Facile synthesis of LTA molecular sieve membranes on covalently functionalized supports by using diisocyanates as molecular linkers

被引:75
作者
Huang, Aisheng [1 ]
Caro, Juergen [1 ]
机构
[1] Leibniz Univ Hannover, Inst Phys Chem & Electrochem, D-30167 Hannover, Germany
基金
英国工程与自然科学研究理事会;
关键词
ZEOLITE NAA MEMBRANE; FORMATION MECHANISM; GAS PERMEATION; SECONDARY GROWTH; HIGH-PERMEANCE; A MEMBRANES; THIN-FILMS; SEPARATION; PERVAPORATION; PERFORMANCE;
D O I
10.1039/c1jm11549a
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Much effort has been paid towards the preparation of hydrophilic zeolite LTA membranes, and these zeolite LTA membranes have showed excellent performance in hydrophilic separations. However, there are only a few reports on successful shape-selective separations of gas mixtures on zeolite LTA membranes, most separation factors reported so far were lower than the corresponding Knudsen constants. It is often found that zeolite LTA membranes contain inter-crystalline defects to degrade their separation selectivity, which result from the problems that the isolated crystals on the support surface grow together to form a continuous supported LTA layer. In the present work, via urethane bonds formed by the reaction of isocyanate groups with surface hydroxyls, a facile synthesis method is developed for the seeding-free preparation of supported dense zeolite LTA layers by using 1,4-diisocyanate as a molecular binder to anchor the zeolite nutrients onto the support surface. The alpha-Al(2)O(3) supported zeolite LTA membrane with a thickness of about 3.5 mu m displays molecular sieving performance in gas permeation tests.
引用
收藏
页码:11424 / 11429
页数:6
相关论文
共 49 条
[1]   Gas permeation properties of A-type zeolite membrane formed on porous substrate by hydrothermal synthesis [J].
Aoki, K ;
Kusakabe, K ;
Morooka, S .
JOURNAL OF MEMBRANE SCIENCE, 1998, 141 (02) :197-205
[2]   Assembly of nanozeolite monolayers on the gold substrates of piezoelectric sensors [J].
Biemmi, Enrica ;
Bein, Thomas .
LANGMUIR, 2008, 24 (19) :11196-11202
[3]   Why is it so extremely difficult to prepare shape-selective Al-rich zeolite membranes like LTA and FAU for gas separation? [J].
Caro, J. ;
Albrecht, D. ;
Noack, M. .
SEPARATION AND PURIFICATION TECHNOLOGY, 2009, 66 (01) :143-147
[4]   Zeolite membranes - Recent developments and progress [J].
Caro, Juergen ;
Noack, Manfred .
MICROPOROUS AND MESOPOROUS MATERIALS, 2008, 115 (03) :215-233
[5]   Alumina-supported SAPO-34 membranes for CO2/CH4 separation [J].
Carreon, Moises A. ;
Li, Shiguang ;
Falconer, John L. ;
Noble, Richard D. .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 2008, 130 (16) :5412-+
[6]   SAPO-34 seeds and membranes prepared using multiple structure directing agents [J].
Carreon, Moises A. ;
Li, Shiguang ;
Falconer, John L. ;
Noble, Richard D. .
ADVANCED MATERIALS, 2008, 20 (04) :729-+
[7]   CONTROL OF TRANSPORT-PROPERTIES WITH A MICROPOROUS MEMBRANE REACTOR TO ENHANCE YIELDS IN DEHYDROGENATION REACTIONS [J].
CASANAVE, D ;
GIROIRFENDLER, A ;
SANCHEZ, J ;
LOUTATY, R ;
DALMON, JA .
CATALYSIS TODAY, 1995, 25 (3-4) :309-314
[8]  
Chau JLH, 2000, J MEMBRANE SCI, V164, P257
[9]   Uniformly a-oriented MFI zeolite films by secondary growth [J].
Choi, J ;
Ghosh, S ;
Lai, ZP ;
Tsapatsis, M .
ANGEWANDTE CHEMIE-INTERNATIONAL EDITION, 2006, 45 (07) :1154-1158
[10]   Diisocyanates as novel molecular binders for monolayer assembly of zeolite crystals on glass [J].
Chun, YS ;
Ha, K ;
Lee, YJ ;
Lee, JS ;
Kim, HS ;
Park, YS ;
Yoon, KB .
CHEMICAL COMMUNICATIONS, 2002, (17) :1846-1847