Abstract
The technical feasibility of adopting the fixed-film reactor concept for biogas production from screened dairy manure was investigated. The methane production capability of laboratory-scale 4L anaerobic reactors (conventional and fixed-film) receiving screened dairy manure and operated at 35° was compared. Dairy manure filtrate with 4.4% TS and 3.4% VS (average value) was prepared from 1:1 manure/water slurry. The feed material was added itermittently at loading rates ranging from 2.34 to 25 and 2.25 to 778 g VS/L.d respectively for the conventional and fixed-film reactors. Maximum methane production rate (L.CH4/L.digester/day) for the conventional reactor was 0.63 L.CH4/L.d achieved at a 6 day hydraulic retention time (HRT). For the fixed-film reactor, the maximum production rate was 6.20 L.CH4/L.d when operated at a loading rate of 259 g.VS/L.d (3 hrs HRT). The fixed-film reactor was capable of sustaining a loading of 778 g.VS/L.d (1 hr. HRT). The fixed-film reactor performed much better than the conventional reactors. The average biogas methane content from the fixed-film reactor (65.8%) was always higher than from the conventional reactors (61.6%). These results indicate that a large reduction of required reactor volume is possible through application of a fixed-film concept.
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