Nonlinear Model Predictive Control: A Self-Adaptive Approach

被引:24
作者
Dones, Ivan [2 ]
Manenti, Flavio [1 ]
Preisig, Heinz A. [2 ]
Buzzi-Ferraris, Guido [1 ]
机构
[1] Politecn Milan, CMIC Dept Giulio Natta, I-20133 Milan, Italy
[2] NTNU, Dept Chem Engn, N-7491 Trondheim, Norway
关键词
OPTIMIZING CONTROL; PATH OPTIMIZATION; GRADE TRANSITION; MULTIPLE MODEL; STRATEGY; IDENTIFICATION; PERSPECTIVES; REDUCTION; OPERATION; SYSTEMS;
D O I
10.1021/ie901693w
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Model predictive control (MPC) is an online application based on dynamic models. Its application faces two major obstacles: (i) computational constraints and (ii) the need to accurately simulate the process by a model that properly predicts how the plant will behave in the future. Implementation of MPC is not always possible in large-scale or industrial applications due to the computational complexity of MPC and to the dimensionality of the models. To facilitate MPC implementations, this paper proposes a self-adaptive approach based on simplified (or reduced-order) nonlinear models. The proposed methodology yields an MPC that adjusts the dimension of the model according to both the current process conditions and the control objectives. The self-adaptive approach is described and validated on an industrial case study, a C4-splitter.
引用
收藏
页码:4782 / 4791
页数:10
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