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U.S. Department of Energy
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Biological conversion of biomass to methane. Quarterly progress report

Technical Report ·
DOI:https://doi.org/10.2172/5245027· OSTI ID:5245027
Progress in comparative studies of complete-mix and multi-stage reactors for use in the anaerobic fermentation of organic solids for methane production is reported. Results indicate that if a balanced population of organisms can be maintained in the initial stage, multi-stage fermentation is more efficient than a complete-mix system. However, if the system is stressed, failure of the multi-staged system is more rapid. When the first stage is not inhibited due to a short retention time, the waste stabilization in the additional stages is minimal. Further studies on the effect of retention time on reaction rates indicate that the type of reactor design desired will depend upon the objective of the system. If it is desired to maximize the conversion of solids to methane, a staged system will produce more methane per unit volume of reactor for a given quantity of substrate. If the objective is to maximize methane production per unit volume of reactor, a single-stage reactor operating at near the minimum retention is required. Results of studies on the fermentation of manures and corn stover are discussed briefly. (JGB)
Research Organization:
Illinois Univ., Urbana (USA). Dept. of Civil Engineering
Sponsoring Organization:
USDOE
OSTI ID:
5245027
Report Number(s):
COO/2917-7
Country of Publication:
United States
Language:
English