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论文类型：期刊论文

发表时间：2015-08-01

发表刊物：JOURNAL OF PROCESS CONTROL

收录刊物：SCIE、EI、Scopus

卷号：32

页面范围：1-9

ISSN号：0959-1524

关键字：Nonlinear systems; Multistage dynamic systems; Optimal control; Fed-batch fermentation; Total variation

摘要：This paper proposes a new optimal control model for the production of 1,3-propanediol (1,3-PD) via microbial fed-batch fermentation. The proposed model is governed by a nonlinear multistage dynamic system with two modes: feeding mode, in which glycerol and alkali substrates are added continuously to the fermentor; and batch mode, in which no substrates are added to the fermentor. The non-standard objective function incorporates both the final 1,3-PD yield and the cost of changing the input feeding rate, which is the control variable for the fed-batch fermentation process. Continuous state inequality constraints are imposed to ensure that the concentrations of biomass, glycerol, and reaction products lie within specified limits. Using the constraint transcription method, we approximate the continuous state inequality constraints by a conventional inequality constraint to yield an approximate parameter optimization problem. We then develop a combined particle swarm and gradient-based optimization algorithm to solve this approximate problem. The paper concludes with simulation results. (C) 2015 Elsevier Ltd. All rights reserved.