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doi:10.1016/S0959-1524(96)00023-6    
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Copyright © 1997 Published by Elsevier Science Ltd.

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Interpolating optimizing process control

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Bjarne A. FossE-mail The Corresponding Author, a, and S. Joe QinE-mail The Corresponding Author, b

a Department of Engineering Cybernetics, Norwegian University of Science and Technology, Norway

b Department of Chemical Engineering, The University of Texas at Austin, USA


Received 2 April 1996; 
revised 23 September 1996. 
Available online 7 May 1998.

Abstract

A new model-based optimizing controller for a set of nonlinear systems is proposed. The nonlinear model set is based on a convex combination of two bounding linear models. An optimal control sequence is computed for each of the two bounding models. The proposed control algorithm is based on a convex combination of the two control sequences. A novel feature in these two optimizations is an added constraint related to the feasibility of the ‘other’ bounding model. The control algorithm can for example be used in model predictive control. We provide robust feasibility guarantees and an upper bound on the optimal criterion if the bounding models are linear FIR models. Further, simulation examples demonstrate significant feasibility improvements in the case where the bounding models are general linear state-space models. The proposed method guarantees robust feasibility for a 1-step ahead prediction in the general case. This can be of interest in MPC applications.

Author Keywords: model-based control; optimization; convexity; model predictive control; nonlinear systems; robustness; interpolation

Article Outline

• References

On sabbatical leave at The Department of Chemical Engineering, The University of Texas at Austin, USA


 
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