A model predictive formulation for control of open-loop unstable cascade systems

被引:25
作者
Nagrath, D [1 ]
Prasad, V [1 ]
Bequette, BW [1 ]
机构
[1] Rensselaer Polytech Inst, Howard P Isermann Dept Chem Engn, Troy, NY 12180 USA
基金
美国国家科学基金会;
关键词
process control; systems engineering; optimization; dynamic simulation; model predictive control; unstable cascade systems;
D O I
10.1016/S0009-2509(01)00398-0
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Cascade control is commonly used in the operation of chemical processes to reject disturbances that have a rapid effect on a secondary measured state, before the primary measured variable is affected. In this paper, we develop a state estimation-based model predictive control approach that has the same general philosophy of cascade control (taking advantage of secondary measurements to aid disturbance rejection), with the additional advantage of the constraint handling capability of model predictive control (MPC). State estimation is achieved by using a Kalman filter and appending modeled disturbances as augmented states to the original system model. The example application is an open-loop unstable jacketed exothermic chemical reactor, where the jacket temperature is used as a secondary measurement in order to infer disturbances in jacket feed temperature and/or reactor feed flow rate. The MPC-based cascade strategy yields significantly etter performance than classical cascade control when operating close to constraints on the jacket flow rate. (C) 2002 Published by Elsevier Science Ltd.
引用
收藏
页码:365 / 378
页数:14
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