Anaerobic Membrane Bioreactor Treatment of Synthetic Municipal Wastewater at Ambient Temperature

被引:63
作者
Ho, Jaeho [1 ]
Sung, Shihwu [2 ]
机构
[1] S Carolina Dept Hlth & Environm Control, Columbia, SC 29201 USA
[2] Iowa State Univ, Dept Civil Construct & Environm Engn, Ames, IA 50011 USA
基金
美国国家科学基金会;
关键词
anaerobic membrane bioreactor; hydraulic retention time; ambient temperature; methane production; synthetic municipal wastewater; CROSS-FLOW FILTRATION; REACTOR; UASB;
D O I
10.2175/106143009X407339
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The performance of a crossflow anaerobic membrane bioreactor (AnMBR) to treat synthetic municipal wastewater was investigated at different hydraulic retention times (HRTs). The AnMBR was operated at chemical oxygen demand (COD) loading rates of 1 to 2 kg COD/m(3).d for 280 days. The permeate COD concentration was always lower than 40 mg/L, and no noticeable volatile fatty acids were detected, regardless of HRT variations, while soluble COD (SCOD) was accumulated in the reactor with decreases in HRT. The particle size reduction was relatively lower than other studies reported, even after a long operation time resulting from the low operation crossflow velocity. Approximately 30% of COD was not available for methane recovery, irrespective of applied HRTs, as a result of the COD loss by dissolved methane, sulfate reduction, and untreated COD in the permeate. The fraction of methane recovered from the synthetic municipal wastewater decreased from 48 to 35%, with the decrease of HRT from 12 to 6 hours, as a result of the increase of mixed-liquor SCOD, which was rejected and accumulated in the AnMBR. Therefore, AnMBR operation with relatively long HRTs and SRTs may be favorable, to enhance methane recovery and reduce or eliminate sludge production. Water Environ. Res., 81, 922 (2009).
引用
收藏
页码:922 / 928
页数:7
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