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Fate of sulfate during the thermophilic methane fermentation process

Thesis/Dissertation ·
OSTI ID:6914754
The reactor design utilized was the suspended growth thermophilic anaerobic contact system. The experimental program was divided into four separate investigations which included sulfate interaction in continuously fed contact reactors, sulfide-pH speciation effects, metal control of sulfide precipitation, and maximum kinetic measurements. During continuous fermenter operation, negligible effluent sulfate levels indicated that complete reduction of sulfate occurred with influent loadings up to 80 mg/l-d SO/sub 4//sup -2/-S. Comparison of the maximum sulfate reduction rate obtained during batch digestion to the maximum specific sulfate loading rate during continuous flow operation illustrated that sulfate reduction kinetics were nonlimiting, and thus, responsible for complete removal of sulfate. By proper pH maintenance, stable reactor conditions were obtained during the entire range of influent sulfate concentrations tested. However, as the influent SO/sub 4//sup -2/-S/COD ratio was increased from 0.003 to 0.08, the methane production rate decreased by 60% (from 0.26 to 0.11 l CH/sub 4//L-day), and volatile acid concentrations increased from 200 to 4500 mg/l acetate. Significant inhibition of thermophilic methanogenesis appeared at a soluble sulfide concentration greater than 120 mg/l sulfide-sulfur. Sulfide speciation was sensitive to variations in fermenter pH. Insoluble iron phosphate additions were an efficient gaseous sulfide control process with no adverse effects on methane production.
Research Organization:
Cornell Univ., Ithaca, NY (USA)
OSTI ID:
6914754
Country of Publication:
United States
Language:
English