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Investigation of convective transport in the gas diffusion layer used in polymer electrolyte fuel cells

Otávio Beruski1,*, Thiago Lopes1,2,†, Anthony R. J. Kucernak2,‡, and Joelma Perez1,§

  • 1Instituto de Química de São Carlos, Universidade de São Paulo, 13566-590 São Carlos, São Paulo, Brazil
  • 2Department of Chemistry, Imperial College London, South Kensington Campus, London SW7 2AZ, United Kingdom

  • *Present address: Nuclear and Energy Research Institute, IPEN/CNEN-SP, 05508-000 São Paulo, São Paulo, Brazil; oberuski@alumni.usp.br
  • Present address: Nuclear and Energy Research Institute, IPEN/CNEN-SP, 05508-000 São Paulo, São Paulo, Brazil; tlopeschem@gmail.com
  • anthony@imperial.ac.uk
  • §jperez@iqsc.usp.br

Phys. Rev. Fluids 2, 103501 – Published 17 October, 2017

DOI: https://doi.org/10.1103/PhysRevFluids.2.103501

Abstract

Recent experimental data on a fuel-cell-like system revealed insights into the fluid flow in both free and porous media. A computational model is used to investigate the momentum and species transport in such a system, solved using the finite element method. The model consists of a stationary, isothermal, diluted species transport in free and porous media flow. The momentum transport is treated using different formulations, namely, Stokes-Darcy, Darcy-Brinkman, and hybrid Stokes-Brinkman formulations. The species transport is given by the advection equation for a reactant diluted in air. The formulations are compared to each other and to the available experimental data, where it is concluded that the Darcy-Brinkman formulation reproduces the data appropriately. The validated model is used to investigate the contribution of convection in reactant transport in porous media of fuel cells. Convective transport provides a major contribution to reactant distribution in the so-called diffusion media. For a serpentine channel and flow with Re=260590, convection accounts for 29–58% of total reactant transport to the catalyst layer.

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