Journal
FUEL CELLS
Volume 4, Issue 4, Pages 358-364Publisher
WILEY-V C H VERLAG GMBH
DOI: 10.1002/fuce.200400034
Keywords
Diffusive Mass Transport; Geometry Variations; PEMFC Model; Planar PEMFC; Self-breathing PEMFC
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This paper presents model-based analysis of a proton exchange membrane fuel cell (PEMFC) with a planar design is the power supply for portable applications. The cell is operated with hydrogen and consists of an open cathode side allowing for passive, self-breathing, operation. This planar fuel cell is fabricated using printed circuit board (PCB) technology. Long-term stability of this type of fuel cell has been demonstrated. A stationary, two-dimensional, isothermal, mathematical model of the planar fuel cell is developed. Fickian diffusion of the gaseous components (O-2, H-2, H2O) in the gas diffusion layers and the catalyst layers a accounted for. The transport of water is considered in the gaseous phase only. The electrochemical reactions are described by the Tafel equation. The potential and current balance equations are solved separately for protons and electrons. The resulting system of partial differential equations is solved by a finite element method using FEMLAB (COMSOL Inc.) software. Three different cathode opening, rations are realized and the corresponding polarization curves are measured. The measurement arc compared to numerical simulation results. The model reproduces the shape of the measured polarization curves and comparable limiting current density values, due to mass transport limitation, are obtained. The simulated distribution of gaseous water shows that an increase of the water concentration under the rib occurs. It is concluded that liquid water may condense under the rib leading to a reduction of the open pore space accessible for gas transport. Thus, a broad rib not only hinders the oxygen supply itself, but may also cause additional mass transport problems due to the condensation of water.
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