A detailed model for transport processes in a methane fed planar SOFC

被引:14
|
作者
Vakouftsi, E. [1 ]
Marnellos, G. [1 ,2 ]
Athanasiou, C. [1 ,2 ]
Coutelieris, F. A. [1 ,3 ]
机构
[1] Univ Western Macedonia, Dept Engn & Management Energy Resources, Bakola Sialvera 50100, Kozani, Greece
[2] Univ Thessaloniki, Chem Proc Engn Res Inst, Ctr Res & Technol, Thessaloniki 57001, Greece
[3] Natl Ctr Sci Res Demokritos, Aghia Paraskevi 15310, Greece
来源
关键词
Internal methane reforming; SOFC; Heat transfer; Modeling; OXIDE FUEL-CELL; KINETICS; ANODE; SIMULATION; SYNGAS; SYSTEM;
D O I
10.1016/j.cherd.2010.05.003
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In the present work the basic transport processes occurring in a planar solid oxide fuel cell (SOFC) were simulated. The Navier-Stokes and energy equations, including convective and diffusive terms, were numerically solved by the commercial CFD-ACE(+). program along with the mass and charge transport equations. To achieve this, a three-dimensional geometry for the planar fuel cell has been built. It was also assumed that the feedstream was a mixture of methane and steam in a ratio avoiding carbon formation. In accordance with the literature, the steam reforming reaction, the water-gas shift reaction as well as electrochemical reactions were introduced to the model. The spatial variation of the mixture's velocity, the temperature profiles and the species concentrations (mass fractions) were obtained. Furthermore, the effect of temperature on the produced current density was investigated and compared to the outcomes from isothermal imposed conditions. (C) 2010 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:224 / 229
页数:6
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