Electrochemical Capture of CO2 from Natural Gas Using a High-Temperature Ceramic-Carbonate Membrane

被引:11
|
作者
Tong, Jingjing [1 ,2 ]
Zhang, Lingling [2 ]
Fang, Jie [2 ]
Han, Minfang [1 ,3 ]
Huang, Kevin [2 ]
机构
[1] China Univ Min & Technol, Sch Chem & Environm Engn, Beijing 100083, Peoples R China
[2] Univ S Carolina, Dept Mech Engn, Columbia, SC 29201 USA
[3] Tsinghua Univ, Dept Thermal Engn, Beijing 100084, Peoples R China
基金
美国国家科学基金会;
关键词
SEPARATION; MIXTURES; CO2/CH4; CONDUCTIVITY; TRANSPORT; REMOVAL; DIOXIDE; PLAYS;
D O I
10.1149/2.0481504jes
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
This study reports the first investigation of using a ceramic-carbonate dual-phase membrane to electrochemically separate CO2 from a simulated natural gas. The CO2 permeation flux density was systematically studied as a function of temperature, CO2 partial pressure and time. As expected, the flux density was observed to increase with temperature and CO2 partial pressure. Long-term stability test showed that flux density experienced an initial performance-improving "break-in" period followed by a slow decay. Post-test microstructural analysis suggested that a gradual loss of carbonate during the test could be the cause of the flux-time behavior observed. (C) The Author(s) 2015. Published by ECS. This is an open access article distributed under the terms of the Creative Commons Attribution 4.0 License (CC BY, http://creativecommons.org/licenses/by/4.0/), which permits unrestricted reuse of the work in any medium, provided the original work is properly cited. All rights reserved.
引用
收藏
页码:E43 / E46
页数:4
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