Theoretical optimisation of a SOFC composite cathode

被引:134
作者
Deseure, J [1 ]
Bultel, Y [1 ]
Dessemond, L [1 ]
Siebert, E [1 ]
机构
[1] UJF, ENSEEG, CNRS INPG, UMR 5631,LEPMI,Lab Electrochim & Physiocochim Mat, F-38402 St Martin Dheres, France
关键词
oxygen reduction; SOFC; modeling; composite electrode; graded electrode;
D O I
10.1016/j.electacta.2004.09.012
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
Theoretical calculations and experimental results have clearly demonstrated that a composite electrode should exhibit low activation polarisation by spreading the electrochemical active area within the volume of the electrode. The present modelling has been performed in order to Live a complete description of such an electrode structure as well as the processes occurring therein. A one-dimension flooded homogeneous model and a microscopic approach were used. The cathode was assumed to be composed of spherical particles of ionic (YSZ) and electronic conductors (M). The porous mixture of spherical grains was described as a face-centred cubic lattice. The microstructural parameters of interest include: the electrode thickness (L), the grain diameter (d(ysz) = d(M) = d(g)), the porosity (6), the specific adsorption surface area (av(ads)), the specific electrochemical surface area (av(tpb)), the pore diameter (d(p)) and the composition (e,). The proposed approach defines three independent parameters: E, dg and E,. For a given electrode composition, the results suggest that the nature of the rate determining step depends on grain size. An optimised porosity value is also determined. In case of a limitation by the charge transfer step, the model predicts that grading both composition and reaction sites is effective in increasing the electrochemical performances whereas grading porosity is not beneficial. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2037 / 2046
页数:10
相关论文
共 38 条
[1]   Mechanism and kinetics of oxygen reduction on porous La1-xSrxCoO3-δ electrodes [J].
Adler, SB .
SOLID STATE IONICS, 1998, 111 (1-2) :125-134
[2]   Electrode kinetics of porous mixed-conducting oxygen electrodes [J].
Adler, SB ;
Lane, JA ;
Steele, BCH .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1996, 143 (11) :3554-3564
[3]  
[Anonymous], 2001, GENIE REACTION CHIMI
[4]   Catalyst gradient for cathode active layer of proton exchange membrane fuel cell [J].
Antoine, O ;
Bultel, Y ;
Ozil, P ;
Durand, R .
ELECTROCHIMICA ACTA, 2000, 45 (27) :4493-4500
[5]  
BONANOS N, 2002, P 5 EUR SOL OX FUEL, P578
[6]   Structure/performance relations for Ni/yttria-stabilized zirconia anodes for solid oxide fuel cells [J].
Brown, M ;
Primdahl, S ;
Mogensen, M .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2000, 147 (02) :475-485
[7]   Modeling impedance diagrams of active layers in gas diffusion electrodes: diffusion, ohmic drop effects and multistep reactions [J].
Bultel, Y ;
Genies, L ;
Antoine, O ;
Ozil, P ;
Durand, R .
JOURNAL OF ELECTROANALYTICAL CHEMISTRY, 2002, 527 (1-2) :143-155
[8]  
CASSIDY M, 2000, P 4 EUR SOL OX FUEL, V2, P637
[9]   Microstructure and cathodic performance of La0.9Sr0.1MnO3/yttria-stabilized zirconia composite electrodes [J].
Choi, JH ;
Jang, JH ;
Oh, SM .
ELECTROCHIMICA ACTA, 2001, 46 (06) :867-874
[10]  
DESEURE J, 2003, THESIS INPG