Optimal control of nonlinear fed-batch process using direct transcription method

被引:8
|
作者
Simorgh, Abolfazl [1 ]
Razminia, Abolhassan [1 ]
Tenreiro Machado, J. A. [2 ]
机构
[1] Persian Gulf Univ, Sch Engn, Dept Elect Engn, DSC Res Lab, Bushehr 75169, Iran
[2] Polytech Porto, ISEP Inst Engn, Dept Elect Engn, Rua Dr Antonio Bernardino Almeida, P-4249015 Porto, Portugal
关键词
Optimal control; Fed-batch reactors; Direct trapezoidal method; Smooth feed rate; Nonlinear programming; TRAJECTORY OPTIMIZATION;
D O I
10.1016/j.compchemeng.2019.106561
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
In this paper, we investigate the direct transcription method for dynamic optimization applied to fed-batch processes. The performance index proposed for optimization has a more general form than the classical ones. As a result, more design characteristics such as the minimum time, maximum production, desired production, and minimum energy are provided. As a matter of fact, abrupt changes in the feed profiles can lead to undesirable behaviors in bioprocesses, such as decreasing the productivity. To handle the mentioned drawback, a novel idea is presented that results in achieving smooth control policies by limiting the higher-order derivatives of the feed rates. Owing to the nonlinear model of the fed-batch processes, the presence of constraints and free final time analysis, the problem is reformulated as a nonlinear programming optimization by the direct trapezoidal method. Finally, the proposed method is applied to the invertase and PHB production processes and the effectiveness of the presented approach is demonstrated by comparing with several works in the literature. (C) 2019 Elsevier Ltd. All rights reserved.
引用
收藏
页数:11
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