by Yutaka YONEYAMA, Shigemi OKADA, Naohide MATSUMOTO, Ayako IGARASHI, & Akihiro NAKAMURA
In order to establish the feasibility of methane fermentation for treating low organic concentration wastewater, a pilot-scale UASB reactor was operated under an unheated condition over 631 days by seeding mesophilic sewage digested sludge and by feeding with a municipal wastewater. The pilot-scale UASB reactor had a treatment capacity of 50 m3/d, an effective capacity of 20.2 m3 and a net depth of 5 m. The result obtained from a continuous experiment indicated a stable treatment, i.e. , between 397-631 days after the startup. The mean values obtained during this time indicated a biogas generation of 2.4 m3/d, methane gas composition of 70.5%, CODCr removal of 63.8% at water temperature of 23.8℃, CODCr volumetric load of 0.99 kg-CODCr / (m3·d), and CODCr sludge load of 0.12 kg-CODCr /(kg-MLVSS·d).
Keywords
UASB, Unheated condition, Municipal wastewater, Sewage, HRT (Hydraulic Retention Time), CODCr (Chemical Oxygen Demand), Methane, Biogas production rate, Granule