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高通量T型分子筛膜的制备 被引量:6

The Synthesis of High-Flux Zeolite T Membranes
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摘要 采用晶种诱导水热合成法,在配比n(SiO2):n(Al2O3):n(Na2O+K2O):n(NaF):n(H2O)=1.00:0.05:0.35:0—1.00:35.00的溶胶中,于管状大孔陶瓷载体上合成了高通量T型分子筛膜.氟盐的添加大大促进了T型分子筛的晶化速度.在优化条件下,在大孔氧化铝和莫来石载体上合成了c轴取向的致密T型分子筛晶体层,且表现出高的渗透汽化性能.在75℃时,在氧化铝载体上合成的分子筛膜在水/乙醇质量比为10/90体系中的平均渗透通量和分离因子分别为(3.01±0.15)kg·m^-2·h^-1和2140±100,比在莫来石载体上形成膜的平均分离因子升高31.29%,而渗透通量降低13.11%.同时研究了原料液浓度和分离温度对T型分子筛膜的渗透汽化性能的影响. Zeolite T membranes were synthesized by seed-induced hydrothermal synthesis using a gel with a molar ratio of n( SiO2 ) : n( Al2O3 ) : n( Na2O + K2O) : n(NaF) : n(H2O) = 1.00: 0.05: 0.35: 0.50:35.00 on macroporous tubular ceramics supports. The addition of fluoride salts promoted the crystallization of supported zeolite T layers. Under optimized conditions, the c-oriented compact zeolite T layers were synthesized on macroporous mullite and α-Al2O3 tubes. The membranes synthesized on α-Al2O3 tubes had an average total flux of(3.01 ±0.14)kg ·m^-2· h^-1 and an average separation factor of 2 140 ± 100 for the 90wt% ethanol aqueous solution at 75 ℃ ,which are 31.29% higher and 13.11% lower, respectively, than those of the mullite-supported membranes. The effects of op- eration temperature and concentration of water on the pervaporation properties of the membranes were also investiga- ted.
出处 《江西师范大学学报(自然科学版)》 CAS 北大核心 2013年第6期589-593,共5页 Journal of Jiangxi Normal University(Natural Science Edition)
基金 科技部"863"计划(2012AA03A609) 国家国际合作重大专项(2010DFA34440) 国家自然科学基金(20906042 20966003)资助项目
关键词 T型分子筛膜 氟盐 晶种诱导法 渗透汽化 zeolite T membrane fluoride seed-induced pervaporation
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参考文献17

  • 1Eliceche A M,Daviou C M,Hoch P M. Optimisation of azeotropic distillation columns combined with pervaporation membranes[J].{H}Computers and Chemical Engineering,2002.563-573.
  • 2Lipnizki F,Field R W,Ten P K. Pervaporation-based hybrid process:a review of process design,applications and economics[J].{H}Journal of Membrane Science,1999.183-210.
  • 3Feng Xianshe,Huang Robert Y M. Liquid separation by membrane pervaporation:a review[J].{H}Industrial and Engineering Chemistry Research,1997.1048-1066.
  • 4Cui Ying,Kita Hidetoshi,Okamoto Ken-Ichi. Zeolite T membrane:preparation,characterization,pervaporation of water/organic liquid mixtures and acid stability[J].{H}Journal of Membrane Science,2004,(1):17-27.
  • 5Rakoczy R A,Traa Y. Nanocrystalline zeolite A:synthesis,ion exchange and dealumination[J].{H}Microporous and Mesoporous Materials,2003.69-78.
  • 6Cui Ying,Kita Hidetoshi,Okamoto Ken-Ichi. Preparation and gas separation performance of zeolite T membrane[J].{H}Journal of Materials Chemistry,2004.924-932.
  • 7Mirfendereski S M,Mazaheri T,Sadrzadeh M. CO2 and CH4 permeation through T-type zeolite membranes:effect of synthesis parameters and feed pressure[J].{H}Separation and Purification Technology,2008.317-323.
  • 8周汉,李砚硕,朱广奇,刘杰,林励吾,杨维慎.微波合成a&b取向的T型分子筛膜及其在渗透汽化耦合酯化反应中的应用[J].催化学报,2008,29(7):592-594. 被引量:11
  • 9Zhou Han,Li Yanshuo,Zhu Guangqi. Microwave-assisted hydrothermal synthesis of a & b-oriented zeolite T membranes and their pervaporation properties[J].{H}Separation and Purification Technology,2009.164-172.
  • 10周荣飞,胡娜,袁慧,朱美华,王振卓,陈祥树.T型分子筛膜的合成、表征与渗透汽化性能[J].无机化学学报,2009,25(8):1439-1446. 被引量:13

二级参考文献61

  • 1吕丹,李邦民,王金渠,鲍仲英,殷德宏.NaA分子筛膜的水热合成及表征[J].安全与环境学报,2005,5(1):32-34. 被引量:2
  • 2黄爱生,李砚硕,刘杰,杨维慎.抽空涂晶法合成A型分子筛膜及渗透汽化性能研究[J].膜科学与技术,2005,25(2):5-10. 被引量:12
  • 3王卫平,潘秀莲,张小亮,熊国兴,杨维慎.钯/陶瓷中空纤维复合膜反应器中的水煤气变换反应[J].催化学报,2005,26(12):1042-1046. 被引量:8
  • 4Morigami Y, Kondo M, Abe J,et al. The first large-scale pervaporation plant using tubular-type module with zeolite NaA membrane [J]. Sep Purif Technol, 2001, 25(1-3): 251-260.
  • 5Jafar J J, Peter M, Budd R. Enhancement of esteritlcation reaction yield using zeolite A vapour permeation membrane [J]. J Membr Sci, 2002, 199:117-123.
  • 6Li Y S, Zhou H, Zhu G Q,et al. Hydrothermal stability of LTA zeolite membranes in pervaporation [J]. J Membr Sci, 2007, 297: 10- 15.
  • 7Kondo M, Komofi M, Kita H, et al.Tubular-type pervaporation module with zeolite NaA membrane [J]. J Membr Sci, 1997, 133: 133-141.
  • 8Okamoto K, Kita H, Horii K, et al. Zeohte NaA membrane:preparation:single-gas permeation, and pervapomtion and vapor permeation of water/organic liquid mixtures [J]. Ind Eng Chem Res, 2001(40): 163-175.
  • 9Shah D, Kissick K, Ghorpade A, et al. Pervaporation of alcohol-water and dimethylformamide-water mixtures using hydrophilic zeolite NaA membranes: mechanisms and experimental results [J]. J Membr Sci, 2000, 179: 185-205.
  • 10Kumakiri I, Yamaguchi T, Nakao S I. Ind. Eng. Chem. Res., 1999,38:4682-4688.

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