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This study designed and operated two sets of A²/O-self-forming dynamic membrane reactors: one with aeration inside the membrane module and the other without aeration (control group). The dynamic membrane structure, membrane fouling, and treatment efficiency of both systems were systematically investigated. The results showed that the permeate flux and treatment efficiency were comparable between the two systems during the initial operational stage. However, as operation duration increased, the control group gradually developed a dynamic layer dominated by anoxic/anaerobic sludge, whereas the aerated group formed a dynamic layer with an alternating aerobic-anoxic-anaerobic structure. Compared to the control group, the aerated system developed a porous, network-like dynamic layer composed primarily of filamentous aerobic sludge, which significantly improved permeate flux and extended operational duration by nearly 40%. Furthermore, the extensive anoxic/anaerobic zones in the control group's dynamic membrane led to the death of aerobic microorganisms and the subsequent release of organic nitrogen and phosphorus. Consequently, the effluent concentrations of ammonia nitrogen and total phosphorus exhibited a gradual increase over time. In contrast, the aerated group maintained higher microbial activity in its dynamic layer, and the alternating aerobic-anoxic-anaerobic activated sludge configuration facilitated simultaneous nitrification-denitrification, significantly reducing effluent concentrations of both ammonia nitrogen and total phosphorus.

, authors=Fei-fan HE¹, Yu-peng WANG¹, Wei-bing JIANG¹, Le-han DING¹, Rui MIAO^{1, 2, *}, Lei WANG^{1, 2}, authorsList=Fei-fan HE, Yu-peng WANG, Wei-bing JIANG, Le-han DING, Rui MIAO, Lei WANG, authorCompany=null, correspAuthors=Rui MIAO, authorNote=null, correspAuthorsNote=null, copyrightStatement=null, copyrightOwner=null, extLink=null, articleAbsUrl=null, sourceXml=null, magXml=null, pdfUrl=null, pdf=null, pdfFileSize=null, pdfExtLink=null, richHtmlUrl=null, mobilePdfUrl=null, reviewReport=null, pdfFirstPage=null, abstractGraph=null, abstractGraphContent=null, abstractVideo=null, citation=null, cebUrl=null, magXmlContent=null, mapNumber=null, fund=null), CN=ArticleExt(id=1314918501052150217, articleId=1314918499361845702, tenantId=1146029695717560320, journalId=1234093305789726721, language=CN, title=氧环境对自生动态膜污染行为及处理效果影响机制研究, columnId=1234106386565624579, journalTitle=中国环境科学, columnName=水污染与控制, runingTitle=null, highlight=null, articleAbstract=

本研究构建了两组A²/O-自生动态膜反应器（膜组件内曝气与无曝气对照组），系统考察了动态膜结构、膜污染及处理性能的差异．结果表明：运行初期两组动态膜的渗透通量及处理效果相近；随着运行时间延长，对照组逐渐形成以缺氧/厌氧污泥为主的动态层，而曝气组动态层则为好氧-缺氧-好氧相间状．相较于对照组，曝气组中以丝状菌属为优势的好氧污泥在基材表面形成了网状多孔动态层，从而显著提升了渗透通量，并将系统运行周期延长了约40%．同时，对照组动态膜内大范围缺/厌氧环境导致好氧微生物死亡并释放有机氮、磷，致使出水氨氮和总磷浓度持续上升；而曝气组凭借好氧-缺氧-好氧交替的活性污泥层维持了较高微生物活性，实现了同步硝化反硝化，出水氨氮和总磷浓度显著降低．

, authors=何非凡¹, 王宇鹏¹, 姜伟兵¹, 丁乐晗¹, 苗瑞^{1, 2, *}, 王磊^{1, 2}, authorsList=何非凡, 王宇鹏, 姜伟兵, 丁乐晗, 苗瑞, 王磊, authorCompany=null, correspAuthors=苗瑞, authorNote=, correspAuthorsNote=, copyrightStatement=null, copyrightOwner=null, extLink=null, articleAbsUrl=null, sourceXml=db50/xj91nmiFRbTdoZMUg==, magXml=DclSvj5ssA84cP0ustM90A==, pdfUrl=null, pdf=jT81hZ4DWWP+q/DzZ93aIg==, pdfFileSize=3295790, pdfExtLink=null, richHtmlUrl=null, mobilePdfUrl=null, reviewReport=null, pdfFirstPage=null, abstractGraph=null, abstractGraphContent=null, abstractVideo=null, citation=null, cebUrl=null, magXmlContent=RXnYiiwy6derR3lNx+XDWA==, mapNumber=null, fund=null)}, authors=[Author(id=1314918503560344017, tenantId=1146029695717560320, journalId=1234093305789726721, articleId=1314918499361845702, orderNo=0, firstName=null, middleName=null, lastName=null, nameCn=null, orcid=null, stid=null, country=null, authorPic=null, dead=0, email=19819562969@163.com, emailSecond=null, emailThird=null, correspondingAuthor=0, authorType=1, ext={EN=AuthorExt(id=1314918503983968723, tenantId=1146029695717560320, journalId=1234093305789726721, articleId=1314918499361845702, authorId=1314918503560344017, language=EN, stringName=Fei-fan HE, firstName=Fei-fan, middleName=null, lastName=HE, prefix=null, suffix=null, authorComment=null, nameInitials=null, affiliation=null, department=null, xref=¹, address=^1.Key Laboratory of Northwest Water Resource, Environment and Ecology, Key Laboratory of Membrane Separation of Shaanxi Province, School of Environmental and Municipal Engineering, Xi'an University of Architecture and Technology, Xi'an 710055, China, bio=null, bioImg=null, bioContent=null, aboutCorrespAuthor=null), CN=AuthorExt(id=1314918504365650388, tenantId=1146029695717560320, journalId=1234093305789726721, articleId=1314918499361845702, authorId=1314918503560344017, language=CN, stringName=何非凡, firstName=null, middleName=null, lastName=null, prefix=null, suffix=null, authorComment=null, nameInitials=null, affiliation=null, department=null, xref=¹, address=^1.西安建筑科技大学环境与市政工程学院，西北水资源与环境生态教育部重点实验室，陕西省膜分离重点实验室，陕西 西安 710055, bio={"content":"

何非凡（1999-），男，山东菏泽人，西安建筑科技大学硕士研究生，研究方向为膜法水处理技术．发表论文1篇．19819562969@163.com.

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何非凡（1999-），男，山东菏泽人，西安建筑科技大学硕士研究生，研究方向为膜法水处理技术．发表论文1篇．19819562969@163.com.

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