Abstract

BackgroundSimultaneous co-fermentation of mixed sugars is an important feature to consider in the production of ethanol from lignocellulosic biomass hydrolysates because it enhances the overall ethanol yield and volumetric productivity during fermentation. Continuous cultures can be used during ethanol production from lignocellulosic hydrolysates to prevent catabolite repression by glucose on other sugars, such as xylose, and thus promote the simultaneous and total consumption of sugars and reduce fermentation time. The use of single- and two-stage continuous cultures under micro-aerated conditions for simultaneous consumption of xylose and glucose, and fermentation to ethanol by ethanologenic Escherichia coli strain MS04 was studied. Mineral medium supplemented with glucose, xylose and sodium acetate, was used to compare continuous cultures performance to batch cultures.ResultsSingle-stage continuous cultures under micro-aerated conditions allowed the total co-consumption of a mixture of glucose and xylose (7.5 and 42.5 g/L, respectively) in mineral medium, with steady state ethanol production of 18 g/L, and a volumetric ethanol productivity of 0.9 g/L h, when low dilution rates (0.05 h−1) were used. However, the volumetric productivity was lower than the batch process under similar conditions (1.3 g/L h). Conversely, micro-aerated two-stage continuous culture enhanced the volumetric productivity up to 1.6 g/L h at a dilution rate of 0.15 h−1, with a total consumption of sugars and a slight reduction of the overall ethanol yield.ConclusionsThe total and simultaneous consumption of glucose and xylose by the ethanologenic E. coli strain MS04 was accomplished by using two-stage continuous culture under micro-aerated conditions with an increase in the volumetric ethanol productivity of 23% and 78% when compared to batch and single-stage continuous cultures, respectively. Multi-stage continuous cultivation can be used to promote the simultaneous consumption of all sugars contained in biomass hydrolysates, and thus increase the volumetric ethanol productivity of the fermentation process.

Highlights

  • Simultaneous co-fermentation of mixed sugars is an important feature to consider in the production of ethanol from lignocellulosic biomass hydrolysates because it enhances the overall ethanol yield and volumetric productivity during fermentation

  • The results showed that two-stage continuous culture was better than batch and single-stage continuous culture regarding the volumetric ethanol productivity by ethanologenic E. coli MS04, promoting the simultaneous and total consumption of pentose and hexose sugars to potentially produce second-generation bioethanol (SGB)

  • D dilution rate, μ specific growth rate, YPS ethanol yield on sugars consumed as percentage of the maximum theoretical; YXS biomass yield on sugars consumed, QP volumetric ethanol productivity, qP specific ethanol productivity such as strains of E. coli and S. cerevisiae, growing in batch culture on synthetic media supplemented with xylose or glucose/xylose mixtures [39,40,41,42,43]

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Summary

Introduction

Simultaneous co-fermentation of mixed sugars is an important feature to consider in the production of ethanol from lignocellulosic biomass hydrolysates because it enhances the overall ethanol yield and volumetric productivity during fermentation. Several microorganisms, such as yeasts and bacteria have been isolated or genetically modified, like Escherichia coli, Saccharomyces cerevisiae and Zymomonas mobilis, among others, to generate new biocatalysts capable to consume pentose and hexose sugar mixtures, for efficiently producing SGB [19,20,21,22,23] For such purpose, E. coli shows several advantages, such as efficient consumption of hexoses and pentoses present in the hemicellulosic hydrolysates [24, 25] and high tolerance to various toxic compounds [9, 19, 22, 26]. This phenomenon limits ethanol titer, overall yield, and productivity [7, 13, 25, 28]

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