Permeation properties of bi-layered Al-ZSM-5/silicalite-1 membranes

被引:22
作者
Mabande, G. T. P.
Noack, M.
Avhale, A.
Koelsch, P.
Georgi, G.
Schwieger, W. [1 ]
Caro, J.
机构
[1] Univ Erlangen Nurnberg, Inst Chem React Engn, Egerlandstr 3, D-91058 Erlangen, Germany
[2] Berlin Adlershof eV, Inst Appl Chem, D-12489 Berlin, Germany
[3] Leibniz Univ Hannover, Inst Phys Chem & Electrochem, D-30167 Hannover, Germany
关键词
MFI membrane; stainless steel support; single gas permeation; mixture separation; bi-layered membrane;
D O I
10.1016/j.micromeso.2006.04.019
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The permeation properties of bi-layered Al-ZSM-5/Silicalite-1 membranes were studied using nitrogen/n-hexane permporosimetry, hydrogen/sulphur hexafluoride single gas permeation/mixture separation and n/i-pentane and p/o-xylene mixture separation. At 25 degrees C and in the 200 kPa feed-t-100 kPa permeate permeation mode hydrogen/sulphur hexafluoride permselectivities increased with the Al-ZSM-5 layer and decreased with the Silicalite-1 layer thickness. This behaviour was not related to defects but rather to different molecular interactions according to the chemical compositions of the membranes. Differences in hydrogen/sulphur hexafluoride permselectivities and separation factors were not as pronounced in most of the membranes for permeation measurements at 105 degrees C and in the 100-to-1 kPa permeation mode. The membranes composed of Al-ZSM-5 on Silicalite-1 layers were of better quality than membranes with the reverse order of layers according to permporosimetry measurements. The best membrane of this type had a hydrogen/sulphur hexafluoride ideal permselectivity and mixture separation factor of 210 and 97, respectively, at 105 degrees C. It achieved separation factors of 8 and 5 for the separation of 1: 1 mixtures of n/i-pentane and p/o-xylene, respectively. All membranes deteriorated in quality after calcination at temperatures >= 450 degrees C in air in comparison to the initial calcination at 400 degrees C in a nitrogen atmosphere with trace amounts of air. (C) 2006 Elsevier Inc. All rights reserved.
引用
收藏
页码:55 / 61
页数:7
相关论文
共 28 条
[1]   Gas permeation properties of ion-exchanged ZSM-5 zeolite membranes [J].
Aoki, K ;
Tuan, VA ;
Falconer, JL ;
Noble, RD .
MICROPOROUS AND MESOPOROUS MATERIALS, 2000, 39 (03) :485-492
[2]   Synthesis and applications of molecular sieve layers and membranes [J].
Bein, T .
CHEMISTRY OF MATERIALS, 1996, 8 (08) :1636-1653
[3]   Separations using zeolite membranes [J].
Coronas, J ;
Santamaría, J .
SEPARATION AND PURIFICATION METHODS, 1999, 28 (02) :127-177
[4]  
Gora L., 2001, STUD SURF SCI CATAL, V135, P3145
[5]   Progress in zeolitic membranes [J].
Jansen, K ;
Maschmeyer, T .
TOPICS IN CATALYSIS, 1999, 9 (1-2) :113-122
[6]   The influence of the calcination rate on silicalite-1 membranes [J].
Jareman, F ;
Andersson, C ;
Hedlund, J .
MICROPOROUS AND MESOPOROUS MATERIALS, 2005, 79 (1-3) :1-5
[7]   Effects of aluminum content on the separation properties of MFI membranes [J].
Jareman, F ;
Hedlund, J ;
Sterte, J .
SEPARATION AND PURIFICATION TECHNOLOGY, 2003, 32 (1-3) :159-163
[8]  
Lai W., 2000, US Patent, Patent No. 6037292
[9]   Gas and organic vapor permeation through b-oriented MFI membranes [J].
Lai, ZP ;
Tsapatsis, M .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (12) :3000-3007
[10]   Siliceous ZSM-5 membranes by secondary growth of b-oriented seed layers [J].
Lai, ZP ;
Tsapatsis, M ;
Nicolich, JR .
ADVANCED FUNCTIONAL MATERIALS, 2004, 14 (07) :716-729