Optimal 1,3-propanediol production: Exploring the trade-off between process yield and feeding rate variation

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Optimal 1,3-propanediol production: Exploring the trade-off between process yield and feeding rate variation

This paper proposes a new optimal control model for the production of 1,3-propanediol (1,3-PD) viamicrobial fed-batch fermentation. The proposed model is governed by a nonlinear multi stage dynamic system with two modes: feeding mode, in which glycerol and alkali substrates are added continuously to...

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Bibliographic Details
Main Authors:	Wang, L., Lin, Qun, Loxton, Ryan, Teo, Kok Lay, Cheng, G.
Format:	Journal Article
Published:	Elsevier Ltd. 2015
Subjects:	Multistage dynamic systems Fed-batch fermentation Total variationa Nonlinear systems Optimal control
Online Access:	http://hdl.handle.net/20.500.11937/13423

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