Kinetics of propionate conversion in anaerobic continuously stirred tank reactors

Environ Technol. 2008 Feb;29(2):151-60. doi: 10.1080/09593330802028535.

Abstract

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, Amax, and the half saturation constant, Km, were initially estimated by applying the integrated Michaelis-Menten equation. Amax was in the range from 22.8 to 29.1 micromol gVS(-1) h(-1) while Km was in the range from 0.46-0.95 mM. In general, Amax gave a good reflection of the reactor performances. Secondly, the accuracy of the applied method was evaluated by use of radiotracer methodology. Amax was found to be 14-15% 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 Km 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.

Publication types

  • Research Support, Non-U.S. Gov't

MeSH terms

  • Anaerobiosis*
  • Biodegradation, Environmental
  • Biomass
  • Bioreactors*
  • Equipment Design
  • Hydrolysis
  • Kinetics
  • Propionates / analysis*
  • Reproducibility of Results
  • Time Factors
  • Waste Disposal, Fluid / methods
  • Waste Management
  • Water Purification

Substances

  • Propionates