Solid-Gas Interactions of Nanoscaled La0.6Sr0.4CoO3‑δ and Their Impacts
This contribution will focus on the solid/gas interaction between nanoscaled La0.6Sr0.4CoO3‑δ (LSC) thin films and the surrounding gas atmosphere in terms of gas composition and partial pressures and discusses the resulting influence on the electrochemical properties. The thin-film cathodes were derived by a sol-gel process based on metal organic precursors and were directly deposited onto Ce0.9Gd0.1O1.95electrolyte pellets .
Differently designed experiments and thermodynamic calculations were performed in order to investigate the influence of water-vapor or carbon dioxide in the surrounding atmosphere and of the oxygen partial pressure on the cathode performance. The latter plays an important role during the cathode fabrication process. Low oxygen partial pressures occur during the thermal decomposition of the metal organic precursors of the cathode material, which lead to the formation of a beneficial hetero-interface of (La,Sr)2CoO4±δ and La0.6Sr0.4CoO3-δ, as could be shown by thermodynamic calculations . The influence of H2O(g) and CO2 on the electrochemical performance was investigated experimentally in a temperature range of 400 … 650 °C . Both gases negatively affect the solid/gas electrochemistry of the cathode (cf. Figure 1). CO2 leads to poisoning of the cathode, which is reversible at temperatures above 500 °C. At temperatures below 500 °C a regeneration of the cathodes could only be achieved by a treatment in pure oxygen. In contrast to this behavior, H2O leads to an irreversible and continuously increasing degradation. A detailed analysis of electrochemical impedance spectroscopy data disclosed, which polarization processes are majorly affected. CO2 mainly affects the surface-exchange reaction, whereas H2O – in the time frame of the test – impedes the oxygen ion diffusion within the cathode.
The results demonstrate the changeability of the solid-gas electrochemistry at mixed conducting cathodes. Based on these results operation strategies in terms of optimal operation temperature and required gas preprocessing (e.g. drying of oxidant gas) can be deduced, potentially decreasing the degradation during operation.
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