Modeling Impedance Response of SOFC Cathodes Prepared by Infiltration

被引:52
作者
Bidrawn, F. [1 ]
Kuengas, R. [1 ]
Vohs, J. M. [1 ]
Gorte, R. J. [1 ]
机构
[1] Univ Penn, Dept Chem & Biomol Engn, Philadelphia, PA 19104 USA
关键词
OXIDE FUEL-CELLS; ANODE-SUPPORTED SOFCS; POROUS LA1-XSRXCOO3-DELTA ELECTRODES; YTTRIA-STABILIZED ZIRCONIA; ELECTROCHEMICAL PERFORMANCE; OXYGEN NONSTOICHIOMETRY; COMPOSITE CATHODES; THIN-FILM; TRANSPORT-PROPERTIES; SOLID ELECTROLYTES;
D O I
10.1149/1.3565174
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
A mathematical model has been developed to understand the performance of electrodes prepared by infiltration of La(0.8)Sr(0.2)FeO(3) (LSF) and La(0.8)Sr(0.2)MnO(3) (LSM) into yttria-stabilized zirconia (YSZ). The model calculates the resistances for the case where perovskite-coated, YSZ fins extend from the electrolyte. Two rate-limiting cases are considered: oxygen ion diffusion through the perovskite film or reactive adsorption of O(2) at the perovskite surface. Adsorption is treated as a reaction between gas-phase O(2) and oxygen vacancies, using equilibrium data. With the exception of the sticking probability, all parameters in the model are experimentally determined. Resistances and capacitances are calculated for LSF-YSZ and there is good agreement with experimental values at 973 K, assuming adsorption is rate limiting, with a sticking probability between 10(-3) and 10(-4) on vacancy sites. According to the model, perovskite ionic conductivity does not limit performance so long as it is above similar to 10(-7) S/cm. However, the structure of the YSZ scaffold, the ionic conductivity of the scaffold, and the slope of the perovskite redox isotherm significantly impact electrode impedance. Finally, it is shown that characteristic frequencies of the electrode cannot be used to distinguish when diffusion or adsorption is rate-limiting. (C) 2011 The Electrochemical Society. [DOI: 10.1149/1.3565174] All rights reserved.
引用
收藏
页码:B514 / B525
页数:12
相关论文
共 77 条
[1]   Mechanisms and rate laws for oxygen exchange on mixed-conducting oxide surfaces [J].
Adler, S. B. ;
Chen, X. Y. ;
Wilson, J. R. .
JOURNAL OF CATALYSIS, 2007, 245 (01) :91-109
[2]   Mechanism and kinetics of oxygen reduction on porous La1-xSrxCoO3-δ electrodes [J].
Adler, SB .
SOLID STATE IONICS, 1998, 111 (1-2) :125-134
[3]   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
[4]   Factors governing oxygen reduction in solid oxide fuel cell cathodes [J].
Adler, SB .
CHEMICAL REVIEWS, 2004, 104 (10) :4791-4843
[5]   Simplified processing of anode-supported thin film planar solid oxide fuel cells [J].
Basu, RN ;
Blass, G ;
Buchkremer, HP ;
Stöver, D ;
Tietz, F ;
Wessel, E ;
Vinke, IC .
JOURNAL OF THE EUROPEAN CERAMIC SOCIETY, 2005, 25 (04) :463-471
[6]   A new framework for physically based modeling of solid oxide fuel cells [J].
Bessler, Wolfgang G. ;
Gewies, Stefan ;
Vogler, Marcel .
ELECTROCHIMICA ACTA, 2007, 53 (04) :1782-1800
[7]   Rapid impedance modeling via potential step and current relaxation simulations [J].
Bessler, Wolfgang G. .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2007, 154 (11) :B1186-B1191
[8]   The influence of equilibrium potential on the hydrogen oxidation kinetics of SOFC anodes [J].
Bessler, Wolfgang G. ;
Warnatz, Juergen ;
Goodwin, David G. .
SOLID STATE IONICS, 2007, 177 (39-40) :3371-3383
[9]   The effect of Ca, Sr, and Ba doping on the ionic conductivity and cathode performance of LaFeO3 [J].
Bidrawn, F. ;
Lee, S. ;
Vohs, J. M. ;
Gorte, R. J. .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2008, 155 (07) :B660-B665
[10]   Efficient reduction of CO2 in a solid oxide electrolyzer [J].
Bidrawn, F. ;
Kim, G. ;
Corre, G. ;
Irvine, J. T. S. ;
Vohs, J. M. ;
Gorte, R. J. .
ELECTROCHEMICAL AND SOLID STATE LETTERS, 2008, 11 (09) :B167-B170