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三醋酸纤维素正渗透膜的制备与性能初步研究 被引量:3

PREPARATION AND PRELIMINARY PERFORMANCE STUDY ON CELLULOSE TRIACETATE FORWARD OSMOSIS MEMBRANE
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摘要 以高分子物质三醋酸纤维素(CTA)作为膜材料主要成分,将其溶解于1,4-二氧六环溶剂中,加入致孔剂聚乙烯吡咯烷酮K30(PVP),加热搅拌形成均匀铸膜液采用相转化法制备正渗透膜。在温度为(20±1)℃,原溶液为去离子水,汲取液为2 mol/L氯化钠溶液的条件下测试膜的性能,研究了CTA和PVP含量及预蒸发时间3种因素对正渗透膜性能的影响。结果表明,在1,4-二氧六环和乳酸体积分别为170和13.2 mL下,当CTA和PVP的质量分别为23、4 g,预蒸发时间为60 s时,正渗透膜的性能最佳,水通量可达10.24 L/(m2·h),溶质反混通量为6.68 g/(m2·h)。 The forward osmosis membrane was prepared via phase inversion method by using cellulose Iriacetate (CTA) as main material, 1,4-dioxane as solvent, and polyvinyl pyrrolidone (PVP) as porogen. At approximately 20 ℃, the membrane performance was tested with 2 mol/L NaCI solution as the draw solution and deionized water as the feed solution. The effects of CTA content, PVP content and solvent evaporation time on the membrane performance were investigated: The results show that when 1,4-dioxane and lactic acid were 170 mL and 13.2 mL, the CTA and PVP content were 23 g and 4 g, and pre-evapomtion time was 60 s, the membrane has the optimum performance (the water flux was 10.24 L/(m2.h) and reverse solute flux was 6.68 g/(m2.h).
出处 《水处理技术》 CAS CSCD 北大核心 2013年第10期27-30,共4页 Technology of Water Treatment
基金 国家科技支撑计划课题(2012BAJ25B04)
关键词 三醋酸纤维素 正渗透膜 聚乙烯吡咯烷酮K30 膜制备 性能测试 cellulose triacetate forward osmosis membrane PVP membrane preparation performance test
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参考文献15

  • 1M A Shannon, P W Bohn, M Eltmelech, et al. Science and technology for waterlpurification in the coming decades [J].Nature,2008,452:301 - 310.
  • 2M A Montgomery, M Elimeleeh. Water and sanitation in developing countries: including health in the equation[J].Environment Science& Technology,2007,41:17-24.
  • 3M Elimelech. The global challenge for adequate and safe water[J]. Journal of Water Supply: Research and Teclmology-AQUA,2006, 55:3-10.
  • 4E I A. International, world energy outlook 2010 [R].The Energy Information Administration,2010.
  • 5C W King, M E Webber. Water intensity of transportation[J]. Environmental Science &Technology,2008,42:7866-7872.
  • 6K B Petrotos, H N Lazarides. Osmotic concentration of liquid foods [J].Journal of Food Engineering,2001,49:201-206.
  • 7K L Lee, R W Baker, H K Lonsdale. Membranes for power generation by pressure-retarded osmosis[J].Journal of Membrane Scienece, 1981, 8:141-171.
  • 8李刚,李雪梅,柳越,王铎,何涛,高从堦.正渗透原理及浓差极化现象[J].化学进展,2010,22(5):812-821. 被引量:38
  • 9李刚,李雪梅,王铎,何涛,高从堦.正渗透膜技术及其应用[J].化工进展,2010,29(8):1388-1398. 被引量:52
  • 10Shuaifei Zhao, Linda Zou, Chuyang Y Tang, et al. Recent developments in forward osmosis: Opportunities and challenges[J].Joumal of Membrane Scienec,2102,396:1-21.

二级参考文献128

  • 1Lee K L, Baker R W, Lonsdale H K. Journal of Membrane Science, 1981, 8(2) : 141-171.
  • 2McCutcheon J R, McGinnis R L, Elimelech M. Journal of Membrane Science, 2006, 278 (1/2) : 114-123.
  • 3Mehta G D, Loeb S. Journal of Membrane Science, 1978, 4: 261 -265.
  • 4Loeb S, Titelman L, Korngold E, et al. Journal of Membrane Science, 1997, 129(2) : 243-249.
  • 5Gray G T, McCutcheon J R, Elimelech M. Desalination, 2006, 197(1/3) : 1-8.
  • 6Mulder M. Basic Principles of Membrane Technology. Dordrecht: Kluwer Academic, 1996.
  • 7Tan C H, N g H Y. Journal of Membrane Science, 2008, 324(1/2) : 209-219.
  • 8Welty J R, Wicks C E, Wilson R E, et al. Fundamentals of momentum, heat, and mass transfer. 4th ed. NY: Wiley, 2000. 550-585.
  • 9Tan C H, Ng H Y. Journal of Membrane Science, 2008, 324( 1/ 2) : 209-219.
  • 10McCutcheon J R, Elimelech M. Journal of Membrane Science,2006, 284( 1/2): 237-247.

共引文献95

同被引文献63

  • 1吴翠玲,李新平,秦胜利.纤维素溶剂研究现状及应用前景[J].中国造纸学报,2004,19(2):171-175. 被引量:58
  • 2Mc Cutcheon J R, Elimelech M. Influence of membrane support layer hydrophobicity on water flux in osmotically driven membrane processes[J].J Membr Sci,2008,318(1/2):458-466.
  • 3Yu Y, Seo S, Kim I-C, Lee S. Nanoporous polyethersulfone (PES) membrane with enhanced flux applied in forward osmosis process [J].J Membr Sci,2011,375(1/2):63-68.
  • 4Arena J T, Mc Closkey B, Freeman B D, McCutcheon JR. Surface modification of thin film composite membrane support layers with polydopamine: Enabling use of reverse osmosis membranes in pressure retarded osmosis[J].J Membr Sci,2011,375(1/2):55-62.
  • 5Su J, ang Q, Teo JF, Chung T-S. Cellulose acetate nanofiltration hollow fiber membranes for forward osmosis processes[J].J Membr Sci,2010,355(1/2):36-44.
  • 6Cano-Odena A, Spilliers M, Dedroog T, et al. Optimization of cellulose acetate nanofiltration membranes for micropollutant removal via genetic algorithms and high throughput experimentation[J].J Membr Sci,2011,366(1/2):25-32.
  • 7Saimm M, Sereewatthanawut E, Li K, et al. Method for the preparation of cellulose acetate flat sheet composite membranes for forward osmosis-Desalination using MgSO4 draw solution[J].Desalination, 2011,273(2/3):299-307.
  • 8Zhang S, Wang K Y, Chung T-S, et al. Molecular design of the cellulose ester-based forward osmosis membranes for desalination [J].Chem Eng Sci,2011,66(9):2008-2018.
  • 9Ong R C, Chung T-S. Fabrication and positron annihilation ectroscopy (PAS) characterization of cellulose triacetate membranes for forward osmosis[J].J Membr Sci,2012,394/395:230-240.
  • 10Yip N Y, Tiraferri A, Phillip W A, et al. High performance thin-film composite forward osmosis membrane[J].Environ Sci Technol,2010, 44(10):3812-3818.

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