Optimal Control of a Fed-Batch Fermentation Involving Multiple Feeds

Optimal Control of a Fed-Batch Fermentation Involving Multiple Feeds

A nonlinear dynamical system, in which the feed rates of glycerol and alkali are taken as the control functions, is first proposed to formulate the fed-batch culture of 1,3-propanediol (1,3-PD) production. To maximize the 1,3-PD concentration at the terminal time, a constrained optimal control model...

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Bibliographic Details
Main Authors: Chongyang Liu, Zhaohua Gong, Zhaoyi Huo, Bangyu Shen
Format: Article
Language:English
Published: Wiley 2012-01-01
Series:Journal of Applied Mathematics
Online Access:http://dx.doi.org/10.1155/2012/245315
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