A robust multi-model predictive controller for distributed parameter systems

被引:42
|
作者
Garcia, Miriam R. [1 ,2 ]
Vilas, Carlos [1 ]
Santos, Lino O. [3 ]
Alonso, Antonio A. [1 ]
机构
[1] IIM CSIC, Proc Engn Grp, Vigo 36208, Spain
[2] Natl Univ Ireland, Hamilton Inst, Maynooth, Kildare, Ireland
[3] Univ Coimbra, Fac Sci & Technol, Dept Chem Engn, CIEPQPF, P-3030790 Coimbra, Portugal
基金
爱尔兰科学基金会;
关键词
Plant model mismatch; Proper orthogonal decomposition; Controller stability; Projection methods; OPTIMAL ACTUATOR/SENSOR PLACEMENT; PROPER ORTHOGONAL DECOMPOSITION; FEEDBACK CONTROLLERS; COHERENT STRUCTURES; CONTROL STRATEGY; STABILITY; REDUCTION; MODELS; STATE; MPC;
D O I
10.1016/j.jprocont.2011.10.008
中图分类号
TP [自动化技术、计算机技术];
学科分类号
0812 ;
摘要
In this work a robust nonlinear model predictive controller for nonlinear convection-diffusion-reaction systems is presented. The controller makes use of a collection of reduced order approximations of the plant (models) reconstructed on-line by projection methods on proper orthogonal decomposition (POD) basis functions. The model selection and model update step is based on a sufficient condition that determines the maximum allowable process-model mismatch to guarantee stable control performance despite process uncertainty and disturbances. Proofs on the existence of a sequence of feasible approximations and control stability are given. Since plant approximations are built on-line based on actual measurements, the proposed controller can be interpreted as a multi-model nonlinear predictive control (MMPC). The performance of the MMPC strategy is illustrated by simulation experiments on a problem that involves reactant concentration control of a tubular reactor with recycle. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:60 / 71
页数:12
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