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二次生长法FAU型沸石膜的合成与表征 被引量:2

Synthesis and characterization of FAU zeolite membrane on seeded substrate
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摘要 采用二次生长成膜的方法,在合成液的配比为46Na2O:12.8SiO2:1Al2O3:4 500H2O的稀溶液中,在大孔a—Al2O3陶瓷管载体外表面,合成出致密的FAU型沸石膜,并用扫描电镜、X射线衍射以及气体渗透性能等手段对沸石膜进行了表征.用热浸渍法将与载体孔径尺寸相近的晶种引入载体表面,晶种嵌入了载体表面的孔口和次孔口,且均匀地分布在膜管表面,明显改善了载体的表面性质,促进了膜的生长.所制备的膜表面晶粒相互交织生长完好,致密,连续,规整,无裂缺,沸石膜厚约6~7μm.H2的渗透率为1.46×10^-6mol/(m^2·s·Pa),H/SF6的理想分离因子为9.67,高于其努森扩散值8.54.对稀溶液中沸石膜的形成机制也进行了探讨. Continuous ultra fine crystal FAU membranes were synthesized hydrothermally on the outer surface of - alumina support tube ( 12 mm o. d, and 8 mm i. d. ). The molar composition of the starting gel was 46Na2O: 12.8SiO2 : 1Al2O3 : 4 500H2O. Surface - modified tubes were seeded with zeolite X crystals prior to membrane synthesis. The seed layer with uniform crystal size that was as larger as the average pore diameter of the alumina supports on the substrate favored the formation of a continuous top - layer zeolite membrane during the growth. The substrate surface was improved significantly, and a uniform and smooth seed layer was formed by seeding. The outer surface of the tube is completely covered with zeolite crystals and the thickness of the membrane is about 6-7 μm. The measured permeability of H2 is about 1.46 × 10^-6 mol/(m2 ·s·Pa), and the ideal selectivity of H2/SF6 is 9.67, which is higher than the respective Knudsen diffusion ratio of 8.54. The mechanism of membrane formation was investigated.
出处 《膜科学与技术》 CAS CSCD 北大核心 2007年第6期9-12,共4页 Membrane Science and Technology
基金 国家自然科学基金资助项目(20176004)
关键词 FAU沸石 沸石膜 二次合成 晶种 机理 FAU-type zeolite zeolite membrane hydrothermal synthesis crystal seeds mechanism
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参考文献13

  • 1Piera E, Salomon M A, Corons J. Synthesis, characterization and separation properties of a composite mordenite/ ZSM - 5/ehabazite hydrophilie membrane [ J ]. J Membr Sci,1998,149: 99-- 114.
  • 2Weh K, Noack M, Sieber I. Permeation of single gases and gas mixtures through faujasite - type molecular sieve membranes[J ]. Micro Meso Mater, 2002,54: 27 - 36.
  • 3Kusakabe K, Kuroda T, Morooka S. Separation of carbon dioxide from nitrogen using ion - exchanged faujasitetype zeolite membranes formed on porous support tube[J]. J Membr Sci, 1998,148 : 13 - 23.
  • 4许中强,陈庆龄,卢冠忠,MA Yi-hua.在多孔陶瓷载体上X型分子筛生长成膜的研究[J].石油化工,2000,29(8):578-581. 被引量:6
  • 5许中强,陈庆龄,卢冠忠,马忆华.X型分子筛膜的制备及渗透性能的改善[J].石油炼制与化工,2001,32(9):43-48. 被引量:7
  • 6许中强,卢冠忠,陈庆龄,马忆华.二次生长法在多孔载体上制备X型分子筛膜[J].催化学报,2000,21(5):489-493. 被引量:5
  • 7许中强,陈庆龄,卢冠忠,MA Yi Hua.多孔不锈钢载体上X型分子筛的生长成膜[J].催化学报,2000,21(2):151-155. 被引量:6
  • 8Lai Z, Bonilla G, Diaz I, et al. Microstructural optimization of a zeolite membrane for organic vapor separation[J]. Science, 2003, 300(5618):456.
  • 9Li S G, Tuan Vu A, Falconer J L. X - type zeolite membranes: preparation, characterization, and pervaporation performance[J]. Micro Meso Mater, 2002,53:59 -70.
  • 10Coutinho D, Kenneth J, Balkus J. Preparation and characterization of zeolite X membranes via pulsed - laser deposition[J ]. Micro Meso Mater, 2002,52 : 79 - 91.

二级参考文献17

  • 1张雄福,刘海鸥,王金渠,King Lun Yeung.用亚微米级晶种涂层法合成NaA沸石膜及其结构表征[J].催化学报,2004,25(7):586-590. 被引量:7
  • 2Yan Y S,Ind Eng Chem Res,1995年,34卷,5期,1652页
  • 3Jia M D,J Membr Sci,1994年,90卷,1/2期,1页
  • 4Lai R,Ind Eng Chem Res,1998年,37卷,11期,4275页
  • 5Yan Y S,Ind Eng Chem Res,1995年,34卷,5期,1652页
  • 6Jia M D,USP 5 46 4798,1995年
  • 7Jia M D,J Membr Sci,1994年,90期,1页
  • 8Ma Y H,FormationofZeoliteMembranesfromSols[P] .WO :93 17781,1993年
  • 9Yan Y H,Ind Eng Chem Res,1995年,34卷,5期,1652页
  • 10许中强,陈庆龄,卢冠忠,MA Yi Hua.多孔不锈钢载体上X型分子筛的生长成膜[J].催化学报,2000,21(2):151-155. 被引量:6

共引文献20

同被引文献38

  • 1孙炜,陈中,黄素逸.浓度对NaCl水溶液影响的分子动力学模拟[J].武汉理工大学学报,2005,27(7):26-29. 被引量:8
  • 2王金渠,李邦民,刘建亮,鲁金明,鲍仲瑛,缪长喜.ZSM-5型沸石膜反应器在乙苯脱氢反应中的模式[J].化工学报,2006,57(8):1923-1926. 被引量:6
  • 3袁俊生,郭兆寿,张林栋.新型钾分子筛的表征及其对K^+的交换性能[J].过程工程学报,2006,6(6):903-906. 被引量:12
  • 4孔春龙,王金渠,鲁金明,陶凯.纳米晶种涂层法合成Silicalite-1沸石膜[J].过程工程学报,2007,7(1):71-74. 被引量:9
  • 5Mcleary E E, Jansen J C, Kapteijn F. Zeolite based films, membranes and membrane reactors: progress and prospects [ J ]. Micropor. Mesopor. Mater. ,2006,90( 1-3 ) : 198-220.
  • 6Ockwig N W, Nenoff T M. Mmembrane for hydrogen separation [ J ]. Chem. Rev. , 2007,107 ( 10 ) :4078 -4110.
  • 7Lu G Q,Costa J C D D, Duke M,et al. Inorganic membranes for hydrogen production and purification: a critical review and perspective [ J ]. J. Colloid. lnterf. Sci. ,2007,314(2):589-603.
  • 8Caro J, Noack M, Kolsch, et al. Zeolite membranes-state of their development and perspective [ J ]. Micropor. Mesopor. Mater. ,2000,38 ( 1 ) :3-24.
  • 9Tavolaro A, Drioli E. Zeolite membrane [ J ]. Adv. Mater. , 1999,11 ( 12 ) :975-996.
  • 10Algieri C, Bernardo P, Barbieri G, et al. A novel seeding procedure for preparing tubular NaY zeolite membranes[ J ]. Micropor. Mesopor. Mater. , 2009,119 (1-3) :129-136.

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