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...
| المؤلفون الرئيسيون: | , , , |
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| التنسيق: | مقال |
| اللغة: | English |
| منشور في: |
Hindawi Limited
2012-01-01
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| سلاسل: | Journal of Applied Mathematics |
| الوصول للمادة أونلاين: | http://dx.doi.org/10.1155/2012/245315 |