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Long-term competition between sulfate reducing and methanogenic bacteria in UASB reactors treating volatile fatty
1Department of Environmental Technology, Agricultural University of Wageningen, "Biotechnion," Bomenweg 2, P.O. Box 8129, 6700 EV Wageningen, The Netherlands.
Biotechnology and Bioengineering
|April 1, 1999
Summary
Sulfate-reducing bacteria (SRB) outcompete methane-producing bacteria (MB) for acetate when sulfate is in excess. Reactor conditions like high pH and short solid retention time can accelerate this shift in microbial dominance.
Area of Science:
- * Environmental microbiology
- * Anaerobic digestion
- * Microbial ecology
Background:
- * Competition between methane-producing bacteria (MB) and sulfate-reducing bacteria (SRB) is crucial in anaerobic digestion.
- * Acetate is a key substrate utilized by both MB and SRB.
- * Understanding this competition impacts wastewater treatment and biogas production.
Purpose of the Study:
- * To investigate the competition for acetate between MB and SRB in upflow anaerobic sludge bed (UASB) reactors.
- * To determine the influence of COD:sulfate ratio on microbial dominance.
- * To model the long-term dynamics of this microbial competition.
Main Methods:
- * Operation of mesophilic UASB reactors treating volatile fatty acids (VFA) or acetate with varying COD:sulfate ratios.
- * Evaluation of acetate utilization partitioning based on conversion rates and microbial activities.
- * Dynamic simulations using a mathematical model with Monod kinetics.
Main Results:
- * A COD:sulfate ratio below 0.67 favored SRB dominance over MB.
- * Prolonged operation (250-400 days) was required for SRB to utilize 90% of acetate.
- * Mathematical modeling confirmed the long-term nature of acetate competition.
Conclusions:
- * High sulfate conditions shift acetate utilization towards SRB.
- * Reactor operational parameters (pH, solid retention time) and inoculum composition influence competition dynamics.
- * Optimizing conditions can accelerate SRB outcompetition of MB for acetate.