Gas permeation through DDR-type zeolite membranes at high temperatures

被引:190
作者
Kanezashi, Masakoto [1 ]
O'Brien-Abraham, Jessica [1 ]
Lin, Y. S. [1 ]
Suzuki, Kenji [2 ]
机构
[1] Arizona State Univ, Dept Chem Engn, Tempe, AZ 85287 USA
[2] NGK Insulat Ltd, New Products Dev Ctr, Mizuho Ku, Nagoya, Aichi 4678530, Japan
关键词
DDR-type zeolite membrane; gas permeation; diffusivity; high temperatures; diffusion theory;
D O I
10.1002/aic.11457
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
DDR-type zeolite membranes were prepared by the secondary growth method on porous a-alumina disk, followed by on-stream counter diffusion chemical vapor deposition modification to eliminate the intercrystalline micropores. Single gas permeation of He, H-2, CO2, and CO through this zeolite membrane before and after CVD modification was measured in 25-500 degrees C. Intracrystalline diffusivities for these four gases in DDR-type zeolite were obtained from the permeation data above 300 degrees C to examine the effects of the size and molecular weight of permeating gases on diffusion and permeation rate for this zeolite membrane. For the unmodified DDR-type zeolite membrane with presence of a small amount intercrystalline micropores the diffusivity (or permeance) with a low activation energy depends on both the size and molecular weight of permeating gases. For the CVD-modified DDR-type zeolite membrane with intercrystalline micropores eliminated, the activation energy for diffusion and diffusivity increases with increasing molecular size of the permeating gases. (C) 2008 American Institute of Chemical Engineers.
引用
收藏
页码:1478 / 1486
页数:9
相关论文
共 30 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]   Separation of inorganic/organic gas mixtures by porous silica membranes [J].
Asaeda, M ;
Yamasaki, S .
SEPARATION AND PURIFICATION TECHNOLOGY, 2001, 25 (1-3) :151-159
[3]   PREPARATION AND SEPARATION PROPERTIES OF SILICALITE COMPOSITE MEMBRANES [J].
BAI, CS ;
JIA, MD ;
FALCONER, JL ;
NOBLE, RD .
JOURNAL OF MEMBRANE SCIENCE, 1995, 105 (1-2) :79-87
[4]   Fundamentals and applications of pervaporation through zeolite membranes [J].
Bowen, TC ;
Noble, RD ;
Falconer, JL .
JOURNAL OF MEMBRANE SCIENCE, 2004, 245 (1-2) :1-33
[5]   Synthesis of NaA zeolite membrane with high performance [J].
Chen, XB ;
Yang, WS ;
Liu, J ;
Xu, XC ;
Huang, AS ;
Lin, LW .
JOURNAL OF MATERIALS SCIENCE LETTERS, 2002, 21 (13) :1023-1025
[6]   Separations of C4 and C6 isomers in ZSM-5 tubular membranes [J].
Coronas, J ;
Noble, RD ;
Falconer, JL .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (01) :166-176
[7]   AGING AND STABILITY OF MICROPOROUS SOL-GEL-MODIFIED CERAMIC MEMBRANES [J].
DELANGE, RSA ;
KEIZER, K ;
BURGGRAAF, AJ .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (11) :3838-3847
[8]  
DENEXTER MJ, 1994, STUD SURF SCI CATAL, V84, P1159
[9]   SULFUR-DIOXIDE SORPTION PROPERTIES AND THERMAL-STABILITY OF HYDROPHOBIC ZEOLITES [J].
DENG, SG ;
LIN, YS .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (11) :4063-4070
[10]   SILICALITE, A NEW HYDROPHOBIC CRYSTALLINE SILICA MOLECULAR-SIEVE [J].
FLANIGEN, EM ;
BENNETT, JM ;
GROSE, RW ;
COHEN, JP ;
PATTON, RL ;
KIRCHNER, RM ;
SMITH, JV .
NATURE, 1978, 271 (5645) :512-516