Application of Ba0.5Sr0.5Co0.8Fe0.2O3-δ membranes in an oxy-fuel combustion reactor

被引:16
|
作者
Mezghani, Khaled [1 ]
Hamza, Amir [1 ]
机构
[1] King Fahd Univ Petr & Minerals, Mech Engn Dept, Dhahran 31261, Saudi Arabia
关键词
Oxygen transport membranes; Oxygen separation; Carbon capture; Oxy-fuel combustion; HOLLOW-FIBER MEMBRANES; PERMEATION; STABILITY; CO2; CONDUCTIVITY; PERFORMANCE; SEPARATION; CAPTURE; CELLS;
D O I
10.1016/j.memsci.2016.07.001
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Oxygen separation from air through ceramic ion transport membranes is anticipated to be one of the technologies that can make fossil fuel power plants to operate without carbon dioxide (CO2) emission. Consequently, the level of carbon emission in the atmosphere, which causes global warming, could be contained. The most promising material for such ion transport membranes is the Ba0.5Sr0.5Co0.8Fe0.2O3 (delta) (BSCF), which has been reported to have the highest oxygen permeation flux. However, lack of chemical stability of these membranes in CO2 rich environment is recognized as a major problem. In this study, the performance and stability of BSCF membranes in an oxy-fuel combustor have been evaluated using methane gas. The flow rate of the methane (CH4) gas has been optimized to the value of 0.65 ml/min at 920 degrees C. Under this flow rate, the BSCF stability has also been evaluated. The study has shown that the BSCF stability depends on the amount of excess-oxygen in the reactor. If all oxygen, generated by the membrane, is consumed during the combustion reaction then BSCF starts to deteriorate and its permeability decreases with time. On the other hand, when the combustion reaction does not consume all oxygen, and a minimum excess-oxygen is retained, the BSCF remains stable with constant oxygen flux. This fact has been established using two BSCF membranes with different thicknesses and same exposed area of 113 mm(2). The first membrane has 1.4 mm thickness and its initial oxygen permeability under combustion reaction is 0.83 umol cm 2 s(-1) with an excess of 7.5% oxygen. After 190 h of combustion, the oxygen permeability has dropped to 0.76 umol cm(-2) s(-1) (7.9% reduction). The second BSCF membrane has a thickness of 1.0 mm produces 0.91 umol cm(-2) S-1 with a 15% excess oxygen during the combustion reaction. This membrane has shown excellent stability for more than 200 h of complete methane combustion. This is a remarkable result which shows that a carefully controlled fuel volume introduced in a BSCF membrane-reactor provides high oxygen output and excellent stability for a long period of time. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:254 / 262
页数:9
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