Electrochemical separation of CO2 from a simulated flue gas with high-temperature ceramic-carbonate membrane: New observations

被引:37
|
作者
Tong, Jingjing [1 ,2 ]
Zhang, Lingling [2 ]
Han, Minfang [1 ,3 ]
Huang, Kevin [2 ]
机构
[1] China Univ Mining & 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
Carbonate; Ceramic; CO2; separation; Membrane; Mixed conductor; DIOXIDE PERMEATION; ELECTRICAL-CONDUCTIVITY; CAPTURE; ABSORPTION; TRANSPORT; MODEL;
D O I
10.1016/j.memsci.2014.12.017
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Development of highly efficient and cost-effective carbon capture and storage technology is vitally important to the reduction of carbon emissions and mitigation of global climate change. In this study, a ceramic-carbonate membrane conducting both oxide-ions and carbonate-ions is explored to directly separate CO2 from a simulated flue gas in the temperature range of 550-650 degrees C. The CO2 permeation flux density is found to increase with temperature as well as concentrations of CO2 and O-2, and stable over a testing period of 100 h. It is also observed for the first time that the membrane is permeable to O-2. A parallel mechanism responsible for the facilitated CO2 and O-2 transport is proposed. (C) 2014 Elsevier B.V. All rights reserved.
引用
收藏
页码:1 / 6
页数:6
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