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Distributed parameter model of an airlift fermentor
Author(s) -
Merchuk Jose C.,
Stein Y.,
Mateles R. I.
Publication year - 1980
Publication title -
biotechnology and bioengineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 1.136
H-Index - 189
eISSN - 1097-0290
pISSN - 0006-3592
DOI - 10.1002/bit.260220607
Subject(s) - airlift , separator (oil production) , fermentation , plug flow , biomass (ecology) , volumetric flow rate , flow (mathematics) , process engineering , mixing (physics) , mechanics , oxygen , bioreactor , chemistry , environmental science , materials science , thermodynamics , engineering , physics , ecology , biology , food science , organic chemistry , quantum mechanics
A distributed parameter model for an airlift fermentor is presented. A riser represents the airlift fermentor, with plug flow in both gas and liquid phases, a well‐mixed section that acts as gas separator, and a downcomer with plug flow. The set of equations proposed makes possible both the understanding and design of the system. Macroscopic balances shows a behavior that is very close to conventional continuous stirred tank fermentor from the viewpoint of biomass production. In addition, the model predicts concentration profiles of biomass, substrate and oxygen in the liquid, and oxygen in the gas phase. This allows estimation of optimal gas flow rate for sufficient oxygen transfer with minimum energy input.