Abstract
In this paper, we extend a recent one-dimensional isothermal steady-state generalized Darcy model for two-phase flow in the porous cathode gas diffusion layer of a polymer electrolyte fuel cell, so as to include the effect of heat transfer. As for the isothermal case, we arrive at either a fixed- or free-boundary problem, depending on the main problem parameters: inlet temperature (\(T^\mathrm{in}\)), inlet water saturation (\(s^\mathrm{in}\)), inlet relative humidity (RH), porous medium hydrophobicity and cathode overpotential (\(\eta \)). The inclusion of heat transfer is found to limit the range of values of \(\eta ,T^\mathrm{in}\) and RH over which two-phase flow can occur, as compared to that predicted by the isothermal model. The ensuing non-isothermal two-phase flow model equations are then computed numerically, with particular care being required for the treatment of an integrably singular inter-phase mass transfer term.
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Acknowledgments
The authors acknowledge the support of the Mathematics Applications Consortium for Science and Industry (www.macsi.ul.ie), funded by the Science Foundation Ireland (SFI) Mathematics Initiative grant 06/MI/005 and SFI grant 12/IA/1683. The first author also acknowledges the award of a visiting researcher grant within the Government of Brazil’s “ Science without Borders” programme.
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Vynnycky, M., Gordon, A.D. Non-isothermal hydrophobicity-dependent two-phase flow in the porous cathode gas diffusion layer of a polymer electrolyte fuel cell. J Eng Math 92, 123–146 (2015). https://doi.org/10.1007/s10665-014-9748-8
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DOI: https://doi.org/10.1007/s10665-014-9748-8