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低模板剂法合成Silicalite-1沸石膜及其气体渗透性能研究 被引量:2

Preparation and gas permeance separation property of silicalite-1 zeolite membrane with low-template method
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摘要 在较低的模板剂浓度下,采用二次生长法在大孔(孔径约4~6μm)α-Al2O3载体上合成Silicalite-1沸石膜,并采用X射线衍射法、扫描电子显微镜及不同温度下单组分气体渗透实验对所合成的沸石膜进行表征.结果表明,合成的是典型的Silicalite-1沸石膜,无其他杂质形成;制备的沸石膜连续、互生、致密,没有明显的缺陷.在40℃下H2的渗透速率为4.47×10^-7mol/(m^2·s·Pa),H2/SF6的理想分离系数44,远高于其Knudsen扩散系数8.54.在40~200℃之间,H2/SF6的理想分离系数曲线呈V型,H2的渗透速率几乎不变,N2的渗透速率随温度升高略下降。 Silicalite- 1 zeolite membrane was prepared on macroporous support (pore size of 4--6/lm) by secondary growth method with low - template. XRD, SEM and single gas permeability tests as a function of tem- perature were used to characterize assynthesized zeolite membrane. The results showed that the prepared membrane was typical zeolite silicalite - 1, continuous, compact and dense and no obvious defects. The perme- ability of H2 was 4.47 × 10^- 7 mol/(m2·s·Pa) and the ideal selectivity of H2/SF6 reached to 44 at 40℃. Moreover, the idea selectivity of H2/SF6 which was larger than its Knudsen ratio of 8.54. With the increase in the temperature (from 40 ℃to 200℃ ), the shape of idea selectivity curve of H2/SF6 was V type and the permeability of H2 was nearly constant, while the permeability of N2 decreased little.
出处 《膜科学与技术》 CAS CSCD 北大核心 2008年第4期67-70,共4页 Membrane Science and Technology
基金 中石化基金资助项目(406018)
关键词 SILICALITE-1沸石膜 低模板剂 单组分气体渗透 分离系数 silicalite - 1 membrane low - template single - gas p, ermeation selectivity
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参考文献11

  • 1Yuan W H, Lin Y S, Yang W S. Molecular sieving MFI - type zeolite membranes for pervaporation separation of xylene isomers[J]. J Am Chem Soc,2004, 126:4776- 4777.
  • 2Morigami Y, Kindi M, Abe J, et al. The first large-scale pervaporation plant using tubulartype module with zeolite NaA membrane [ J ]. Sep Purif Technol, 2001,25 : 251 - 260.
  • 3Caro J, Noack M, Kolsch P, et al. Zeolite membranes-state of their development and perspective [ J ]. Microp Mesop Mater, 2000,38: 3 - 24.
  • 4Tavolaro A, Drioli E. Zeolite membranes[J ]. Adv Mater, 1999, 11 : 975 - 996.
  • 5Lin Y S, Kumakiri I, Nair B N. Microporous inorganic membranes[J]. Sep Purif Meth,2002,31 (2) :229- 379.
  • 6Dong J H, Payzant E A, Hu M Z C, et al. Synthesis of MFI - type zeolite membranes on porous a - alumina supports by wet gel crystallization in the vapor phase[J]. J Mater Sci, 2003,38 : 979 - 985.
  • 7Wang Z B, Yan Y S. Controlling crystal orientation in zeolite MFI thin films by direct in situ crystallization[J ]. Chem Mater, 2001,13: 1101 - 1107.
  • 8Bemal M P, Xomeritakis G, Tsapatsis M. Tubular MFI zeolite membranes made by secondary (seed) growth [ J ]. Catal Today, 2001,67:101 - 107.
  • 9Engstrorm V, Mikailova B, Hedlund J, et al. The effect of seed size on the growth of silicalite- 1 films on gold surfaces[J]. Microp Mesop Mat, 2000,38:51 -60.
  • 10Lai R,Cravalas G R,Surface seeding in ZSM- 5 membrane properties[ J ]. Ind Eng Chem Res, 1998,37: 4275 - 4283.

同被引文献17

  • 1陈大茴,杨丽珠,郑晓咏.铁酸镍纳米粒子的制备与表征[J].佳木斯大学学报(自然科学版),2004,22(3):371-373. 被引量:5
  • 2龙英才,杨国荣,孙尧俊.硅沸石Silicalite-1吸附与脱附性质的研究Ⅰ.若干气体及小分子烃类的吸附与脱附[J].石油化工,1994,23(12):786-791. 被引量:3
  • 3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
  • 4Yuan W H, Lin Y S, Yang W S. Molecular sieving MFI--type zeo- lite membranes for pervaporation separation of xylene isomers [J]. J Am Chem Soc, 2004, 126:4776-4777.
  • 5Grahn M, Hedlund J. Maxwell--Stefan modeling of high flux tubu- lar silicalite-1 membranes for C02 removal from COdH2 gas mix- tures [J]. Journal of membrane science, 2014, 471:328-337.
  • 6Kong C L, Lu J M, Yang J H, et aL Catalytic dehydrogenation of ethylbenzene to styrene in a zeolite siliealite-I membrane reactor [J]. Journal of membrane science, 2007, 306:29-35.
  • 7Bowen T C,Noble R D,Falconer J L.Fundamentals and Applications of Pervaporation through Zeolite Membranes[J].J.Membr.Sci.,2004,245:1-33.
  • 8Nomura M,Bin T,Nakao S.Selective ethanol extraction from fermentation broth using a silicalite-1membrane[J].Sep Purif Technol,2002,27(1):59-66.
  • 9Matsusuda H,Yanagishita H,Negishi H.Improvement of ethanol selectivity of silicalite membrane in pervaporation by silicone rubber coating[J].J Membr Sci,2002,210(2):433-437.
  • 10T Sano,M Hasegawa,Y Kawakami et al.Potentials of silicalite membranes for the separafion of alcohol/water mixtures[J].Stud.Surf.Sci.Catal.,1994,84:1175-1184.

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