Journal of The Electrochemical Society · 1984 · 96 citations · 0 references
EngineeringChemical EngineeringMaterials EngineeringElectrochemical EngineeringElectrochemistrySurface ScienceElectrochemical CellsElectrochemical Energy ConversionElectrochemical KineticsElectrode KineticsElectrode MaterialsFuel CellsAnode PerformanceElectrode ProcessesElectrode Reaction KineticsFuel Cell ElectrodesFuel Cell Performance ModelingIonic ConductionMass Transport MechanismsMolten Carbonate Fuel Cells
A dual‐porosity, agglomerate‐type model for the porous anode and cathode of the molten carbonate fuel cell is developed and used to predict electrode performance in a small, differential‐conversion, cell. The model is based on a phenomenological treatment of mass transport, electrode kinetics, and ionic conduction, combined with structural assumptions. The model predicts the steady‐state performance, given a minimum number of structural parameters. Comparison with experimental data for a 3 cm2 anode and cathode shows good agreement for plausible values of these parameters.