Three-dimensional simulation of chemically reacting gas flows in the porous support structure of an integrated-planar solid oxide fuel cell

被引:276
作者
Haberman, BA [1 ]
Young, JB [1 ]
机构
[1] Univ Cambridge, Engn Dept, Hopkinson Lab, Cambridge CB2 1PZ, England
基金
英国工程与自然科学研究理事会;
关键词
SOFQ; porous; simulation; chemical reaction;
D O I
10.1016/j.ijheatmasstransfer.2004.04.010
中图分类号
O414.1 [热力学];
学科分类号
摘要
The behaviour of an integrated-planar solid oxide fuel cell (IP-SOFC) strongly depends on the reactive diffusive flows within its porous support structure. Fuel is transported through the porous structure to the anodes of the electrochemical cells and the structure may be impregnated with the required catalysts for the steam reforming of methane. It is important to be able to calculate the distribution of gas properties within the porous structure in order to predict the performance of each cell and to determine the amount of internal reforming that takes place. This paper describes a three-dimensional numerical calculation method which has been developed to solve the governing equations in the porous structure. The calculation method includes the interaction between the flow in the porous medium and that in the adjacent fuel supply channel. The results highlight the importance of the kinetics of the reforming reaction and the thermal boundary conditions, both of which have a significant effect on the flow field within the porous structure. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3617 / 3629
页数:13
相关论文
共 25 条
[1]   METHANE STEAM REFORMING KINETICS FOR SOLID OXIDE FUEL-CELLS [J].
ACHENBACH, E ;
RIENSCHE, E .
JOURNAL OF POWER SOURCES, 1994, 52 (02) :283-288
[2]   Modeling of mass and heat transport in planar substrate type SOFCs [J].
Ackmann, T ;
de Haart, LGJ ;
Lehnert, W ;
Stolten, D .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2003, 150 (06) :A783-A789
[3]  
[Anonymous], ASME
[4]   BOUNDARY CONDITIONS AT A NATURALLY PERMEABLE WALL [J].
BEAVERS, GS ;
JOSEPH, DD .
JOURNAL OF FLUID MECHANICS, 1967, 30 :197-&
[5]  
BUSTAMANTE F, 2002, 47 FUEL CHEM DIV
[6]   Catalytic aspects of the steam reforming of hydrocarbons in internal reforming fuel cells [J].
Clarke, SH ;
Dicks, AL ;
Pointon, K ;
Smith, TA ;
Swann, A .
CATALYSIS TODAY, 1997, 38 (04) :411-423
[7]   Intrinsic reaction kinetics of methane steam reforming on a nickel/zirconia anode [J].
Dicks, AL ;
Pointon, KD ;
Siddle, A .
JOURNAL OF POWER SOURCES, 2000, 86 (1-2) :523-530
[8]   Structural properties of SOFC anodes and reactivity [J].
Drescher, I ;
Lehnert, W ;
Meusinger, J .
ELECTROCHIMICA ACTA, 1998, 43 (19-20) :3059-3068
[9]   SOFC technology development at Rolls-Royce [J].
Gardner, FJ ;
Day, MJ ;
Brandon, NP ;
Pashley, MN ;
Cassidy, M .
JOURNAL OF POWER SOURCES, 2000, 86 (1-2) :122-129
[10]   THE BRINKMAN MODEL FOR NATURAL-CONVECTION ABOUT A SEMI-INFINITE VERTICAL FLAT-PLATE IN A POROUS-MEDIUM [J].
HSU, CT ;
CHENG, P .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1985, 28 (03) :683-697