Effect of electrode microstructure on gas-phase diffusion in solid oxide fuel cells

Abstract The relation between electrode microstructure and gas diffusion has been investigated with different morphologies of Pt electrodes by using AC impedance techniques. The measurements were carried out at temperatures of 873–1273 K and oxygen partial pressure (P O 2 ) of 0.01–1 atm. Gas-phase diffusion was observed only for high-performance electrodes at the high-temperature (1073–1273 K) and low-oxygen-partial-pressure regions ( O 2 ). Considering the physical and electrochemical characteristics of impedance arcs, it was found that the arc at the frequency of below 1 Hz was related to gas conversion resistance, while the arc at the frequency of around 10 Hz represented pore diffusion resistance through the current-collecting part. For a thick electrode with a low porosity, however, gas diffusion resistance through pores of an electrode was observed at a frequency of around 100 Hz. From the results of a comparison of electrode performances with different electrode microstructures, electrochemical reaction sites (ERS) are supposed to be located at the peripheral line of Pt and YSZ as well as the Pt/YSZ interfaces where reaction gas can easily diffuse.

[1]  T. M. Gür,et al.  Importance of electrode/zirconia interface morphology in high-temperature solid electrolyte cells , 1987 .

[2]  T. Etsell,et al.  Overpotential Behavior of Stabilized Zirconia Solid Electrolyte Fuel Cells , 1971 .

[3]  Mogens Bjerg Mogensen,et al.  Gas Diffusion Impedance in Characterization of Solid Oxide Fuel Cell Anodes , 1999 .

[4]  Jonghee Han,et al.  Performance of anode-supported solid oxide fuel cell with La0.85Sr0.15MnO3 cathode modified by sol–gel coating technique , 2002 .

[5]  Suk Woo Nam,et al.  Characteristics of cathodic polarization at Pt/YSZ interface without the effect of electrode microstructure , 2003 .

[6]  Mogens Bjerg Mogensen,et al.  Gas Conversion Impedance: A Test Geometry Effect in Characterization of Solid Oxide Fuel Cell Anodes , 1998 .

[7]  Y. Yamakoshi,et al.  An Estimation of the Electrode‐Electrolyte Contact Area by Linear Sweep Voltammetry in Pt / ZrO2 Oxygen Electrodes , 1993 .

[8]  Svein Sunde,et al.  Monte Carlo Simulations of Polarization Resistance of Composite Electrodes for Solid Oxide Fuel Cells , 1996 .

[9]  M. Mogensen,et al.  Performance/structure correlation for composite SOFC cathodes , 1996 .

[10]  A. Nowick,et al.  Cathodic and Anodic Polarization Phenomena at Platinum Electrodes with Doped CeO2 as Electrolyte I . Steady‐State Overpotential , 1979 .

[11]  M. Nishiya,et al.  LaMnO3 air cathodes containing ZrO2 electrolyte for high temperature solid oxide fuel cells , 1992 .

[12]  J. E. Bauerle Study of solid electrolyte polarization by a complex admittance method , 1969 .

[13]  E. A. Mason,et al.  Gas Transport in Porous Media: The Dusty-Gas Model , 1983 .

[14]  J. Currie,et al.  Gaseous diffusion in porous media. Part 2. - Dry granular materials , 1960 .

[15]  Stuart B. Adler,et al.  Electrode Kinetics of Porous Mixed‐Conducting Oxygen Electrodes , 1996 .

[16]  T. M. Gür,et al.  Steady‐State D‐C Polarization Characteristics of the O 2, Pt/Stabilized Zirconia Interface , 1980 .

[17]  N. Themelis Transport and chemical rate phenomena , 1995 .