Abstract

A two-stage continuous fermentation process, using a continuous stirred tank fermenter (CSTF) and a tower fermenter (TF) connected in series, has been studied for ethanol production from d-glucose. The addition of a protein-phospholipid complex as a protective agent (PA) in the TF led to a three-fold increase in ethanol productivity and a 23.63% increase in final ethanol concentration in the tower effluent. The results are consistent with our previous findings on a cascade operation of CSTFs, namely, that the addition of PA to the tower increases cell tolerance towards ethanol at ethanol concentrations up to 70 gl −1. Both studies indicate that beyond this experimentally determined critical ethanol concentration, ethanol production is significantly inhibited. Mathematical modelling of the behaviour of a single flocculated yeast floc suggested that, for yeast flocs up to 1 mm diameter, neither internal nor external diffusion of substrate is limiting. Therefore, a simplified mathematical method was developed for the analysis of the TF system. By plotting the calculated values from the derived performance equation and the experimental values of substrate conversion vs. residence time, good agreement was obtained between these two for the addition of PA. However, a small deviation was observed for the PA-free system.

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