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Numerical Simulation on Impacts of Thickness of Nafion Series Membranes and Relative Humidity on PEMFC Operated at 363 K and 373 K

Author

Listed:
  • Akira Nishimura

    (Division of Mechanical Engineering, Graduate School of Engineering, Mie University, 1577 Kurimamachiya-cho, Tsu 514-8507, Mie, Japan)

  • Kyohei Toyoda

    (Division of Mechanical Engineering, Graduate School of Engineering, Mie University, 1577 Kurimamachiya-cho, Tsu 514-8507, Mie, Japan)

  • Yuya Kojima

    (Division of Mechanical Engineering, Graduate School of Engineering, Mie University, 1577 Kurimamachiya-cho, Tsu 514-8507, Mie, Japan)

  • Syogo Ito

    (Division of Mechanical Engineering, Graduate School of Engineering, Mie University, 1577 Kurimamachiya-cho, Tsu 514-8507, Mie, Japan)

  • Eric Hu

    (School of Mechanical Engineering, The University of Adelaide, Adelaide, SA 5005, Australia)

Abstract

The purpose of this study is to understand the impact of the thickness of Nafion membrane, which is a typical polymer electrolyte membrane (PEM) in Polymer Electrolyte Membrane Fuel Cells (PEMFCs), and relative humidity of supply gas on the distributions of H 2 , O 2 , H 2 O concentration and current density on the interface between a Nafion membrane and anode catalyst layer or the interface between a Nafion membrane and cathode catalyst layer. The effect of the initial temperature of the cell ( T ini ) is also investigated by the numerical simulation using the 3D model by COMSOL Multiphysics. As a result, the current density decreases along with the gas flow through the gas channel irrespective of the Nafion membrane thickness and T ini , which can be explained by the concentration distribution of H 2 and O 2 consumed by electrochemical reaction. The molar concentration of H 2 O decreases when the thickness of Nafion membrane increases, irrespective of T ini and the relative humidity of the supply gas. The current density increases with the increase in relative humidity of the supply gas, irrespective of the Nafion membrane thickness and T ini . This study recommends that a thinner Nafion membrane with well-humidified supply gas would promote high power generation at the target temperature of 363 K and 373 K.

Suggested Citation

  • Akira Nishimura & Kyohei Toyoda & Yuya Kojima & Syogo Ito & Eric Hu, 2021. "Numerical Simulation on Impacts of Thickness of Nafion Series Membranes and Relative Humidity on PEMFC Operated at 363 K and 373 K," Energies, MDPI, vol. 14(24), pages 1-24, December.
    • Handle: RePEc:gam:jeners:v:14:y:2021:i:24:p:8256-:d:697759
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    References listed on IDEAS

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    Cited by:

    1. Akira Nishimura & Daiki Mishima & Kyohei Toyoda & Syogo Ito & Mohan Lal Kolhe, 2023. "Numerical Simulation on Effect of Separator Thickness on Coupling Phenomena in Single Cell of PEFC under Higher Temperature Operation Condition at 363 K and 373 K," Energies, MDPI, vol. 16(2), pages 1-28, January.
    2. Hossein Pourrahmani & Hamed Shakeri & Jan Van herle, 2022. "Thermoelectric Generator as the Waste Heat Recovery Unit of Proton Exchange Membrane Fuel Cell: A Numerical Study," Energies, MDPI, vol. 15(9), pages 1-21, April.
    3. Siwen Gu & Jiaan Wang & Xinmin You & Yu Zhuang, 2023. "Investigating the Parameter-Driven Cathode Gas Diffusion of PEMFCs with a Piecewise Linearization Model," Energies, MDPI, vol. 16(9), pages 1-12, April.
    4. Akira Nishimura & Kyohei Toyoda & Daiki Mishima & Syogo Ito & Eric Hu, 2022. "Numerical Analysis on Impact of Thickness of PEM and GDL with and without MPL on Coupling Phenomena in PEFC Operated at Higher Temperature Such as 363 K and 373 K," Energies, MDPI, vol. 15(16), pages 1-31, August.

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