Multivariate statistical process control of an industrial-scale fed-batch simulator

被引:15
|
作者
Duran-Villalobos, Carlos A. [1 ]
Goldrick, Stephen [2 ]
Lennox, Barry [1 ]
机构
[1] Univ Manchester, Sch Elect & Elect Engn, Manchester M13 9PL, Lancs, England
[2] UCL, Dept Biochem Engn, London WC1E 6BT, England
基金
英国工程与自然科学研究理事会;
关键词
Optimal control; Batch to batch optimisation; Model predictive control; Data-driven modelling; Missing data methods; Partial least square regression; MODEL-PREDICTIVE CONTROL; PARTIAL LEAST-SQUARES; PRODUCT QUALITY; ENSURING VALIDITY; RUN OPTIMIZATION; ADAPTIVE-CONTROL; MISSING DATA; PLS; FERMENTATION; REACTORS;
D O I
10.1016/j.compchemeng.2019.106620
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
This article presents an improved batch-to-batch optimisation technique that is shown to be able to bring the yield closer to its set-point from one batch to the next. In addition, an innovative Model Predictive Control technique is proposed that over multiple batches, reduces the variability in yield that occurs as a result of random variations in raw material properties and in-batch process fluctuations. The proposed controller uses validity constraints to restrict the decisional space to that described by the identification dataset that was used to develop an adaptive multi-way partial least squares model of the process. A further contribution of this article is the formulation of a bootstrap calculation to determine confidence intervals within the hard constraints imposed on model validity. The proposed control strategy was applied to a realistic industrial-scale fed-batch penicillin simulator, where its performance was demonstrated to provide improved consistency and yield when compared with nominal operation. Crown Copyright (C) 2019 Published by Elsevier Ltd.
引用
收藏
页数:13
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