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
相关论文
共 33 条
  • [21] Distributional uncertainty analysis using power series and polynomial chaos expansions
    Nagy, Z. K.
    Braatz, R. D.
    [J]. JOURNAL OF PROCESS CONTROL, 2007, 17 (03) : 229 - 240
  • [22] Robust nonlinear model predictive control of batch processes
    Nagy, ZK
    Braatz, RD
    [J]. AICHE JOURNAL, 2003, 49 (07) : 1776 - 1786
  • [23] A NOVEL FLEXIBILITY ANALYSIS APPROACH FOR PROCESSES WITH STOCHASTIC PARAMETERS
    PISTIKOPOULOS, EN
    MAZZUCHI, TA
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 1990, 14 (09) : 991 - 1000
  • [24] Rossi F, 2015, COMPUT-AIDED CHEM EN, V37, P1517
  • [25] Online model-based optimization and control for the combined optimal operation and runaway prediction and prevention in (fed-)batch systems
    Rossi, Francesco
    Copelli, Sabrina
    Colombo, Andrea
    Pirola, Carlo
    Manenti, Flavio
    [J]. CHEMICAL ENGINEERING SCIENCE, 2015, 138 : 760 - 771
  • [26] Rossi F, 2014, COMPUT-AIDED CHEM EN, V33, P745
  • [27] A Novel All-in-One Real-Time Optimization and Optimal Control Method for Batch Systems: Algorithm Description, Implementation Issues, and Comparison with the Existing Methodologies
    Rossi, Francesco
    Manenti, Flavio
    Buzzi-Ferraris, Guido
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2014, 53 (40) : 15639 - 15655
  • [28] Multi-stage scenario generation by the combined moment matching and scenario reduction method
    Rubasheuski, Uladzimir
    Oppen, Johan
    Woodruff, David L.
    [J]. OPERATIONS RESEARCH LETTERS, 2014, 42 (05) : 374 - 377
  • [29] Schildbach G, 2015, P AMER CONTR CONF, P415, DOI 10.1109/ACC.2015.7170771
  • [30] Dynamic optimization of batch processes - II. Role of measurements in handling uncertainty
    Srinivasan, B
    Bonvin, D
    Visser, E
    Palanki, S
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2003, 27 (01) : 27 - 44