Safe-Steering of Batch Process Systems

被引:23
作者
Aumi, Siam [1 ]
Mhaskar, Prashant [1 ]
机构
[1] McMaster Univ, Dept Chem Engn, Hamilton, ON L8S 4L7, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
process control; control; safety; batch control; FAULT-TOLERANT CONTROL; PREDICTIVE CONTROL; ACTUATOR FAULTS; QUALITY PREDICTION; NONLINEAR-SYSTEMS; OPTIMAL-DESIGN; STABILIZATION; OPTIMIZATION; OPERATION; REACTORS;
D O I
10.1002/aic.11920
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
This work considers the problem of controlling batch processes to achieve a desired final product quality subject to input constraints and faults in the control actuators. Specifically, faults are considered that cannot be handled via robust control approaches, and preclude the ability to reach the desired end-point, necessitating fault-rectification. A safe-steering framework is developed to address the problem of determining how to utilize the functioning inputs during fault rectification to ensure that after fault-rectification, the desired product properties can be reached upon batch termination. To this end first a novel reverse-time reachability region (we define the reverse time reachability region as the set of states from where the desired end point can be reached by batch termination) based MPC is formulated that reduces online computations, as well as provides a useful tool for handling faults. Next, a safe-steering framework is developed that utilizes the reverse-time reachability region based MPC in steering the state trajectory during fault rectification to enable (upon fault recovery) the achieving of the desired end point properties by batch termination. The proposed controller and safe-steering framework are illustrated using a fed-batch process example. (C) 2009 American Institute of Chemical Engineers AIChE J, 55: 2861-2872, 2009
引用
收藏
页码:2861 / 2872
页数:12
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