Operational performance of a submerged membrane bioreactor for reclamation of bath wastewater

被引:57
作者
Rui, L [1 ]
Xia, H [1 ]
Chen, LJ [1 ]
Wen, XH [1 ]
Yi, Q [1 ]
机构
[1] Tsing Hua Univ, Dept Environm Sci & Engn, Environm Simulat & Pollut Control State Key Joint, Beijing 100084, Peoples R China
关键词
membrane bioreactor; wastewater reuse; wastewater reclamation; filtration; membrane fouling; membrane cleaning;
D O I
10.1016/j.procbio.2003.11.038
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
Bath wastewater is an ideal wastewater-reclamation source for its large discharge amount, simple pollutant composition and low pollutant content. The feasibility of reclaiming bath wastewater with a membrane bioreactor was investigated in a pilot plant of 10 m(3) per day at an organic load of 0.50-1.85 kg-COD/(m(3) per day). The operation was continued for 216 days without sludge discharge and chemical cleaning of membrane modules. The quality of the effluent obtained met the wastewater reclamation standard of China, with COD < 40 mg/l, NH4+-N <0.5 mg/l and anionic surfactant (AS) <0.2 mg/l. Biological treatment removed most pollutants in the influent, degrading 34-85% of COD and 98% of anionic surfactant. The membrane separation balanced the unstable biological treatment of COD but demonstrated no contribution to anionic surfactant removal. Inorganic substances were found to accumulate in the bioreactor. The main reason for membrane fouling was considered to be sludge adhesion and gel layer formation over the outer membrane surface and microbial growth over the inner membrane surface. (C) 2003 Elsevier Ltd. All rights reserved.
引用
收藏
页码:125 / 130
页数:6
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