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新型聚酰胺复合正渗透膜的制备与表征 被引量:2

Studies on preparation and performance of novel polyamide composite FO membrane
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摘要 以聚砜为支撑基膜,以间苯二甲胺(m-XDA)和均苯三甲酰氯(TMC)为复合单体,经界面聚合反应制备聚酰胺复合正渗透膜。研究了聚酰胺复合正渗透膜的制备条件对膜性能的影响,并考察其耐氯性和抗污染能力。实验结果表明,选择合适的制备参数,16%PSf、6%PVP、60s挥发时间、40℃水浴、0.5%m-XDA、0.05%TMC、反应时间120s,制备出的复合正渗透膜性能优良。以去离子水为原料液,1mol/L NaCl为汲取液时的水通量最高达到17.5L/(m^2·h),反向扩散通量基本上在1.7mol/(m^2·h),对NaCl截留率为90%以上。在HA模拟溶液中,复合正渗透膜的水通量较正常情况下明显下降,再进一步比较pH值=5.5和8.0时可见,pH值较低时污染更为严重。对复合正渗透膜的耐氯性能进行考察,结果表明,复合正渗透膜的耐氯性在2 000ppmh左右。 The composite FO membrane was prepared through interfacial polymerization withm-xylylenediamine and trimesoyl chloride supported by PSf membrane.In this paper,the studies were focused on preparation and characterization of the FO composite membrane.The optimized parameters forcomposite FO membrane were 16%PSf,6%PVP,60 s evaporation time,40 ℃ water bath and 0.5%m-XDA,0.05% TMC,120 s reaction time.When deionized water is served as feed solution and 1 mol/L NaCl as draw solution,thewater flux of the FO composite membrane can reach to 17.5 L/(m2 . h ) and the solute reverses diffusion flux is 1.7 mol/(m2 .h),the membrane rejection of NaCl is about 90%.In the HA simulated solution,the water flux of composite FO membranewas decreased.After a further contrast of pH=5.5 and pH=8.0,a fact was con-firmed that lower pH value accompanies with more severe pollution.Studieson chlorine resistance of the com-posite FO membrane was shown that the chlorine resistance capacity of the composite FO membrane was up to 2 000 ppmh.
作者 肖维溢 管盼盼 王铎 XIAO Weiyi GUAN Panpan WANG Duo(College of Chemistry and Chemical Engineering, Ocean University of China, Qingdao 266100,China)
出处 《功能材料》 EI CAS CSCD 北大核心 2016年第B06期127-133,共7页 Journal of Functional Materials
基金 国家自然科学基金资助项目(20976171)
关键词 正渗透 复合膜 聚酰胺 耐氯性 耐污染性 forward osmosis composite membrane polyamide resistance to fouling chlorine resistance
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参考文献14

  • 1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
  • 2Petrotos K B, Quantick P, Petropakis H. A study of the direct osmotic concentration of tomatoJuice in tubular membrane-module configuration. I. The effect of certain basic process parameters on the process performance[J].Journal of Membrane Science, 1998, 150(1) :99-110.
  • 3Babu B R, Rastogi N K, Raghavarao K. Effect of process parameters on transmembrane flux during direct osmosis[J]'Journal of Membrane Science, 2006, 2800): 185-194.
  • 4Garg A, Gupta M, Bhargava H N. Effect of formulation parameters on the release characteristics of propranolol from asymmetric membrane coated tablets[J]. EuropeanJournal of Pharmaceutics and Biopharmaceutics, 2007, 67 (3): 725-731.
  • 5La Van D A, McGuire T, Langer R. Small-scale systems for in vivo drug delivery[J]. Nature Biotechnology, 2003, 21 (0) : 1184-119l.
  • 6邢珊珊,朱洪涛.正渗透污泥脱水工艺的影响因素研究[J].中国科技论文,2014,9(6):707-712. 被引量:3
  • 7曹瀛戈,张建中,徐明,等.正渗透技术及其在造纸工业中的应用探索[J].中国造纸学报,2014,16:297—301.
  • 8Ngai Yip, Alberto Tiraferri , William A Philip, et al. High performance thin-film composite forward osmosis membrane[J]' Environmental Science Technology, 2010, 44( 10): 3812-3818.
  • 9肖佩佩,殷勇,宋健峰,王周为,李雪梅,李刚,曾楚怡,何涛.界面聚合正渗透膜结构参数的调控[J].膜科学与技术,2014,34(5):40-43. 被引量:2
  • 10赵晓画,赵晓燕,王铭,纪俊玲.PVA-CS/PHBV复合膜制备及其性能研究[J].膜科学与技术,2014,34(3):63-68. 被引量:3

二级参考文献90

  • 1周勇,俞三传,高从堦.反渗透复合膜(Ⅰ)结构与性能[J].化工学报,2006,57(6):1370-1373. 被引量:17
  • 2张锴,俞昊,周哲,朱美芳,陈彦模.PHBV/CH_2Cl_2溶液体系静电纺纤维直径及其分布控制[J].合成纤维,2007,36(7):21-26. 被引量:2
  • 3Tzahi Y Cath, Amy E Childress, Menachem Elimelech. Forward osmosis: principles, applications, and recent developments[J].J Membr Sci.,281 (2006) 70-87.
  • 4Prachi Patel-Predd. Water desalination takes a step forward[J].Environ Sci Technol.,2006,40( 11 ):3454-3455.
  • 5K L Lee, R W Baker, H K Lonsdale. Membranes for power generation by pressure retarded osmosis [J].J Membr Sci.,1981:8 141-171.
  • 6J 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.
  • 7G T Gray, J R McCutcheon. M Elimelech, Internal concentration polarization in forward osmosis: role of membrane orientation[J]. Desalination,2006,197:1-8.
  • 8David R Lide. CRC handbook of chemistry and physics [M]. Boca Raton: CRC Press,2003.
  • 9James E Miller, Lindsey R Evans. Forward Osmosis: a new approach to water purification and desalination[R].Sandia:SANDIA REPORT SAND2006-4634,2006.
  • 10G W Batchelder. Process for the demineralization of water:US,3 171799 [P]. 1965 -03 -02.

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