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...
| Main Authors: | , , , |
|---|---|
| Format: | Article |
| Sprog: | English |
| Udgivet: |
Hindawi Limited
2012-01-01
|
| Serier: | Journal of Applied Mathematics |
| Online adgang: | http://dx.doi.org/10.1155/2012/245315 |