Efficient ceramic zeolite membranes for CO2/H2 separation

被引:59
|
作者
Korelskiy, D. [1 ]
Fouladvand, P. Ye S. [1 ]
Karimi, S. [1 ]
Sjoberg, E. [1 ]
Hedlund, J. [1 ]
机构
[1] Lulea Univ Technol, Chem Technol, SE-97187 Lulea, Sweden
基金
瑞典研究理事会;
关键词
ADSORPTION-ISOTHERMS; CALORIMETRIC HEATS; GAS PERMEATION; MFI MEMBRANES; CO2; REMOVAL; ETHANOL; CAPTURE; C2H6; O-2;
D O I
10.1039/c5ta02152a
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Membranes are considered one of the most promising technologies for CO2 separation from industrially important gas mixtures like synthesis gas or natural gas. In order for the membrane separation process to be efficient, membranes, in addition to being cost-effective, should be durable and possess high flux and sufficient selectivity. Current CO2-selective membranes are low flux polymeric membranes with limited chemical and thermal stability. In the present work, robust and high flux ceramic MFI zeolite membranes were prepared and evaluated for separation of CO2 from H-2, a process of great importance to synthesis gas processing, in a broad temperature range of 235-310 K and at an industrially relevant feed pressure of 9 bar. The observed membrane separation performance in terms of both selectivity and flux was superior to that previously reported for the state-of-the-art CO2-selective zeolite and polymeric membranes. Our initial cost estimate of the membrane modules showed that the present membranes were economically viable. We also showed that the ceramic zeolite membrane separation system would be much more compact than a system relying on polymeric membranes. Our findings therefore suggest that the developed high flux ceramic zeolite membranes have great potential for selective, cost-effective and sustainable removal of CO2 from synthesis gas.
引用
收藏
页码:12500 / 12506
页数:7
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