Abstract
The performance of scaled-up (100 cm**2) fuel cells with cross flow of fuel and oxidant has been modeled using the polarization characteristics of small-scale (3 cm**2) fuel cells. The model also yields the two-dimensional (superficial) current distribution. The performance predicted by the model approximates to within 4% the experimental data if a suitable average value is assigned to the effective cell impedance. The latter depends on the inlet gas composition but does not vary much with the current; its value may be estimated from small-scale cell data. Carbon monoxide conversion contributes appreciably to the performance of low Btu cells; it tends to make the current distribution less uniform. The presence of methane must be considered in pressurized cells, but it does not appear to be formed to a significant extent. The relative contribution of mass transfer and kinetic resistance to the cell impedance are discussed in light of recent experimental results.
Cite
CITATION STYLE
Sampath, V., Sammells, A. F., & Selman, J. R. (1980). A Performance and Current Distribution Model for Scaled‐Up Molten Carbonate Fuel Cells. Journal of The Electrochemical Society, 127(1), 79–85. https://doi.org/10.1149/1.2129643
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