; nonlinear systems; MPC; ENERGY; OPTIMIZATION; PERFORMANCE; STABILITY; SUBJECT; STATE;
D O I
10.1002/aic.14673
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Closed-loop stability of nonlinear systems under real-time Lyapunov-based economic model predictive control (LEMPC) with potentially unknown and time-varying computational delay is considered. To address guaranteed closed-loop stability (in the sense of boundedness of the closed-loop state in a compact state-space set), an implementation strategy is proposed which features a triggered evaluation of the LEMPC optimization problem to compute an input trajectory over a finite-time prediction horizon in advance. At each sampling period, stability conditions must be satisfied for the precomputed LEMPC control action to be applied to the closed-loop system. If the stability conditions are not satisfied, a backup explicit stabilizing controller is applied over the sampling period. Closed-loop stability under the real-time LEMPC strategy is analyzed and specific stability conditions are derived. The real-time LEMPC scheme is applied to a chemical process network example to demonstrate closed-loop stability and closed-loop economic performance improvement over that achieved for operation at the economically optimal steady state. (c) 2014 American Institute of Chemical Engineers AIChE J, 61: 555-571, 2015
引用
收藏
页码:555 / 571
页数:17
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