Development of an industrial medium for economical 2,3-butanediol production through co-fermentation of glucose and xylose by Klebsiella oxytoca

Bioresour Technol. 2009 Nov;100(21):5214-8. doi: 10.1016/j.biortech.2009.05.036. Epub 2009 Jun 13.

Abstract

An industrial medium containing urea as a sole nitrogen source, low levels of corn steep liquor and mineral salts as nutrition factors to retain high 2,3-butanediol production through co-fermentation of glucose and xylose (2:1, wt/wt) by Klebsiella oxytoca was developed. Urea and corn steep liquor were identified as the most significant factors by the two-level Plackett-Burman design. Steepest ascent experiments were applied to approach the optimal region of the two factors and a central composite design was employed to determine their optimal levels. Under the optimal medium, the yield of 2,3-butanediol plus acetoin relative to glucose and xylose was up to 0.428 g/g, which was 85.6% of theoretical value. The cheap nitrogen source and nutrition factors combining the co-fermentation process using lignocellulose derived glucose and xylose as the carbon source in the developed medium would be a potential solution to improve the economics of microbial 2,3-butanediol production.

Publication types

  • Research Support, Non-U.S. Gov't

MeSH terms

  • Butylene Glycols / metabolism*
  • Culture Media / chemical synthesis*
  • Fermentation*
  • Glucose / metabolism*
  • Industry*
  • Klebsiella oxytoca / metabolism*
  • Models, Biological
  • Regression Analysis
  • Reproducibility of Results
  • Surface Properties
  • Time Factors
  • Xylose / metabolism*

Substances

  • Butylene Glycols
  • Culture Media
  • 2,3-butylene glycol
  • Xylose
  • Glucose