Continuous production of butanol by Clostridium acetobutylicum immobilized in a fibrous bed bioreactor

Appl Biochem Biotechnol. 2004 Spring:113-116:887-98. doi: 10.1385/abab:115:1-3:0887.

Abstract

We explored the influence of dilution rate and pH in continuous cultures of Clostridium acetobutylicum. A 200-mL fibrous bed bioreactor was used to produce high cell density and butyrate concentrations at pH 5.4 and 35degreesC. By feeding glucose and butyrate as a cosubstrate, the fermentation was maintained in the solventogenesis phase, and the optimal butanol productivity of 4.6 g/(L h) and a yield of 0.42 g/g were obtained at a dilution rate of 0.9 h-1 and pH 4.3. Compared to the conventional acetone-butanol-ethanol fermentation, the new fermentation process greatly improved butanol yield, making butanol production from corn an attractive alternative to ethanol fermentation.

Publication types

  • Research Support, U.S. Gov't, Non-P.H.S.

MeSH terms

  • Acetone / chemistry
  • Bioreactors*
  • Biotechnology / methods*
  • Butanols / chemistry*
  • Butanols / metabolism*
  • Clostridium / metabolism*
  • Culture Media
  • Ethanol / pharmacology
  • Fermentation
  • Hydrogen-Ion Concentration
  • Kinetics
  • Temperature
  • Time Factors

Substances

  • Butanols
  • Culture Media
  • Acetone
  • Ethanol