In a polymer electrolyte membrane (PEM) fuel cell, the condensed water in the gas channel prevents the supply of reactants to electrodes, which deteriorates the cell performance. The Lattice Boltzmann simulation has been conducted to understand the behavior of condensed water in the gas channels. The scheme of the two-phase flow with large density difference was applied to find the optimum gas channel design. The present simulation demonstrates the effect of the cross-sectional shape, the droplet initial position, droplet volume and the air flow velocity for a hydrophobic gas channel. Introducing a new dimensionless parameter, which is the pump work needed to remove the droplet from the gas channel, we investigate the effect of each parameter on the drain performance of a PEM fuel cell’s gas channel.
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ASME 2010 8th International Conference on Fuel Cell Science, Engineering and Technology
June 14–16, 2010
Brooklyn, New York, USA
Conference Sponsors:
- Advanced Energy Systems Division
ISBN:
978-0-7918-4404-5
PROCEEDINGS PAPER
Liquid Water and Gas Flow Simulation in a Channel of PEM Fuel Cells Using the Lattice Boltzmann Method
Ben Salah Yasser,
Ben Salah Yasser
Hokkaido University, Hokkaido, Japan
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Yutaka Tabe,
Yutaka Tabe
Hokkaido University, Hokkaido, Japan
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Takemi Chikahisa
Takemi Chikahisa
Hokkaido University, Hokkaido, Japan
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Ben Salah Yasser
Hokkaido University, Hokkaido, Japan
Yutaka Tabe
Hokkaido University, Hokkaido, Japan
Takemi Chikahisa
Hokkaido University, Hokkaido, Japan
Paper No:
FuelCell2010-33123, pp. 541-547; 7 pages
Published Online:
December 3, 2010
Citation
Yasser, BS, Tabe, Y, & Chikahisa, T. "Liquid Water and Gas Flow Simulation in a Channel of PEM Fuel Cells Using the Lattice Boltzmann Method." Proceedings of the ASME 2010 8th International Conference on Fuel Cell Science, Engineering and Technology. ASME 2010 8th International Fuel Cell Science, Engineering and Technology Conference: Volume 1. Brooklyn, New York, USA. June 14–16, 2010. pp. 541-547. ASME. https://doi.org/10.1115/FuelCell2010-33123
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