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A Microscale Modeling Tool for the Design and Optimization of Solid Oxide Fuel Cells

机译:用于设计和优化固体氧化物燃料电池的微型建模工具

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A two dimensional numerical model of a solid oxide fuel cell (SOFC) with electrode functional layers is presented. The model incorporates the partial differential equations for mass transport, electric conduction and electrochemical reactions in the electrode functional layers, the anode support layer, the cathode current collection layer and at the electrode/electrolyte interfaces. A dusty gas model is used in modeling the gas transport in porous electrodes. The model is capable of providing results in good agreement with the experimental I-V relationship. Numerical examples are presented to illustrate the applications of this numerical model as a tool for the design and optimization of SOFCs. For a stack assembly of a pitch width of 2 mm and an interconnect-electrode contact resistance of 0.025 Ωcm2, a typical SOFC stack cell should consist of a rib width of 0.9 mm, a cathode current collection layer thickness of 200–300 μm, a cathode functional layer thickness of 20–40 μm, and an anode functional layer thickness of 10–20 μm in order to achieve optimal performance.
机译:提出了带有电极功能层的固体氧化物燃料电池(SOFC)的二维数值模型。该模型在电极功能层,阳极支撑层,阴极集流层以及电极/电解质界面处结合了用于质量传输,导电和电化学反应的偏微分方程。尘土气体模型用于模拟多孔电极中的气体传输。该模型能够提供与实验I-V关系良好吻合的结果。数值实例说明了该数值模型作为SOFC设计和优化工具的应用。对于节距宽度为2 mm且互连电极接触电阻为0.025Ωcm 2 的堆叠组件,典型的SOFC堆叠电池应包括0.9 mm的肋宽度,阴极集流层为了获得最佳性能,其最大厚度为200–300μm,阴极功能层厚度为20–40μm,阳极功能层厚度为10–20μm。

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