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Effect of engineered environment on microbial community structure in biofilter and biofilm on reverse osmosis membrane

机译:工程环境对反渗透膜生物滤池和生物膜微生物群落结构的影响

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摘要

Four dual media filters (DMFs) were operated in a biofiltration mode with different engineered environments (DMF I and II: coagulation with/without acidification and DMF III and IV: without/with chlorination). Designed biofilm enrichment reactors (BERs) containing the removable reverse osmosis (RO) coupons, were connected at the end of the DMFs in parallel to analyze the biofilm on the RO membrane by DMF effluents. Filtration performances were evaluated in terms of dissolved organic carbon (DOC) and assimilable organic carbon (AOC). Organic foulants on the RO membrane were also quantified and fractionized. The bacterial community structures in liquid (seawater and effluent) and biofilm (DMF and RO) samples were analyzed using 454-pyrosequencing. The DMF IV fed with the chlorinated seawater demonstrated the highest reductions of DOC including LMW-N as well as AOC among the other DMFs. The DMF IV was also effective in reducing organic foulants on the RO membrane surface. The bacterial community structure was grouped according to the sample phase (i.e., liquid and biofilm samples), sampling location (i.e., DMF and RO samples), and chlorination (chlorinated and non chlorinated samples). In particular, the biofilm community in the DMF IV differed from the other DMF treatments, suggesting that chlorination exerted as stronger selective pressure than pH adjustment or coagulation on the biofilm community. In the DMF IV, several chemoorganotrophic chlorine-resistant biofilm-forming bacteria such as Hyphomonas, Erythrobacter, and Sphingomonas were predominant, and they may enhance organic carbon degradation efficiency. Diverse halophilic or halotolerant organic degraders were also found in other DMFs (i.e., DMF I, II, and III). Various kinds of dominant biofilmforming bacteria were also investigated in RO membrane samples; the results provided possible candidates that cause biofouling when DMF process is applied as the pretreatment option for the RO process. (C) 2017 Elsevier Ltd. All rights reserved.
机译:四个双介质过滤器(DMF)在不同工程环境下以生物过滤模式运行(DMF I和II:有/无酸凝结,DMF III和IV:无/有氯化作用)。包含可移动反渗透试管的设计的生物膜富集反应器(BER)在DMF末端并联连接,以通过DMF流出物分析RO膜上的生物膜。根据溶解的有机碳(DOC)和可吸收的有机碳(AOC)评估了过滤性能。 RO膜上的有机污垢也被定量和分级。使用454-焦磷酸测序分析了液体(海水和污水)和生物膜(DMF和RO)样品中的细菌群落结构。用氯化海水喂养的DMF IV在其他DMF中表现出最高的DOC减少量,包括LMW-N和AOC。 DMF IV还可以有效减少RO膜表面的有机污垢。根据样品阶段(即液体和生物膜样品),采样位置(即DMF和RO样品)和氯化(氯化和非氯化样品)对细菌群落结构进行分组。特别是,DMF IV中的生物膜群落与其他DMF处理不同,这表明氯化作用比生物膜群落上的pH调节或凝结具有更强的选择压力。在DMF IV中,主要有几种抗化学有机营养的形成生物膜的细菌,例如:Hyphomonas,Erothrobacter和Sphingomonas,它们可以提高有机碳的降解效率。在其他DMF中(也就是DMF I,II和III)也发现了不同的嗜盐或卤代有机降解剂。反渗透膜样品中还研究了各种占优势的生物膜形成细菌。结果提供了在将DMF工艺用作反渗透工艺的预处理选项时可能导致生物污染的候选物。 (C)2017 Elsevier Ltd.保留所有权利。

著录项

  • 来源
    《Water Research》 |2017年第1期|227-237|共11页
  • 作者单位

    Sungkyunkwan Univ SKKU, Grad Sch Water Resources, 2066,Seobu Ro, Suwon 16419, Gyeonggi Do, South Korea|KAUST, WDRC, BESE, Thuwal 239556900, Saudi Arabia|UTS, Fac Engn & IT, POB 123, Broadway, NSW 2007, Australia;

    Korea Inst Sci & Technol, Ctr Water Resource Cycle Res, 39-1 Hawolgok Dong, Seoul 136791, South Korea;

    Korea Inst Sci & Technol, Ctr Water Resource Cycle Res, 39-1 Hawolgok Dong, Seoul 136791, South Korea|Yonsei Univ, Chem & Biomol Engn, 50 Yonsei Ro, Seoul 120749, South Korea;

    Korea Inst Sci & Technol, Ctr Water Resource Cycle Res, 39-1 Hawolgok Dong, Seoul 136791, South Korea;

    KAUST, WDRC, BESE, Thuwal 239556900, Saudi Arabia;

    UTS, Fac Engn & IT, POB 123, Broadway, NSW 2007, Australia;

    Pusan Natl Univ, Dept Civil & Environm Engn, 63 Busandeahak Ro, Busan 46241, South Korea;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Biofilm; Biofiltration; Chlorination; Coagulation; Seawater reverse osmosis; Microbial community structure;

    机译:生物膜;生物过滤;氯化;混凝;海水反渗透;微生物群落结构;

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