Dynamic modeling and optimal fed-batch f
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Susan M. Cruickshank; Andrew J. Daugulis; P. James McLellan
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Article
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2000
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John Wiley and Sons
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English
β 162 KB
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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