The concept of loss of cell viability was introduced into a model previousl
y developed for a continuous alcoholic fermentation process in a tower reac
tor with recycling of flocculating yeasts. The two models take into account
substrate limitation and inhibition phenomena linked to ethanol and biomas
s. The kinetic parameters were estimated from steady-state data of several
sugar concentrations in feeding stream and constant dilution Fate, recycle
ratio and temperature. Some parameters of the modified model (maximum speci
fic rates) were significantly different from those estimated with the origi
nal model while others (inhibition parameters) remained practically unchang
ed. Both models provided similar predictions and were equally suitable for
modelling of the process.