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Indexed by:Journal Papers

Date of Publication:2015-08-01

Journal:JOURNAL OF PROCESS CONTROL

Included Journals:SCIE、EI、Scopus

Volume:32

Page Number:1-9

ISSN No.:0959-1524

Key Words:Nonlinear systems; Multistage dynamic systems; Optimal control; Fed-batch fermentation; Total variation

Abstract: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.