水处理技术
水處理技術
수처리기술
2010年
3期
115-118
,共4页
元新艳%沈恒根%王琳%孙磊%李世峰
元新豔%瀋恆根%王琳%孫磊%李世峰
원신염%침항근%왕림%손뢰%리세봉
两级序批式MBR%污泥浓度%粉末活性炭%膜污染
兩級序批式MBR%汙泥濃度%粉末活性炭%膜汙染
량급서비식MBR%오니농도%분말활성탄%막오염
two-stage sequencing batch MBR%sludge concentration%PAC%membrane fouling
针对MBR在实际应用过程中存在的同步脱氮除磷效果不佳、膜污染严重等问题,提出两级序批式MBR工艺,对该工艺的膜污染影响因素及控制方法进行了试验研究.结果表明,在MBR中保持适宜的污泥质量浓度对于膜污染的控制有重要的作用,当污泥质量浓度稳定在6~7g·L~(-1)时,膜比流量基本稳定,随着污泥质量浓度的增加,膜比流量逐步降低,当污泥质量浓度超过10g·L~(-1)以后,膜比流量直线下降;投加PAC至1 g·L~(-1)可以增加污泥粒径,减少大分子有机物在膜表面沉积,从而有助于延缓膜污染;序批式间歇运行与空曝相结合的运行方式可以有效降低泥饼层污染及凝胶层污染,使系统在更高膜通量下运行,而膜污染速率却远低于连续流单级好氧MBR系统.
針對MBR在實際應用過程中存在的同步脫氮除燐效果不佳、膜汙染嚴重等問題,提齣兩級序批式MBR工藝,對該工藝的膜汙染影響因素及控製方法進行瞭試驗研究.結果錶明,在MBR中保持適宜的汙泥質量濃度對于膜汙染的控製有重要的作用,噹汙泥質量濃度穩定在6~7g·L~(-1)時,膜比流量基本穩定,隨著汙泥質量濃度的增加,膜比流量逐步降低,噹汙泥質量濃度超過10g·L~(-1)以後,膜比流量直線下降;投加PAC至1 g·L~(-1)可以增加汙泥粒徑,減少大分子有機物在膜錶麵沉積,從而有助于延緩膜汙染;序批式間歇運行與空曝相結閤的運行方式可以有效降低泥餅層汙染及凝膠層汙染,使繫統在更高膜通量下運行,而膜汙染速率卻遠低于連續流單級好氧MBR繫統.
침대MBR재실제응용과정중존재적동보탈담제린효과불가、막오염엄중등문제,제출량급서비식MBR공예,대해공예적막오염영향인소급공제방법진행료시험연구.결과표명,재MBR중보지괄의적오니질량농도대우막오염적공제유중요적작용,당오니질량농도은정재6~7g·L~(-1)시,막비류량기본은정,수착오니질량농도적증가,막비류량축보강저,당오니질량농도초과10g·L~(-1)이후,막비류량직선하강;투가PAC지1 g·L~(-1)가이증가오니립경,감소대분자유궤물재막표면침적,종이유조우연완막오염;서비식간헐운행여공폭상결합적운행방식가이유효강저니병층오염급응효층오염,사계통재경고막통량하운행,이막오염속솔각원저우련속류단급호양MBR계통.
The two-stage sequencing batch membrane bioreactor (TSBMB) process was put forward to face with the problems in poor effect of simultaneous nitrogen and phosphorus removal and serious membrane fouling during practical applications of MBR. The factors of membrane fouling and operation mode of MSMBR have been investigated. The results indicated that keeping proper sludge concentration in MBR played an important role in membrane fouling control. When the sludge concentration was stabilized at 6~7 g·L~(-1), the membrane flux was stable. The membrane flux slowed gradually as the sludge concentration increases, and there was a steep decline in the membrane flux when the sludge concentration higher than 10 g·L~(-1). The sludge size increased and the deposition of macromolecular organism on the membrane surface decreased when the addition of PAC increased to 1 g·L~(-1). Sequencing batch operation mode and the combination of intermittent membrane suction and idle aeration could reduce the cake layer fouling and the colloidal layer fouling effectively. The system could run under higher membrane flux and the membrane fouling rate was far lower than one-stage aerobic MBR.