安全与环境学报
安全與環境學報
안전여배경학보
JOURNAL OF SAFETY AND ENVIRONMENT
2010年
1期
48-51
,共4页
环境工程学%膜生物反应器%预涂%粉末状活性炭%聚合氯化铝
環境工程學%膜生物反應器%預塗%粉末狀活性炭%聚閤氯化鋁
배경공정학%막생물반응기%예도%분말상활성탄%취합록화려
environmental engineering%MBR%pre-coate%PAC%poly-aluminum chloride
以公称孔径为1 μm的聚丙烯无纺布(NWF)为基膜,分别以粉末状活性炭、粉末状活性炭及聚合氯化铝为预涂剂,制作预涂动态膜膜组件,组成预涂动态膜-生物反应器处理人工废水.结果表明,预涂动态膜-生物反应器出水COD值低且稳定,粉末状活性炭预涂膜-生物反应器出水COD平均值为49 mg/L,粉末状活性炭及聚合氯化铝预涂膜-生物反应器出水COD平均值为29 mg/L,而NWF-膜生物反应器出水COD为54 mg/L.膜生物反应器对污染物质的去除虽然主要依靠活性污泥混合液,但附着在基膜上的动态膜的吸附、混凝作用也能去除部分污染物质.预涂膜能减少及防止污染物质向膜材料表面和内部扩散,减轻膜污染,使预涂动膜-生物反应器显示出一定的耐污染性能.但粉末状活性炭粒径过小,影响粉末状活性炭预涂动态膜-生物反应器的出水浊度(平均值为3.3 NTU);而粉末状活性炭与聚合氯化铝形成的预涂动态膜,在提高COD去除效率的同时,能减少活性炭对出水浊度(平均值为2.3 NTU)的影响,保证出水水质.
以公稱孔徑為1 μm的聚丙烯無紡佈(NWF)為基膜,分彆以粉末狀活性炭、粉末狀活性炭及聚閤氯化鋁為預塗劑,製作預塗動態膜膜組件,組成預塗動態膜-生物反應器處理人工廢水.結果錶明,預塗動態膜-生物反應器齣水COD值低且穩定,粉末狀活性炭預塗膜-生物反應器齣水COD平均值為49 mg/L,粉末狀活性炭及聚閤氯化鋁預塗膜-生物反應器齣水COD平均值為29 mg/L,而NWF-膜生物反應器齣水COD為54 mg/L.膜生物反應器對汙染物質的去除雖然主要依靠活性汙泥混閤液,但附著在基膜上的動態膜的吸附、混凝作用也能去除部分汙染物質.預塗膜能減少及防止汙染物質嚮膜材料錶麵和內部擴散,減輕膜汙染,使預塗動膜-生物反應器顯示齣一定的耐汙染性能.但粉末狀活性炭粒徑過小,影響粉末狀活性炭預塗動態膜-生物反應器的齣水濁度(平均值為3.3 NTU);而粉末狀活性炭與聚閤氯化鋁形成的預塗動態膜,在提高COD去除效率的同時,能減少活性炭對齣水濁度(平均值為2.3 NTU)的影響,保證齣水水質.
이공칭공경위1 μm적취병희무방포(NWF)위기막,분별이분말상활성탄、분말상활성탄급취합록화려위예도제,제작예도동태막막조건,조성예도동태막-생물반응기처리인공폐수.결과표명,예도동태막-생물반응기출수COD치저차은정,분말상활성탄예도막-생물반응기출수COD평균치위49 mg/L,분말상활성탄급취합록화려예도막-생물반응기출수COD평균치위29 mg/L,이NWF-막생물반응기출수COD위54 mg/L.막생물반응기대오염물질적거제수연주요의고활성오니혼합액,단부착재기막상적동태막적흡부、혼응작용야능거제부분오염물질.예도막능감소급방지오염물질향막재료표면화내부확산,감경막오염,사예도동막-생물반응기현시출일정적내오염성능.단분말상활성탄립경과소,영향분말상활성탄예도동태막-생물반응기적출수탁도(평균치위3.3 NTU);이분말상활성탄여취합록화려형성적예도동태막,재제고COD거제효솔적동시,능감소활성탄대출수탁도(평균치위2.3 NTU)적영향,보증출수수질.
The pre-coating dynamic membrane bioreactor(PDMBR) was composed of membrane model made of polypropylene (PP) non-woven fiber (NWF) with nominal diameter 1 μm and pre-coated with powdered activated carbon (PAC) and with both of PAC and poly-aluminium chloride. The PDMBR was used for synthetic wastewater treatment. The experimental results showed that the effluent COD from PDMBR is low and stable, the average COD of effluent from PAC-MBR is 49 mg/L, and the average COD from MBR pre-coated with PAC and poly-aluminium chloride is 29 mg/L, but COD of effluent from NWF-MBR is 54 mg/L. It illuminates that pollutants removal mainly depends on mixed activated sludge, but absorption and flocculence of dynamic membrane attached on the model can also remove some pollutants. Pre-coating dynamic MBR can reduce and prevent pollutants diffusing into the surface and interior of the primary membrane so as to mitigate membrane fouling and to make PDMBR have antifouling performace. If particles diameter of PAC is too small, the effluent turbidity (average is 3.3 NTU) from PDMBR will be effected. However, the precoating dynamic membrane formed by PAC and poly-aluminium chloride can not only increase the efficiency of COD removal, but also reduce the effect on effluent turbidity (average is 2.3 NTU) by activated carbon and can ensure good effluent quality.