A general model, previous proposed for entrapped-cell Rotating Biological Surface reactors provided with spongy supports has been improved to take into account limitations in mass transfer and substrate inhibition effects coming from increases in support surface per unit volume and in feed concentration, respectively.
Optimization study and modelling of an entrapped-cell contactor for alcohol fermentation
CONVERTI, ATTILIO;PEREGO, PATRIZIA;DEL BORGHI, MARCO
1990-01-01
Abstract
A general model, previous proposed for entrapped-cell Rotating Biological Surface reactors provided with spongy supports has been improved to take into account limitations in mass transfer and substrate inhibition effects coming from increases in support surface per unit volume and in feed concentration, respectively.
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