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Anaerobic treatment of municipal wastewater with a staged anaerobic fluidized membrane bioreactor (SAF-MBR) system

机译:分阶段厌氧流化膜生物反应器(SAF-MBR)系统厌氧处理市政废水

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摘要

A laboratory-scale staged anaerobic fluidized membrane bioreactor (SAF-MBR) system was used to treat a municipal wastewater primary-clarifier effluent. It was operated continuously for 192days at 6-11L/m ~2/h flux and trans-membrane pressure generally of 0.1bar or less with no fouling control except the scouring effect of the fluidized granular activated carbon on membrane surfaces. With a total hydraulic retention time of 2.3h at 25°C, the average effluent chemical oxygen demand and biochemical oxygen demand concentrations of 25 and 7mg/L yielded corresponding removals of 84% and 92%, respectively. Also, near complete removal of suspended solids was obtained. Biosolids production, representing 5% of the COD removed, equaled 0.049g VSS/g BOD _5 removed, far less than the case with comparable aerobic processes. The electrical energy required for the operation of the SAF-MBR system, 0.047kWh/m ~3, could be more than satisfied by using the methane produced.
机译:实验室规模的分阶段厌氧流化膜生物反应器(SAF-MBR)系统用于处理市政废水一级澄清池废水。它在6-11L / m〜2 / h的通量下连续运转192天,跨膜压力通常为0.1bar或更低,除污垢流化活性炭对膜表面的冲刷作用外,无结垢控制。在25°C下的总水力停留时间为2.3h时,废水的平均化学需氧量和生化需氧量浓度分别为25和7mg / L,分别可分别去除84%和92%。而且,几乎完全除去了悬浮固体。生物固体产量占去除的COD的5%,等于0.049g VSS / g BOD _5去除,远低于可比的好氧工艺。 SAF-MBR系统运行所需的电能0.047kWh / m〜3,可以通过使用所产生的甲烷来满足。

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