期刊文献+

MBfR中表面改性疏水性PVDF中空纤维膜污染特性研究 被引量:1

MEMBRANE FOULING CHARACTERISTICS OF SURFACE MODIFIED HYDROPHOBIC PVDF HOLLOW FIBER MEMBRANE FOR MBfR
下载PDF
导出
摘要 针对膜生物膜反应器(MBf R)研究中疏水性微孔膜供氧能力不足、耐污染性较差等问题,采用界面聚合法对自制疏水性聚偏氟乙烯(PVDF)中空纤维膜进行表面改性,研究制备适用于MBf R技术的中空纤维复合膜。选取典型有机污染物牛血清白蛋白(BSA)、腐殖酸(HA)、海藻酸钠(SA),考察原膜及表面改性膜的抗污染性能。结果表明,表面改性膜的BSA、HA、SA吸附量均低于原膜,分别为原膜的58.6%、56.1%及96.0%;进一步的氧传质实验结果表明3种有机物污染后,改性膜的氧总转移系数衰减率分别为14.4%、15.5%及21.1%,均低于原膜(分别为23.8%、26.8%及38.9%),显示表面改性膜具有良好的抗污染性能。 In order to recover some disadvantages of hydrophobic hollow fiber membrane used in the MBf R, such as insufficient oxygen supply capacity and poor antifouling properties, surface of self-made hydrophobic polyvinylidene fluoride(PVDF) hollow fiber membrane was modified for MBf R technology by the method of interfacial polymerization. Bovine serum albumin(BSA), humic acid(HA) and sodium alginate(SA) were used as typical organic pollutants in order toinvestigate the anti-pollution ability of the original and the modified membrane. The results showed that, BSA, HA and SA adsorption amount of modified membrane were less than that of the original membrane, and the adsorption quantity were 58.6%, 56.1% and 96.0%respectively compared with the original. The further oxygen mass transfer experiments showed that,after being polluted, the total oxygen transfer coefficient of the modified membrane attenuation rates were 14.4%, 15.5% and 21.1%, respectively, lower than that of the original membrane(23.8%, 26.8% and38.9%, respectively), which indicated that anti-fouling capability of modified membrane was better than that of the original membrane.
机构地区 天津工业大学
出处 《水处理技术》 CAS CSCD 北大核心 2015年第11期50-53,共4页 Technology of Water Treatment
基金 国家自然科学基金(51408415,21176188) 天津市科技兴海项目(KJXH2014-03)
关键词 膜生物膜反应器 疏水微孔膜 表面改性 膜污染 membrane biofilm reactor hydrophobic microporous membrane surface modification membrane fouling
  • 相关文献

参考文献17

  • 1Maitin K J, Nerenberg R. The membrane biofilm reactor (MBR) for water and wastewater treatment: Principles, applications, and recent developments[J].Bioresource Technology,2012,122(3):83 -94.
  • 2张杨,李庭刚,强志民,刘俊新,尹秀英.膜曝气生物膜反应器研究进展[J].环境科学学报,2011,31(6):1133-1143. 被引量:31
  • 3Reij M W, Keurentjes J T F, Hartmans S. Membrane bioreactors for waste gas treatment[J].Journal of Biotechnology, 1998,59(3): 155-167.
  • 4Kretden H, Smolders C A, Versteeg G F, et al. Determination of mass transfer rates in wetted and non-wetted microporous membranes[J]. Chemical Engineering Science, 1993,48( 11):2093-2102.
  • 5Casey E, Glennon B, Hamer G. Review of membrane aerated biofilm reactors[J].Resources, Conservation and Recycling,1999,27(2):203- 215.
  • 6Semmens M J, Dahm K, Shanahan J, et al. COD and nitrogen removal by biofilms growing on gas permeable membranes[J].Water Research, 2003,37(18):4343-4350.
  • 7Voss M A, Ahmed T, Semmens M J. Long-term performance ofparallel-flow, bubbleless, hollow-fiber-membrane aerators[J].Water Environment Research, 1999,71 (1):23 -30.
  • 8Hibiya K, Tsuneda S, Hirata A. Formation and characteristics of nitrifying biofilm on a membrane modified with positively-charged polymer chains[J].Colloid and Surfaces B: Biointerfaces,2000,18 (2):105-112.
  • 9环国兰,张宇峰,杜启云,吴云.正交试验优化复合纳滤膜复合条件[J].膜科学与技术,2004,24(5):77-79. 被引量:10
  • 10Ahmed T, Michael J. Use of sealed hollow fibers for bubble less membrane aeration: experimental studies [J].Joumal of Membrane Science,1992,69(1-2): 1-10.

二级参考文献173

共引文献109

同被引文献4

引证文献1

二级引证文献6

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