期刊文献+

正渗透过程参数对渗透性能的影响 被引量:9

Effect of Process Parameters on Osmosis Performance During Forward Osmosis
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摘要 正渗透是新的非热能驱动膜过程。采用界面聚合的方法制备了中空纤维复合膜。以Na2SO4、MgSO4、NaCl和Mg-Cl2水溶液作为驱动液进行了正渗透实验。实验表明,正渗透通量随着驱动液浓度的增加而增加,其中Na2SO4、MgCl2水溶液的渗透通量大于MgSO4、NaCl水溶液的。驱动液中无机盐向原水中扩散的渗透速率随无机盐浓度的增加而增加,且MgCl2>NaCl>Na2SO4>MgSO4。原水流速对正渗透通量的影响极小,而驱动液流速对正渗透通量的影响较大。 Forward(direct) osmosis(FO) is a non-thermal membrane process.A polyamide composite hollow fiber membrane was prepared by the interfacial polymerization.The reverse osmosis properties of the composite membrane were studied.In the present study,four draw solutions(Na2SO4,MgSO4,NaCl and MgCl2) were employed by the FO process to extract water from feed water across the composite membrane.Water osmosis flux was increased with the concentration of draw solutions in forward osmosis mode.The osmosis flux of Na2SO4,MgCl2 solutions is far higher than that of MgSO4,NaCl solutions.Change of osmosis velocity of the inorganic salts was described as MgCl2NaClNa2SO4MgSO4,and the osmosis velocity increased with the increase of inorganic salt concentration.Effect of raw water flux rate was generally very small on permeated flux,but the permeated flux was then raised to higher with increaseing draw solution flux rate.
出处 《高分子材料科学与工程》 EI CAS CSCD 北大核心 2012年第1期86-88,92,共4页 Polymer Materials Science & Engineering
基金 国家重点基础研究发展计划(973计划)课题(2006CB708602)
关键词 正渗透 复合膜 驱动液 渗透性能 forward osmosis composite membrane draw solution osmosis performance
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参考文献8

  • 1Subramani A, Hoek E M V. Direct observation of initial microbial deposition onto reverse osmosis and nanofiltration membranes[J ]. J. Membr. Sci., 2008, 319 (1-2): 111-125.
  • 2Belkacem M, Bekhti S, Bensadok K. Groundwater treatment by reverse osmosis[J]. Desalination, 2007, 206 (1-3) : 100-106.
  • 3Greenlee L F, Lawler D F, Freeman B D, et al. Reverse osmosis declination: water sources [ J ]. Water Research, 2009, 43 (9) : 2317-2348.
  • 4Lattemann S, Kennedy M D, Amy G. Seawater desalination -a green technology[J]. J. Water Supply Res. T., 2010, 59(2-3): 134- 151.
  • 5Al-Jeshi S, Neville A. An experimental evaluation of reverse osmosis membrane performance in oily water[J]. Desalination, 2008, 228( 1- 3) : 287-294.
  • 6高从堦,郑根江,汪锰,王铎,高学理,周勇.正渗透-水纯化和脱盐的新途径[J].水处理技术,2008,34(2):1-4. 被引量:48
  • 7Phillip W A, Yongj S, Elimelech M. Reverse draw solute permeation in forward osmosis: modeling and experiments[J]. Environ. Sci. Technol. , 2010, 44(13) :5170-5176.
  • 8Ng H Y, Tang N W, Wong W S. Performance of forward (direct) osmosis process membrane structure and transport phenomenon [ J ]. Environ. Sci. Tecbnol. , 2006, 40(7): 2408-2413.

二级参考文献35

  • 1Tzahi Y Cath, Amy E Childress, Menachem Elimelech. Forward osmosis: principles, applications, and recent developments[J].J Membr Sci.,281 (2006) 70-87.
  • 2Prachi Patel-Predd. Water desalination takes a step forward[J].Environ Sci Technol.,2006,40( 11 ):3454-3455.
  • 3K L Lee, R W Baker, H K Lonsdale. Membranes for power generation by pressure retarded osmosis [J].J Membr Sci.,1981:8 141-171.
  • 4J R McCutcheon, R L McGinnis, M Elimelech. Desalination by a novel ammonia-carbon dioxide forward osmosis process: influence of draw and feed solution concentrations on process performance[J].J Membr Sci.,2006,278:114-123.
  • 5G T Gray, J R McCutcheon. M Elimelech, Internal concentration polarization in forward osmosis: role of membrane orientation[J]. Desalination,2006,197:1-8.
  • 6David R Lide. CRC handbook of chemistry and physics [M]. Boca Raton: CRC Press,2003.
  • 7James E Miller, Lindsey R Evans. Forward Osmosis: a new approach to water purification and desalination[R].Sandia:SANDIA REPORT SAND2006-4634,2006.
  • 8G W Batchelder. Process for the demineralization of water:US,3 171799 [P]. 1965 -03 -02.
  • 9D N Glew. Process for liquid recovery and solution concentration: US,3216930[P].1965-11-09.
  • 10B S Frank.Desalination of sea water: US, 3670897 [P].1972-06-20.

共引文献47

同被引文献221

  • 1陈丽梅,程敏熙,肖晓芳,黄佐华.盐溶液电导率与浓度和温度的关系测量[J].实验室研究与探索,2010,29(5):39-42. 被引量:48
  • 2解一君,马睿,夏圣骥,高乃云.正渗透水处理技术研究进展[J].给水排水,2012,38(S1):109-112. 被引量:6
  • 3宋英豪,陈瑞芳,熊娅,贾立敏.基于零排放浓盐水处理技术的发展[J].环境工程,2013,31(S1):263-265. 被引量:14
  • 4卢国冬,燕青芝,宿新泰,刘中清,葛昌纯.多孔水凝胶研究进展[J].化学进展,2007,19(4):485-493. 被引量:38
  • 5刘岩,李志东,蒋林时.膜生物反应器(MBR)处理废水的研究进展[J].长春理工大学学报(自然科学版),2007,30(1):98-101. 被引量:21
  • 6Lattemann S, Kennedy M D, Amy G. Seawater desalination-a green technology [J].Joumal of Water Supply Research and Technology, 2010,59(2-3):134-151.
  • 7Achilli A, Cath T Y, Marchand E A, et al. The forward osmosis membrane bioreactor: A low fouling alternative to MBR processes [J].Desalination,2009,239( 1-3): 10-21.
  • 8Comelissen E R, Harmsen D, de Korte KF, et al. Membrane fouling and process performance of forward osmosis membranes on activated sludge [J].Joumal of Membrane Science,2008,319 (1-2): 158-168.
  • 9Zhang H M, Ma Y J, Jiang T, et al. Influence of activated sludge properties on flux behavior in osmosis membrane bioreactor (OMBR)[J].Jottmal 0f Membrane Science,2012,390-391:270-276.
  • 10Achilli A, Cath T Y, Childress A E, Selection of inorganic-based draw solutions for forward osmosis applications [J].Jottmal of Membrane Science,2010,364:233-241.

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