Innovative method for increased methane recovery from two-phase anaerobic digestion of food waste through reutilization of acidogenic off-gas in methanogenic reactor

•Two-phase AD with acidogenic gas diversion from LBR to UASB increased CH4 recovery.•Acidogenic gas diversion increased the COD by 27% and CH4 recovery by 38.6%.•Acidogenic gas utilization contributes ∼8% increase in CH4 recovery.•Mixed acid fermentation dominated by butyrate was observed with gas d...

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Veröffentlicht in:Bioresource technology 2016-10, Vol.217, p.3-9
Hauptverfasser: Yan, Bing Hua, Selvam, Ammaiyappan, Wong, Jonathan W.C.
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Sprache:eng
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Zusammenfassung:•Two-phase AD with acidogenic gas diversion from LBR to UASB increased CH4 recovery.•Acidogenic gas diversion increased the COD by 27% and CH4 recovery by 38.6%.•Acidogenic gas utilization contributes ∼8% increase in CH4 recovery.•Mixed acid fermentation dominated by butyrate was observed with gas diversion. In this study, the performance of a two-phase anaerobic digestion reactor treating food waste with the reutilization of acidogenic off-gas was investigated with the objective to improve the hydrogen availability for the methanogenic reactor. As a comparison a treatment without off-gas reutilization was also set up. Results showed that acidogenic off-gas utilization in the upflow anaerobic sludge blanket (UASB) reactor increased the methane recovery up to 38.6%. In addition, a 27% increase in the production of cumulative chemical oxygen demand (COD) together with an improved soluble microbial products recovery dominated by butyrate was observed in the acidogenic leach bed reactor (LBR) with off-gas reutilization. Of the increased methane recovery, ∼8% was contributed by the utilization of acidogenic off-gas in UASB. Results indicated that utilization of acidogenic off-gas in methanogenic reactor is a viable technique for improving overall methane recovery.
ISSN:0960-8524
1873-2976
DOI:10.1016/j.biortech.2016.03.116