Multi-Scenario Robust Online Optimization and Control of Fed-Batch Systems via Dynamic Model-Based Scenario Selection

被引:15
|
作者
Rossi, Francesco [1 ,2 ]
Reklaitis, Gintaras [1 ]
Manenti, Flavio [2 ]
Buzzi-Ferraris, Guido [2 ]
机构
[1] Purdue Univ, Sch Chem Engn, Forney Hall Chem Engn,480 Stadium Mall Dr, W Lafayette, IN 47907 USA
[2] Politecn Milan, Dipartimento Chim Mat & Ingn Chim Giulio Natta, Piazza Leonardo da Vinci 32, I-20123 Milan, Italy
关键词
process control; optimization; stochastic programming; robust optimal control; PREDICTIVE CONTROL; FLEXIBILITY ANALYSIS; (FED-)BATCH SYSTEMS; UNCERTAINTY; IMPLEMENTATION; GENERATION; FRAMEWORK; REACTOR;
D O I
10.1002/aic.15346
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The manuscript proposes a novel robust methodology for the model-based online optimization/optimal control of fed-batch systems, which consists of two different interacting layers executed asynchronously. The first iteratively computes robust control actions online via multi-scenario stochastic optimization while the second iteratively re-estimates the optimal scenario map after every single/every certain number of control action/actions. The novelty of the approach is twofold: (I) the scenario map is optimally computed/updated based on probabilistic information on the process model uncertainty as well as the sensitivity of the controlled system to the uncertain parameters; and (II) the scenario set is dynamically re-estimated, thus accounting for the effect of disturbances and changes in the operating conditions of the target process. The proposed approach is applied to a fed-batch Williams-Otto process and compared to an existing multi-scenario optimization/control algorithm as well as a non-robust optimization/control strategy to draw conclusions about which method is more effective. (C) 2016 American Institute of Chemical Engineers
引用
收藏
页码:3264 / 3284
页数:21
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