Gas separation characteristics of DDR type zeolite membrane

被引:343
作者
Tomita, T [1 ]
Nakayama, K [1 ]
Sakai, H [1 ]
机构
[1] NGK Insulators Ltd, Mat Res Lab, Mizuho Ku, Nagoya, Aichi 4678530, Japan
关键词
gas separation; DDR type zeolite;
D O I
10.1016/j.micromeso.2003.11.016
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The molecular-sieve DDR type zeolite membrane with an aperture of 0.36 x 0.44 nm was formed on a porous alumina substrate by hydrothermal process. The permeance through the membrane in the single gas feed of helium, hydrogen, carbon dioxide, oxygen, nitrogen, methane, n-butane, i-butane and sulfur hexafluoride were measured at 301 and 373 K up to 0.5 MPa. The permeance decreased by more than three orders of magnitude between 0.35 and 0.40 nm of the kinetic diameter of permeated gas at both 301 and 373 K. The separation factor of CO2 to CH4 in 50% CO2 and 50% CH4 mixed gas feed was 220 and 100 at 301 and 373 K, respectively at 0.5 MPa total gas feed pressure. The permeation properties were slightly affected by the water addition at 301 K. We conclude that the DDR type membrane has few defects and worked as molecular-sieving membrane. (C) 2003 Elsevier Inc. All rights reserved.
引用
收藏
页码:71 / 75
页数:5
相关论文
共 18 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]  
BRECK DW, 1974, ZEOLITE MOL SIEVES, P636
[3]  
DENEXTER MJ, 1994, STUD SURF SCI CATAL, V84, P1159
[4]   STUDIES ON CLATHRASILS .9. CRYSTAL-STRUCTURE OF DECA-DODECASIL 3R, THE MISSING LINK BETWEEN ZEOLITES AND CLATHRASILS [J].
GIES, H .
ZEITSCHRIFT FUR KRISTALLOGRAPHIE, 1986, 175 (1-2) :93-104
[5]  
Gies H., 1984, J INCLUSION PHENOM, V2, P275, DOI DOI 10.1007/BF00663266
[6]   Separation of nitrogen from oxygen using a titanosilicate membrane prepared on a porous α-alumina support tube [J].
Guan, GQ ;
Kusakabe, K ;
Morooka, S .
SEPARATION SCIENCE AND TECHNOLOGY, 2002, 37 (05) :1031-1039
[7]   Formation of a Y-type zeolite membrane on a porous alpha-alumina tube for gas separation [J].
Kusakabe, K ;
Kuroda, T ;
Murata, A ;
Morooka, S .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (03) :649-655
[8]   Synthesis and characterization of oriented MFI membranes prepared by secondary growth [J].
Lovallo, MC ;
Gouzinis, A ;
Tsapatsis, M .
AICHE JOURNAL, 1998, 44 (08) :1903-1913
[9]   Temperature and pressure effects on CO2 and CH4 permeation through MFI zeolite membranes [J].
Poshusta, JC ;
Noble, RD ;
Falconer, JL .
JOURNAL OF MEMBRANE SCIENCE, 1999, 160 (01) :115-125
[10]   Synthesis and permeation properties of SAPO-34 tubular membranes [J].
Poshusta, JC ;
Tuan, VA ;
Falconer, JL ;
Noble, RD .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (10) :3924-3929