Effects of impurities on CO2/CH4 separations through SAPO-34 membranes

被引:101
作者
Li, SG [1 ]
Alvarado, G [1 ]
Noble, RD [1 ]
Falconer, JL [1 ]
机构
[1] Univ Colorado, Dept Chem & Biol Engn, Boulder, CO 80309 USA
关键词
gas separation; zeolite membrane; SAPO-34; carbon dioxide; methane; stability;
D O I
10.1016/j.memsci.2004.10.036
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effects of H2O, N-2, C2H4, C3H8, and n-C4H10 impurities on CO2/CH4 separation were studied for SAPO-34 membranes on stain less steel supports. The CO2 permeance decreased by 12%, but the CO2/CH4 selectivity was stable after 12 days of exposure to 170 ppm. Permeances and selectivity were not significantly affected when 3% N-2 was in the feed. Adding 1% hydrocarbons (C-2-C-4) to the feed decreased both permeance and selectivity; C-4 hydrocarbon caused the largest decrease because heavier hydrocarbons have higher heats of adsorption and thus inhibit CO2 permeation more significantly. Higher hydrocarbon concentrations decreased the permeance and selectivity more. When four impurities were in the feed, a SAPO-34 membrane separated CO2 from CH4 with selectivity as high as 55 and a CO2 permeance of 4.9 x 10(-8) mol/(m(2) s Pa) at 297 K and a feed pressure of 2.2 MPa. The percent impurity in the feed at low pressure was a good indication of the separation behavior at higher pressures. Higher impurity partial pressures did not result in more loss in permeance or selectivity when the CO2 and CH4 partial pressures were corresponding increased. The permeances and selectivities were not permanently reduced by impurities, but were restored by removing the impurity from the feed or by calcining. (c) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:59 / 66
页数:8
相关论文
共 30 条
[1]   Separation of gases with an A-type zeolite membrane [J].
Aoki, K ;
Kusakabe, K ;
Morooka, S .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (07) :2245-2251
[2]   Future directions of membrane gas separation technology [J].
Baker, RW .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (06) :1393-1411
[3]  
Brent M. L., 1984, Crystalline Silicoaluminophosphates, Patent No. [4,440,871, 4440871]
[4]   Preparation and characterization of zeolite X membranes via pulsed-laser deposition [J].
Coutinho, D ;
Balkus, KJ .
MICROPOROUS AND MESOPOROUS MATERIALS, 2002, 52 (02) :79-91
[5]   Separation of CO2-CH4 and CO2-N2 systems using ion-exchanged FAU-type zeolite membranes with different Si/Al ratios [J].
Hasegawa, Y ;
Tanaka, T ;
Watanabe, K ;
Jeong, BH ;
Kusakabe, K ;
Morooka, S .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2002, 19 (02) :309-313
[6]   Synthesis and separation performance of SSZ-13 zeolite membranes on tubular supports [J].
Kalipcilar, H ;
Bowen, TC ;
Noble, RD ;
Falconer, JL .
CHEMISTRY OF MATERIALS, 2002, 14 (08) :3458-3464
[7]   Preparation of Faujasite membranes and their permeation properties [J].
Kita, H ;
Fuchida, K ;
Horita, T ;
Asamura, H ;
Okamoto, K .
SEPARATION AND PURIFICATION TECHNOLOGY, 2001, 25 (1-3) :261-268
[8]   Pushing the limits on possibilities for large scale gas separation: which strategies? [J].
Koros, WJ ;
Mahajan, R .
JOURNAL OF MEMBRANE SCIENCE, 2000, 175 (02) :181-196
[9]   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
[10]   Properties and separation performance of Ge-ZSM-5 membranes [J].
Li, S ;
Tuan, VA ;
Falconer, JL ;
Noble, RD .
MICROPOROUS AND MESOPOROUS MATERIALS, 2003, 58 (02) :137-154