Affiliation:
1. Karlsruhe Institute of Technology (KIT) Institute for Applied Materials – Electrochemical Technologies (IAM‐ET) Karlsruhe Germany
2. Karlsruhe Institute of Technology (KIT) Laboratory for Electron Microscopy Karlsruhe Germany
3. Kerafol Keramische Folien GmbH and Co. KG Eschenbach Germany
Abstract
AbstractSolid oxide cells (SOCs) offer the possibility to operate on hydrogen/steam (H2/H2O), carbon monoxide/carbon dioxide (CO/CO2), and mixtures thereof in the fuel cell as well as in the electrolyzer mode. In this study, the electrochemical processes in an electrolyte‐supported SOC exhibiting a Law Srx Coy Fez O(3‐δ) air electrode and a nickel/gadolinium‐doped ceria (Ni/CGO) fuel electrode (FE) were analyzed by electrochemical impedance spectroscopy, and the subsequent impedance data analysis by the distribution of relaxation times for CO/CO2 fuel mixtures. A physicochemical equivalent circuit model was fitted to the measured spectra. With the help of the extracted parameters, a zero‐dimensional direct current cell model was parametrized to simulate the current‐voltage behavior of the cell. This approach, previously implemented for H2/H2O fuel mixtures, is extended toward CO/CO2 fuels. It will be shown that the same model – with adapted parameters for the FE – can be applied. A comparison of measured and simulated current‐voltage curves showed an excellent agreement for both fuels and operating modes (solid oxide fuel cell/solid oxide electrolyzer cell). Simulations reveal that there is nearly no performance difference between H2O and CO2 electrolysis for the electrolyte‐supported cell with Ni/CGO FE in comparison to an anode‐supported cell with Ni/yttria‐stabilized zirconia FE.
Funder
Bundesministerium für Bildung und Forschung
Subject
Energy Engineering and Power Technology,Renewable Energy, Sustainability and the Environment
Cited by
3 articles.
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