澄清器
废水
无氧运动
化学需氧量
流出物
生物反应器
化学
制浆造纸工业
膜生物反应器
废物管理
膜反应器
挥发性悬浮物
流化床
膜污染
活性污泥
环境科学
环境工程
结垢
膜
工程类
有机化学
生物
生物化学
生理学
作者
Rihye Yoo,Jeong‐Hwan Kim,Perry L. McCarty,Jinhee Bae
标识
DOI:10.1016/j.biortech.2012.06.028
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 192 days at 6-11 L/m(2)/h flux and trans-membrane pressure generally of 0.1 bar 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 7 mg/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 0.049 g 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, 0.047 kW h/m(3), could be more than satisfied by using the methane produced.
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