Simultaneous model identification and optimization in presence of model-plant mismatch

被引:30
作者
Mandur, Jasdeep S. [1 ]
Budman, Hector M. [1 ]
机构
[1] Univ Waterloo, Dept Chem Engn, Waterloo, ON N2L 3G1, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Model based optimization; Run-to-run optimization; Batch processes; Model correction; Modelling for optimization; Model plant mismatch; REAL-TIME OPTIMIZATION; DYNAMIC OPTIMIZATION; PENICILLIN PRODUCTION; UNCERTAINTY; STRATEGIES; DIVERGENCE; OPERATION; EFFICIENT; DESIGN; SYSTEM;
D O I
10.1016/j.ces.2015.02.038
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In a standard optimization approach, the underlying process model is first identified at a given se of operating conditions and this updated model is, then, used to calculate the optimal conditions for the process. This "two-step" procedure can be repeated iteratively by conducting new experiments at optimal operating conditions, based on previous iterations, followed by re-identification and re optimization until convergence is reached. However, when there is a model plant mismatch, the set of parameter estimates that minimizes the prediction error in the identification problem may not predict the gradients of the optimization objective accurately. As a result, convergence of the "two-step" iterative approach to a process optimum cannot be guaranteed. This paper presents a new methodology where the model outputs are corrected explicitly for the mismatch such that, with the updated parameter estimates the identification and optimization objectives are properly reconciled. With the proposed corrections being progressively integrated over the iterations, the algorithm has guaranteed convergence to the process optimum and also, upon convergence, the final corrected model predicts the process behavior accurately. The proposed methodology is illustrated in a run-to-run optimization framework with a fed batch bioprocess as a case study. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:106 / 115
页数:10
相关论文
共 30 条
[1]  
[Anonymous], AICHE S SER
[2]  
BAJPAI RK, 1980, J CHEM TECHNOL BIOT, V30, P332
[3]   Dynamic optimization of bioprocesses: Efficient and robust numerical strategies [J].
Banga, JR ;
Balsa-Canto, E ;
Moles, CG ;
Alonso, AA .
JOURNAL OF BIOTECHNOLOGY, 2005, 117 (04) :407-419
[4]  
Bard Y., 1974, NONLINEAR PARAMETER
[5]   Distributions of the Kullback-Leibler divergence with applications [J].
Belov, Dmitry I. ;
Armstrong, Ronald D. .
BRITISH JOURNAL OF MATHEMATICAL & STATISTICAL PSYCHOLOGY, 2011, 64 (02) :291-309
[6]   Robust optimization - A comprehensive survey [J].
Beyer, Hans-Georg ;
Sendhoff, Bernhard .
COMPUTER METHODS IN APPLIED MECHANICS AND ENGINEERING, 2007, 196 (33-34) :3190-3218
[7]   A modular simulation package for fed-batch fermentation:: penicillin production [J].
Birol, G ;
Ündey, C ;
Çinar, A .
COMPUTERS & CHEMICAL ENGINEERING, 2002, 26 (11) :1553-1565
[8]  
Brdy M, 1994, P 1 IFAC WORKSH NEW, P249
[9]   Adaptation strategies for real-time optimization [J].
Chachuat, B. ;
Srinivasan, B. ;
Bonvin, D. .
COMPUTERS & CHEMICAL ENGINEERING, 2009, 33 (10) :1557-1567
[10]   ONLINE OPTIMIZATION USING A 2-PHASE APPROACH - AN APPLICATION STUDY [J].
CHEN, CY ;
JOSEPH, B .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (09) :1924-1930