Abstract

BackgroundSimultaneous saccharification and fermentation (SSF) is a promising process option for ethanol production from lignocellulosic materials. However, both the overall ethanol yield and the final ethanol concentration in the fermentation broth must be high. Hence, almost complete conversion of both hexoses and pentoses must be achieved in SSF at a high solid content. A principal difficulty is to obtain an efficient pentose uptake in the presence of high glucose and inhibitor concentrations. Initial glucose present in pretreated spruce decreases the xylose utilization by yeast, due to competitive inhibition of sugar transport. In the current work, prefermentation was studied as a possible means to overcome the problem of competitive inhibition. The free hexoses, initially present in the slurry, were in these experiments fermented before adding the enzymes, thereby lowering the glucose concentration.ResultsThis work shows that a high degree of xylose conversion and high ethanol yields can be achieved in SSF of pretreated spruce with a xylose fermenting strain of Saccharomyces cerevisiae (TMB3400) at 7% and 10% water insoluble solids (WIS). Prefermentation and fed-batch operation, both separately and in combination, improved xylose utilization. Up to 77% xylose utilization and 85% of theoretical ethanol yield (based on total sugars), giving a final ethanol concentration of 45 g L-1, were obtained in fed-batch SSF at 10% WIS when prefermentation was applied.ConclusionClearly, the mode of fermentation has a high impact on the xylose conversion by yeast in SSF. Prefermentation enhances xylose uptake most likely because of the reduced transport inhibition, in both batch and fed-batch operation. The process significance of this will be even greater for xylose-rich feedstocks.

Highlights

  • Simultaneous saccharification and fermentation (SSF) is a promising process option for ethanol production from lignocellulosic materials

  • In this work we only focus on glucose

  • (page number not for citation purposes) http://www.biotechnologyforbiofuels.com/content/2/1/8 studied in batch experiments at 7% water insoluble solids (WIS), and in both batch and fed-batch experiments at 10% WIS

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Summary

Introduction

Simultaneous saccharification and fermentation (SSF) is a promising process option for ethanol production from lignocellulosic materials. Both the overall ethanol yield and the final ethanol concentration in the fermentation broth must be high. Almost complete conversion of both hexoses and pentoses must be achieved in SSF at a high solid content. Simultaneous saccharification and fermentation (SSF) [1] has proved to be an interesting option for ethanol production from lignocellulosic materials [2]. At higher WIS contents, the concentrations of inhibitors and hexoses (inhibiting xylose uptake) will be higher. These effects will probably be less pronounced in fed-batch SSF compared with the simple batch mode

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