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Journal article

Kinetics of propionate conversion in anaerobic continuously stirred tank reactors

From

Bioenergy and Biomass, Biosystems Division, Risø National Laboratory for Sustainable Energy, Technical University of Denmark1

Biosystems Division, Risø National Laboratory for Sustainable Energy, Technical University of Denmark2

Risø National Laboratory for Sustainable Energy, Technical University of Denmark3

Department of Systems Biology, Technical University of Denmark4

The kinetic parameters of anaerobic propionate degradation by biomass from 7 continuously stirred tank reactors differing in temperature, hydraulic retention time and substrate composition were investigated. In substrate-depletion experiments (batch) the maximum propionate degradation rate, A(max), and the half saturation constant, K-m, were initially estimated by applying the integrated Michaelis-Menten equation.

A(max) was in the range from 22.8 to 29.1 mu mol gVS(-1) h(-1) while K-m, was in the range from 0.46-0.95 mM. In general, A(max) gave a good reflection of the reactor performances. Secondly, the accuracy of the applied method was evaluated by use of radiotracer methodology. A(max) was found to be 14-157 lower in the substrate-depletion experiment than in the radioisotope experiment due to endogenous propionate production.

By including the endogenous propionate production, a 42-49% lower K-m, was estimated. The results demonstrate that the rate of endogenous substrate (propionate) production should be taken into account when estimating kinetic parameters in biomass from manure-based anaerobic reactors.

Language: English
Year: 2008
Pages: 151-160
ISSN: 1479487x and 09593330
Types: Journal article
DOI: 10.1080/09593330802028535
Keywords

Bioenergi

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