Mathematical modeling of mass and charge transport and reaction in a solid oxide fuel cell with mixed ionic conduction

被引:21
作者
Bertei, A. [1 ]
Thorel, A. S. [2 ]
Bessler, W. G. [3 ,4 ]
Nicolella, C. [1 ]
机构
[1] Univ Pisa, Dept Chem Engn, I-56126 Pisa, Italy
[2] Mines Paris Tech, UMR CNRS 7633, Ctr Mat, F-91003 Evry, France
[3] Inst Tech Thermodynam, German Aerosp Ctr DLR, D-70569 Stuttgart, Germany
[4] Univ Stuttgart, Inst Thermodynam & Thermal Engn, D-70550 Stuttgart, Germany
关键词
Solid oxide fuel cell; IDEAL-Cell; Porous composite membrane; Mathematical modeling; Transport processes in porous media; Design analysis; COMPUTER-SIMULATION; RANDOM PACKING; SOFC; PERCOLATION; PROTON; GASES; SIZE;
D O I
10.1016/j.ces.2011.10.025
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A mathematical model for the description of transport phenomena and reactions in an innovative solid oxide fuel cell (called IDEAL-Cell) under steady-state conditions is presented. This cell is characterized by an intermediate porous composite layer (called central membrane) between cathodic and anodic compartments, which shows mixed conduction of protons and oxygen ions and offers active sites for their recombination to form water vapor. This paper presents an original model of charge transport and reaction in the central membrane. The model, based on local mass and charge balances, accounts for mixed conduction in the solid phase, diffusion and convection in the gas phase and reaction at the solid/gas interface. The model domain is resolved in a continuum approach by using effective properties related to morphology and material properties through percolation theory. The model predictions are successfully compared with experimental data, which provide an estimate of the kinetic parameter of the water recombination reaction. Simulations show a strong dependence of predicted results on the kinetic constant of the water incorporation reaction and the effective conductivities. A design analysis on porosity, thickness, particle dimension, composition of central membrane and cell radius is performed and an optimal membrane design is obtained. (C ) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:606 / 616
页数:11
相关论文
共 31 条
[11]   COMPUTER-SIMULATION OF ISOTROPIC, HOMOGENEOUS, DENSE RANDOM PACKING OF EQUAL SPHERES [J].
JODREY, WS ;
TORY, EM .
POWDER TECHNOLOGY, 1981, 30 (02) :111-118
[12]   Mass transfer within the gas-phase of porous media [J].
Kast, W ;
Hohenthanner, CR .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2000, 43 (05) :807-823
[13]   Protonic conduction in Zr-substituted BaCeO3 [J].
Katahira, K ;
Kohchi, Y ;
Shimura, T ;
Iwahara, H .
SOLID STATE IONICS, 2000, 138 (1-2) :91-98
[14]   Engineering of microstructure and design of a planar porous composite SOFC cathode: A numerical analysis [J].
Kenney, Ben ;
Karan, Kunal .
SOLID STATE IONICS, 2007, 178 (3-4) :297-306
[15]   Computation of TPB length, surface area and pore size from numerical reconstruction of composite solid oxide fuel cell electrodes [J].
Kenney, Ben ;
Valdmanis, Mikelis ;
Baker, Craig ;
Pharoah, J. G. ;
Karan, Kunal .
JOURNAL OF POWER SOURCES, 2009, 189 (02) :1051-1059
[16]   Proton-conducting oxides [J].
Kreuer, KD .
ANNUAL REVIEW OF MATERIALS RESEARCH, 2003, 33 :333-359
[17]   Aspects of the formation and mobility of protonic charge carriers and the stability of perovskite-type oxides [J].
Kreuer, KD .
SOLID STATE IONICS, 1999, 125 (1-4) :285-302
[18]  
Larminie J., 2018, Fuel Cell Systems Explained
[19]  
Mason E.A., 1983, GAS TRANSPORT POROUS
[20]   A comprehensive micro-scale model for transport and reaction in intermediate temperature solid oxide fuel cells [J].
Nam, JH ;
Jeon, DH .
ELECTROCHIMICA ACTA, 2006, 51 (17) :3446-3460