用无纺滤布动态膜生物反应器处理生活污水，以研究动态膜成膜过程及对生活污水的处理效果。结果表明：在曝气量为600ml/min、出水压头为5cm、MLSS为4500mg/L的条件下启动反应器，1h后出水水质稳定，3h后膜通量稳定，可认为反应器启动后3h形成稳定动态膜。动态膜形成后，出水COD、NN4+-N、TP的值分别在14.46 mg/L～37.67 mg/L、0.79mg/L～3.31mg/L 、2.33～4.67 mg/L之间,其中活性污泥对COD、NN4+-N、TP的去除率分别为78.45%、80.17%、21.74%；动态膜对COD、NN4+-N、TP去除率分别为12.39 %、8.23%、13.36%；使反应器对COD、NN4+-N、TP的总去除率提高至90.84%、88.40%、35.10%。可见无纺滤布动态膜可强化普通生物反应器对污水处理效果。

The dynamic membrane bioreactor constructed by non-woven fabric was used for munisipal sewage traetment to study  its forming process and treatment effect for sewage.The results showed that the quality of effluent could be stable one hour later  and the membrane flux could be stable three hour later after DMBR startup ,when the aeration fluxes was 600 ml/min,the hydraulic head was 5cm and the MLSS was 4500mg/L.So it was considered the stable dynamic membrane was formed 3 hours later after the reactor startup. The contents of COD、TP、NN4+-N were 14.46 mg/L～37.67 mg/L、2.33～4.67 mg/L and 0.79mg/L～3.31mg/L after the dynamic membrane formation ,and the removal rates of COD、TP、NN4+-N were 90.84%、88.40% and 35.10%,which 78.45%、80.17%、21.74% were removaled by activated sludge 12.39 %、13.36%、8.23% were removaled by dynamic membrane.It was thus clear that the non¬-woven fabric dynamic membrane had an enhanced  effect to sewage treatment.

[1] 陆为钢，李文卫，王红宇.动态膜生物反应器处理城市生活污水的研究[J].中国给水排水, 2011,27(5):89- 92.
[2] KuberkarV T,Davis R H.Modeling of fouling reduction by secondary membranes[J]. Membr Sci.2000,168(1/2):243-258.
[3] 李晓波,胡保安,顾平.动态膜分离技术研究进[J].展膜科学与技术,2007,27(4):91-95.
[4] Fan B，Huang X. Characteristics of a self-forming dynamic membrane coupled with a bioreactor for municipal wastewater treatment[J]．Environ Sci Technol，2002，36(23):5245-5251．
[5] 李龙,湛含辉.动态膜技术及其在污水处理中的研究进展[J].膜科学与技术.2012,32(3): 112 -116.
[6] 张玉洁,李小利,赵继红.动态膜生物反应器(DMBR)研究进展[J].膜科学与技术.2012,32 (3):117-122.
[7] 洪俊明,尹娟,李伟博.动态膜生物反应器用于污水处理的研究进展[J].水处理技.2012,38 (2):1-4
[8] 卢芳芳,洪俊明,尹娟.缺氧动态膜生物反应器在淡水/海水养殖废水处理中的运行效果[J].化工进展.2011,30(11):2545-2548
[9]  吴春英，吴盈禧，夏俊林等.动态膜生物反应器的运行稳定性及其影响因素研究[J].中国给水排水,2009,( 21):21-25.
[10] 洪俊明,尹娟,卢芳芳.膜基材对动态膜生物反应器性能的影响研究[J].环境工程学报，2011 (02):311-314.
[11] 王勇,黄勇,袁怡等.无纺滤布生物膜反应器对厌氧氨氧化脱氮负荷提高的实现[J]苏州科技学院学报,2009(01):1-6.
[12]  黄天寅,姚嘉,俞汉青等.动态膜生物反应器膜污染过程及阻力分析[J].江苏大学学报(自然科学版).2012, 33(5):1671—7775.
[13] 国家环境保护总局,《水和废水监测分析方法》编委会.水和废水监测分析方法(第四版)[M].北京:中国环境科学出版社,2002.
[14] Bae T H,Tak T M.Interpretation of fouling characteristics of ultraltration membranes during the filtration of membrane bioreactor mixed liquor[J]. MembrBiol,2005,264:151-160．