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...
| Main Authors: | , , , , |
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| Format: | Journal Article |
| Published: |
Elsevier Ltd.
2015
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| Subjects: | |
| Online Access: | http://hdl.handle.net/20.500.11937/13423 |