Coupling glucose fermentation and homoacetogenesis for elevated acetate production: Experimental and mathematical approaches.

Summary of "Coupling glucose fermentation and homoacetogenesis for elevated acetate production: Experimental and mathematical approaches."

Homoacetogenesis is an important potential hydrogen sink in acetogenesis, in which hydrogen is used to reduce carbon dioxide to acetate. So far the acetate production from homoacetogenesis, especially its kinetics, has not been given sufficient attention. In this work, enhanced production of acetate from anaerobic conversion of glucose through coupling glucose fermentation and homoacetogenesis is investigated with both experimental and mathematical approaches. Experiments are conducted to explore elevated acetate production in a coupled anaerobic system. Acetate production could be achieved by homoacetogenesis with a relative high acetate yield under mixed fermentation conditions. With the experimental observations, a kinetic model is formulated to describe such a homoacetogenic process. The maximum homoacetogenic rate (k(m,homo)) is estimated to be 28.5 +/- 1.7 kg COD kg(-1) COD d(-1) with an uptake affinity constant of 3.7x10(-5) +/- 3.1x10(-6) kg COD m(-3). The improved calculation of homoacetogenic kinetics by our approach could correct the underestimation of homoacetogenesis in anaerobic fermentation processes, as it often occurs in these systems supported by literature analysis. The model predictions match the experimental results in different cases well and provide insights into the dynamics of anaerobic glucose conversion and acetate production. Furthermore, acetate production via homoacetogenesis increases by about 40% through utilizing the fed-batch coupling system, attributed to a balance between the hydrogen production in the acetogenesis phase and the hydrogen consumption in the homoacetogenesis phase. This work provides an effective way for increased anaerobic acetate production, and gives us a better understanding about the homoacetogenic kinetics in the anaerobic fermentation process. (c) 2010 Wiley Periodicals, Inc.

Affiliation

Department of Chemistry, University of Science & Technology of China, Hefei, 230026, China.

Journal Details

This article was published in the following journal.

Name: Biotechnology and bioengineering
ISSN: 1097-0290
Pages:

Links

• PubMed Source: http://www.ncbi.nlm.nih.gov/pubmed/20803563
• DOI: http://dx.doi.org/10.1002/bit.22908