Design of Dynamic Experiments in Modeling for Optimization of Batch Processes

被引:20
作者
Martinez, Ernesto C. [1 ]
Cristaldi, Mariano D. [2 ]
Grau, Ricardo J. [2 ]
机构
[1] INGAR CONICET UTN, RA-3002 Santa Fe, GJC, Argentina
[2] INTEC CONICET UNL, RA-3000 Santa Fe, Argentina
关键词
D O I
10.1021/ie8000953
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Finding optimal operating conditions fast with a scarce budget of experimental runs is a key problem to speeding up the development of innovative products and processes. Modeling for optimization is proposed as a systematic approach to bias data gathering for iterative policy improvement through experimental design using first-principles models. Designing dynamic experiments that are optimally informative in order to reduce the uncertainty about the optimal operating conditions is addressed by integrating policy iteration based on the Hamilton-Jacobi-Bellman optimality equation with global sensitivity analysis. A conceptual framework for run-to-run convergence of a model-based policy iteration algorithm is proposed. Results obtained in the fed-batch fermentation of penicillin G are presented. The well-known Baijpai and Reuss bioreactor model validated with industrial data is used to increase on a run-to-run basis the amount of penicillin obtained by input policy optimization and selective (re)estimation of relevant model parameters. A remarkable improvement in productivity can be gain using a simple policy structure after only two modeling runs despite initial modeling uncertainty.
引用
收藏
页码:3453 / 3465
页数:13
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