A dynamic model for the degradation of phenol in a two-phase partitioning bioreactor has been developed based on mechanistic balances around the bioreactor. The key process characteristics including substrate transfer between the organic and aqueous phases, substrate inhibition, oxygen limitation, a
Singular optimal control strategy for a fed-batch bioreactor: Numerical approach
β Scribed by Anil Menawat; R. Mutharasan; D. R. Coughanowr
- Publisher
- American Institute of Chemical Engineers
- Year
- 1987
- Tongue
- English
- Weight
- 649 KB
- Volume
- 33
- Category
- Article
- ISSN
- 0001-1541
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