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Wiley InterScience

FEMS Yeast Research

FEMS Yeast Research

Volume 5 Issue 10, Pages 925 - 934

Published Online: 7 Apr 2006

© 2010 Federation of European Microbiological Societies. Published by Blackwell Publishing Ltd. All rights reserved



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Evolutionary engineering of mixed-sugar utilization by a xylose-fermenting Saccharomyces cerevisiae strain
Marko Kuyper a , Maurice J. Toirkens a , Jasper A. Diderich a , Aaron A. Winkler b , Johannes P. van Dijken a, b , Jack T. Pronk a, *
  a Department of Biotechnology, Delft University of Technology, Julianalaan 67, 2628 BC Delft, The Netherlands   b Bird Engineering B.V., Westfrankelandseweg 1, 3115 HG Schiedam, The Netherlands
  *Corresponding author. Fax: +31 15 2782355., E-mail address: j.t.pronk@tnw.tudelft.nl
Copyright 2005 Federation of European Microbiological Societies
KEYWORDS
Xylose isomerase • Piromyces • Fermentation • Pentose • Yeast • Bioethanol • Pentose phosphate pathway • Lignocellulose • Metabolic engineering • Evolutionary engineering

ABSTRACT

We have recently reported about a Saccharomyces cerevisiae strain that, in addition to the Piromyces XylA xylose isomerase gene, overexpresses the native genes for the conversion of xylulose to glycolytic intermediates. This engineered strain (RWB 217) exhibited unprecedentedly high specific growth rates and ethanol production rates under anaerobic conditions with xylose as the sole carbon source. However, when RWB 217 was grown on glucose–xylose mixtures, a diauxic growth pattern was observed with a relatively slow consumption of xylose in the second growth phase. After prolonged cultivation in an anaerobic, xylose-limited chemostat, a culture with improved xylose uptake kinetics was obtained. This culture also exhibited improved xylose consumption in glucose–xylose mixtures. A further improvement in mixed-sugar utilization was obtained by prolonged anaerobic cultivation in automated sequencing-batch reactors on glucose–xylose mixtures. A final single-strain isolate (RWB 218) rapidly consumed glucose–xylose mixtures anaerobically, in synthetic medium, with a specific rate of xylose consumption exceeding 0.9 g g−1 h−1. When the kinetics of zero trans-influx of glucose and xylose of RWB 218 were compared to that of the initial strain, a twofold higher capacity (Vmax) as well as an improved Km for xylose was apparent in the selected strain. It is concluded that the kinetics of xylose fermentation are no longer a bottleneck in the industrial production of bioethanol with yeast.


Received 9 March 2005, Revised 15 April 2005, Accepted 20 April 2005

DIGITAL OBJECT IDENTIFIER (DOI)
10.1016/j.femsyr.2005.04.004 About DOI

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