期刊文献+

有机物分子尺度对纳滤膜污染的影响研究 被引量:3

Effects of Molecular Weight Distribution of Organic Matter on Nanofiltration Membrane Fouling
原文传递
导出
摘要 以市政污水处理厂的MBR出水作为纳滤进水,从有机物分子尺度分布的微观角度分析进水中有机物分布特征与纳滤膜污染的相关性,研究含不同分子质量的有机物水样对纳滤膜通量衰减、脱盐率以及膜表面污染的影响规律。结果表明,随着进水中溶解性有机物分子质量的减小,膜比通量衰减幅度不断增加,特别是分子质量〈1ku的溶解性有机物引起膜通量衰减幅度最大,连续运行28h后膜比通量下降了85.2%。电镜扫描分析进一步表明,进水中分子质量〈1ku的有机物是造成膜有机污染的主要成分。此外,水中有机物在纳滤膜表面的累积会使纳滤膜的脱盐率有所增加。当进水中有机物分子质量在1ku以下时,纳滤膜的初始脱盐率在94%左右,经28h连续运行后脱盐率上升了3.5%~4%;进水中有机物分子质量在100ku以下时,纳滤膜的初始脱盐率为91%~92%,经28h连续运行后脱盐率上升4%~4.5%。 The relationship between molecular weight distribution of organic matter and nanofiltration membrane (NF) fouling was analyzed using the effluent from membrane bioreactor (MBR) in a municipal wastewater treatment plant. The effects of wastewater samples containing different molecular weight fractions of organic matter on membrane flux decline, desalinization efficiency and membrane surface fouling were investigated. The results showed that the attenuation of membrane specific flux continuously increased with decreasing molecular weight of dissolved organic matter in influent, especially when below 1 ku. After continuous operation for 28 h, the membrane specific flux decreased by 85.2%. Electron microscope scanning of membrane surface further suggested that dissolved organic matter with molecular weight below 1 ku was the dominant component to cause membrane fouling. Accumulation of organic matter on the membrane surface could result in an increase of desalinization efficiency. When the molecular weight of organic matter in influent was below 1 ku, the initial desalinization efficiency of NF was a- bout 94% , and after continuous operation for 28 h, the desalinization rate increased by 3.5% to 4%. When the molecular weight of organic matter in influent was below 100 ku, the initial desalinization of NF was about 91% to 92%, and after continuous operation for 28 h, the desalinization efficiency increased by 4% to 4.5%.
出处 《中国给水排水》 CAS CSCD 北大核心 2013年第19期85-88,共4页 China Water & Wastewater
基金 国家自然科学基金资助项目(51138008 51108315) 天津市科技支撑计划重点项目(11ZCGYSF01500)
关键词 纳滤膜污染 分子质量分布 有机物 nanofiltration membrane fouling molecular weight distribution organic matter
  • 相关文献

参考文献7

  • 1Zhao Y,Song L F, Ong S L. Fouling of RO membranes by effluent organic matter (EfOM):Relating major compo- nents of EfOM to their characteristic fouling behaviors [J]. J MembrSci,2010,349(1/2):75-82.
  • 2Jarusutthirak C, Amy G, Croue P J. Fouling characteris- tics of wastewater effluent organic matter ( EfOM ) isolates on NF and UF membranes [ J ]. Desalination,2002, 145 (1/3) :247 -255.
  • 3Listiarini K,Chun W,Sun D D,et al. Fouling mechanism and resistance analyses of systems comaining sodium algi- nate, calcium, alum and their eombinalion in dead-end fouling of nanofihration membranes [ J ]. J Membr Sci, 2009,344(1/2) :244 - 251.
  • 4Tang C Y,Kwon Y N,Leekie J O. Characterization of hu- mic acid fouled reverse osmosis and nanofiltration mem- branes by transmission electron microscopy and s/reaming potential measurements[ J ]. Environ Sei Technol,2007, 41 (3) :942 -949.
  • 5张海丰,孙宝盛,赵新华,齐庚申.膜生物反应器中溶解性微生物代谢产物的产出[J].中国环境科学,2007,27(4):539-542. 被引量:12
  • 6Park N,Kown B,Kim 1 S,et al. Biofouling potential of various NF membranes with respect to bacteria and their soluble microbial products (SMP):Characterizations,flux decline, and transport parameters [ J ]. J Membr Sci, 2005,258(1/2) :43 -54.
  • 7Janasutthirak C,Amy G. Role of soluble microbial prod- ucts (SMP) in membrane fouling and flux decline[ J]. Environ Sci Technol ,2006,40 ( 3 ) :969 - 974.

二级参考文献10

  • 1Witzig R, Manz W, Rosenberger S, et al. Microbiological aspects of a bioreactor with submerged membranes for aerobic treatment of municipal wastewater [J]. Water Res., 2002,36(2):394-402.
  • 2Namkung E, Rittmarm B E. Effects of SMP on biofilm-reactor performance [J]. J. Environ. Eng. Div. ASCE, 1988,114(1): 199-210.
  • 3Rittmann B E, Bae W, Namkong E, et al. A critical evaluation of microbial product formation in biological processes [J]. Water Sci. Tech., 1987,19(3-4):517-528.
  • 4Yonghun L, Jinwoo C, Youngwoo S, et al. Modeling of submerged membrane bioreactor process for wastewater treatment [J]. Desalination, 2002,146:451-457.
  • 5Hang S, Seok T. Characteristics and fate of soluble microbial products in ceramic membrane bioreactor at various sludge retention times [J]. Water Res., 2003,37(1):121-127.
  • 6Duncan J, Barker, Gianni A, et al. Characterization of soluble residual chemical oxygen demand (COD) in anaerobic wastewater treatment effluents [J]. Water Res., 1999,33(11): 2499-2510.
  • 7Duncan J B, Mannucchi G A, Salvi S M, et al. A review of soluble microbial products (SMP) in wastewater treatment systems [J]. Water Res., 1999,33(14):3063-3082.
  • 8Nagaoka H, Ueda S, Miya A. Influence of bacterial extracellular polymers on the membrane separation activated sludge process [J]. Water Sci. Teclmol., 1996,34(9): 165-172.
  • 9Chrysi S, Laspidou, Bruce E, et al. A unified theory for extracellular polymeric substances, soluble microbial products, and active and inert biomass [J]. Water Res., 2002.36(11): 2711-2720.
  • 10刘锐,黄霞,范彬,藤本真由美,钱易.膜-生物反应器中溶解性微生物产物的研究进展[J].环境污染治理技术与设备,2002,3(1):1-7. 被引量:66

共引文献11

同被引文献29

引证文献3

二级引证文献18

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部