[1]朱美华,袁晓蕾,梁 丽,等.合成条件对高硅SSZ-13分子筛膜单气体渗透性能的影响[J].江西师范大学学报(自然科学版),2017,(06):562-568.
 ZHU Meihua,YUAN Xiaolei,LIANG Li,et al.The Effects of Synthesis Condition on Single Gas Permeation Performance of High Silica SSZ-13 Zeolite Membrane[J].Journal of Jiangxi Normal University:Natural Science Edition,2017,(06):562-568.
点击复制

合成条件对高硅SSZ-13分子筛膜单气体渗透性能的影响()
分享到:

《江西师范大学学报》(自然科学版)[ISSN:1006-6977/CN:61-1281/TN]

卷:
期数:
2017年06期
页码:
562-568
栏目:
出版日期:
2017-12-01

文章信息/Info

Title:
The Effects of Synthesis Condition on Single Gas Permeation Performance of High Silica SSZ-13 Zeolite Membrane
作者:
朱美华袁晓蕾梁 丽吴庆喜张世坤王贺礼张 飞陈祥树
江西省无机膜材料工程技术中心,江西师范大学化学化工学院, 江西 南昌 330022
Author(s):
ZHU MeihuaYUAN XiaoleiLIANG LiWU QingxiZHANG ShikunWANG HeliZHANG FeiCHEN Xiangshu
Jiangxi Inorganic Membane Materials Engineering Research Center,College of Chemical and Chemistry Engineering,Jiangxi Normal University, Nanchang Jiangxi 330022, China
关键词:
高硅SSZ-13分子筛膜 Si/Al比 CO2/CH4气体分离
Keywords:
high silica SSZ-13 zeolite membrane Si/Al ratio CO2/CH4 gas separation
分类号:
O 647
文献标志码:
A
摘要:
采用2次水热合成法在多孔莫来石支撑体外表面上制备高硅SSZ-13分子筛膜,考察了合成溶胶中的Si/Al比、晶化时间、晶化温度、H2O/SiO2比对合成高硅SSZ-13分子筛膜的单气体渗透性能的影响.高硅SSZ-13分子筛膜的CO2和CH4的单气体渗透性能依赖于合成溶胶中的Si/Al比,Si/Al比越高,越有利于气体分离.其次,合成溶胶中H2O/SiO2比和晶化条件也能够影响分子筛晶体形貌、分子筛层厚度以及分子筛膜的单气体渗透性能.当合成溶胶的摩尔配比为1.000 SiO2:0.100 Na2O:0.100 TMAdaOH:80.000 H2O:0.005 Al2O3,晶化时间和温度分别为48 h和160 ℃时,制备的高硅SSZ-13分子筛膜具有最佳的单气体渗透性能,对CO2的渗透速率可达到3.0×10-7 mol· m-2·s-1·Pa-1),CO2/CH4的理想选择性为39.
Abstract:
High silica SSZ-13 zeolite membranes are prepared on the outer surface of the porous mullite support by secondary hydrothermal synthesis.Effect of synthesis conditions, such as SiO2/Al2O3 and H2O/SiO2 ratios of the precursor synthesis gel,crystallization time and temperature, on the single gas permeation performance of high silica SSZ-13 zeolite membranes are studied in details in this work.The CO2 and CH4 single gas permeation performance of high silica SSZ-13 zeolite membranes are greatly depended on the Si/Al ratio of the precursor gel,the high silica SSZ-13 zeolite membranes shows well gas separation performance for CO2/CH4 separation.The initial synthesis gel with the medium H2O/SiO2 ratio and crystallization conditions are crucial to zeolite crystals morphology, zeolite layer thickness and single gas permeation performance of high silica SSZ-13 zeolite membrane.When the molar composition of the precursor synthesis gel, the crystallization temperature and time are 1.000 SiO2:0.100 Na2O:0.100 TMAdaOH:80.000 H2O:0.005 Al2O3, 160 ℃ and 48 h,the CO2 permeances is 3.0×10-7 mol ·m-2·s-1·Pa-1and CO2/CH4 separation factor of the as-synthesized SSZ-13 zeolite membrane is 39.

参考文献/References:

[1] Yang Zhenzhen,He Liangnian,Gao Jiao,et al.Carbon dioxide utilization with C-N bond formation: carbon dioxide capture and subsequent conversion [J].Energy Environmental Science,2012,5(5):6602-6639.
[2] Amitesh M.Atomistic modeling toward high-efficiency carbon capture:A brief survey with a few illustrative examples [J].International Journal of Quantum Chemistry,2014,114(3):163-175.
[3] Ebner A D,Ritter J A.State-of-the-art adsorption and membrane separation processes for carbon dioxide production from carbon dixoxide emitting industries [J].Searation Science Technology,2009,44(6):273-1421.
[4] Baker R W.Future directions of membrane gas separation technology [J].Industrial Engineering Chemistry Research,2002,41(6):1393-1411.
[5] Marc P T.Porous inorganic membrane for CO2 capture: Present and prospects [J].Chemical Reviews,2014,114(2):1413-1492.
[6] Noack M,Mabande G T P,Caro J,et al.Influence of Si/Al ratio,pre-treatment and measurement conditions on permeation properties of MFI membranes on metallic and ceramic supports [J].Microporous and Mesoporous Materials,2005,82(1/2):147-157.
[7] Caro J,Albrecht D,Noack M.Why is it so extremely difficult to prepare shape-selective Al-rich zeolite membranes like LTA and FAU for gas separation [J].Separation and Purification Technology,2009,66(1):143-147.
[8] Noack M,Kolsch P,Dittmar A,et al.Effect of crystal intergrowth supporting substances on the permeation properties of MFI membranes with enhanced Al-content [J].Microporous and Mesoporous Materials,2006,97(1/2/3):88-96.
[9] Diestel L,Liu Xinlin,Li Yanshuo,et al.Comparative permeation studies on three supported membranes:Pure ZIF-8,pure polymethylphenylsiloxane,and mixed matrix membranes [J].Microporous and Mesoporous Materials,2014(189):210-215.
[10] Kosinov N,Auffret C,Gücüyener C,et al.High-flux high-silica SSZ-13 membrane for CO2 separation [J].Journal of Materials Chemistry A,2014,2(32):13083-13092.
[11] Kosinov N,Auffret C,Sripathi G,et al.Influence of support morphology on the detemplation and permeation of ZSM-5 and SSZ-13 zeolite membranes [J].Microporous and Mesoporous Materials,2014(197):268-277.
[12] Gascon J,Kapteijn F,Zorniza B,et al.Practical approach to zeolite memranes and coating:State of the art,opportunities,barriers,and future perspectives [J].Chemistry of Materials,2012,24(15):2829-2844.
[13] Noack M,K?lsch P,Seefeld V,et al.Influence of the Si/Al ratio on the permeation properties of MFI-membranes [J].Microporous and Mesoporous Materials,2005,79(1/2/3):329-337.
[14] Nishiyama N,Gora L,Teplyakov V,et al.Evaluation of reproducible high flux silicalite-1 membranes: Gas permeation and separation characterization [J].Separation and Purification Technology,2001,22/23(1/2/3):295-307.
[15] Huang Aisheng,Wang Nanyi,Caro J.Seeding-free synthesis of dense zeolite FAU membranes on 3-aminopropyltriethoaysilane-functionalized alumina supports [J].Journal of Membrane Science, 2012(389):272-279.
[16] Kondo M,Kita H.Permeation mechanism through zeolite NaA and T-type membranes for practical dehydration of organic solvents [J].Journal of Membrane Science,2010,361(1/2):223-231.
[17] Bergh J,Tihaya A,Kapteijn F.High temperature permeation and separation characteristics of an all-silica DDR zeolite membrane [J].Microporous and Mesoporous Materials,2010,132(1/2):137-147.
[18] Kosinov N,Auffret C,Gücüyener C,et al.High flux high-silica SSZ-13 membrane for CO2 separation [J].Journal of Materials Chemistry A,2014,2(32):13083-13092.
[19] Maghsoudi H,Soltanieh M.Simultaneous separation of H2S and CO2 from CH4 by a high silica CHA-type zeolite membrane [J].Journal of Membrane Science,2014,470:159-165.
[20] Nomura M,Tamashiro D,Sakai S,et al.Improvement of MOR zeolite membranes by using ion beam irradiation [J].Transaction of the Materials Research Society Japan,2013,38(3):481-484.
[21] Hedin N,DeMartin G J,Roth W J,et al.PFG NMR self-diffusion of small hydrocarbons in high silica DDR, CHA and LTA structures [J].Microporous and Mesoporous Materials,2008,109(1/2/3):327-334.
[22] Tomita T,Nakayama K,Sakai H.Gas separation characteristic of DDR type zeolite membrane [J].Microporous and Mesoporous Materials,2004,68(1/2/3):71-75.
[23] Hudson M R,Queen W L,Mason J A,et al.Unconventional, highly selective CO2 adsorption in zeolite SSZ-13 [J].Journal of American Chemistry Society,2012,134(4):1970-1973.
[24] Liu Bo,Zhou Rongfei,Bu Na,et al.Room-temperature ionic liquids modified zeolite SSZ-13 membranes for CO2/CH4 separation [J].Journal of Membrane Science,2017,524:12-19.
[25] Zheng Yihong,Hu Na,Wang Huamei,et al.Preparation of steam-stable high-silica CHA(SSZ-13)membranes for CO2/CH4 and C2H4/C2H6 separation [J].Journal of Membrane Science,2015,475: 303-310.
[26] Kida K,Maeta Y,Yogo K.Preparation and gas permeation properties on pure silica CHA-type zeolite membranes [J].Journal of Membrane Science,2017,522:363-370
[27] Wu Ting,Diaz M C,Zheng Yihong,et al.Influence of propane on CO2/CH4 and N2/CH4 separations in CHA zeolite membranes [J].Journal of Membrane Science,2015,473:201-209.
[28] Kosinov N,Auffret C,Borghuis G J,et al.Influence of the Si/Al ratio on the separation properties of SSZ-13 zeolite membranes [J].Journal of Membrane Science,2015,484:140-145.
[29] Huang Aisheng,Wang Nanyi,Caro J.Synthesis of multi-layer zeolite LTA membranes with enhanced gas separation performance by using 3-aminopropyltrirthoxysilane as interlayer [J].Microporous and Mesoporous Materials,2012(164):294-301.
[30] Eilertsen E A,Arstad B,Svelle S,et al.Single parameter synthesis of high silica CHA zeolites from fluoride media [J].Microporous and Mesoporous Materials,2012(153):94-99.

备注/Memo

备注/Memo:
收稿日期:2017-05-21基金项目:“863”计划(2012AA03A609),国家自然科学基金(20906042,20966003)和江西省自然科学基金(2015ACB20018)资助项目.通信作者:陈祥树(1966-),男,江西玉山人,教授,博士,博士生导师,主要从事膜分离与非均相催化的研究.E-mail:cxs66cn@jxnu.edu.cn
更新日期/Last Update: 1900-01-01