MFI membranes of different Si/Al ratios for pervaporation and steam permeation

被引:100
作者
Noack, M
Kölsch, P
Caro, J
Schneider, M
Toussaint, P
Sieber, I
机构
[1] Inst Appl Chem Berlin Adlershof EV, D-12489 Berlin, Germany
[2] Hahn Meitner Inst Kernforsch Berlin GmbH, D-12489 Berlin, Germany
关键词
binary mixtures; permeation; pervaporation; silicalite membrane; ZSM-5; membrane;
D O I
10.1016/S1387-1811(99)00226-7
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
For pervaporation and steam permeation, in one- and two-step crystallizations, respectively, two kinds of MFI membranes of different SiO2/Al2O3 ratio on a mesoporous alumina ceramic support have been prepared. In the onestep crystallization, using TPA-OH as template, a supported silicalite membrane was obtained by in situ crystallization. In the two-step crystallization, by first attaching seed crystals to the ceramic surface with electrostatic forces and then crystallizing a continuous MFI layer in a template-free synthesis, a ZSM-5 membrane was prepared. The membranes have been characterized by X-ray diffraction (XRD) and scanning electron microscopy (SEM) in combination with electron dispersive X-ray (EDX) line scan as well as by single gas and binary mixture permeation. In pervaporation and steam permeation measurements of water/iso-propanol and water/methanol mixtures, the silicalite membrane showed a hydrophobic and the ZSM-5 membrane a hydrophilic separation behavior. However, only the silicalite membrane obtained by one-step crystallization allows shape selective permeation such as the separation of n/isobutane and methanol/MTBE mixtures. In the case of the polycrystalline ZSM-5 membrane with columnar microstructure, a superposition of mass transport through the crystal boundaries and the crystals takes place. (C) 2000 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:253 / 265
页数:13
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