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Evaluation of virus removal in MBR using coliphages T4 被引量:8

Evaluation of virus removal in MBR using coliphages T4
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摘要 A membrane bioreactor (MBR) with gravity drain was tested for domestic wastewater for 65 days. Results showed that the effluent quality was excellent, and met with the reuse water standard of China (GB/T 18920-2002). Virus removal in the membrane separation process was investi- gated by employing coliphages T4 as a tracer. Two microfil- tration membrane modules, with pore sizes of 0.22 and 0.1 μm, were used to investigate their effects on virus rejection at the transmembrane pressure of 8.5 kPa. It was found that 0.1 μm membrane had complete rejection of virus, and 0.22 μm membrane had significant rejection of virus. In the long- term operation of this MBR, no significant difference was observed between both pore sizes because the virus concen- trations of the effluent in both cases were in the same order. Effluent virus concentration at steady state of MBR running was less than 2 PFU/mL. The removal ratios of coliphage T4 in MF processes were more than 105.5. The membrane sur- face deposits played an important role in the rejection of virus. The formation of cake clay on the membrane surface was the main cause of high rejection of coliphage T4 with MF of 0.22 μm. A membrane bioreactor (MBR) with gravity drain was tested for domestic wastewater for 65 days. Results showed that the effluent quality was excellent, and met with the reuse water standard of China (GB/T 18920-2002). Virus removal in the membrane separation process was investi- gated by employing coliphages T4 as a tracer. Two microfil- tration membrane modules, with pore sizes of 0.22 and 0.1 μm, were used to investigate their effects on virus rejection at the transmembrane pressure of 8.5 kPa. It was found that 0.1 μm membrane had complete rejection of virus, and 0.22 μm membrane had significant rejection of virus. In the long- term operation of this MBR, no significant difference was observed between both pore sizes because the virus concen- trations of the effluent in both cases were in the same order. Effluent virus concentration at steady state of MBR running was less than 2 PFU/mL. The removal ratios of coliphage T4 in MF processes were more than 105.5. The membrane sur- face deposits played an important role in the rejection of virus. The formation of cake clay on the membrane surface was the main cause of high rejection of coliphage T4 with MF of 0.22 μm.
出处 《Chinese Science Bulletin》 SCIE EI CAS 2005年第9期862-867,共6页
基金 supported by the National Natural Science Foundation of China(Grant No.20347001).
关键词 废水处理 微生物学 大肠杆菌 隔膜生物反应器 coliphage T4, MBR, wastewater treatment.
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