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Three-dimensional transient two-phase study of the cathode side of a PEM fuel cell

机译:PEM燃料电池阴极侧的三维瞬态两相研究

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A three-dimensional transient two-phase isothermal model has been developed for the cathode side of a proton exchange membrane fuel cell (PEMFC). This has been done in order to fully investigate the effects and the time variation of liquid water formation as well as the gas phase transport under the start up condition. It is considered that the generated water in the cathode catalyst layer (CL) is liquid water and that the gas diffusion layer (GDL) is hydrophobic. A non-equilibrium water condensation-evaporation is also assumed. The time variations of liquid water distribution in along-channel and through-plane directions are investigated. This is to determine the liquid water accumulation at the start up time (above the channel under the CL), then the movement of the liquid water in the domain and the final accumulation at the steady state condition (above the rib and near the CL). It has also been found that it takes less time for a high average current density to attain the steady state condition which is due to the capillary pressure gradient inside the porous media. Validation of the numerical results has been implemented via a polarization curve comparison with the experimental data. Both sets show good agreement.
机译:已经为质子交换膜燃料电池(PEMFC)的阴极侧建立了三维瞬态两相等温模型。这样做是为了充分研究启动条件下液态水形成的影响和时间变化以及气相传输。认为在阴极催化剂层(CL)中产生的水是液态水,并且气体扩散层(GDL)是疏水性的。还假定了非平衡水的冷凝蒸发。研究了沿通道和通过平面方向的液态水分布的时间变化。这是为了确定启动时(CL下方通道上方)的液态水累积量,然后确定域中液态水的运动以及稳态条件下(CL上方肋骨附近)的最终累积量。 。还已经发现,由于多孔介质内部的毛细管压力梯度,高平均电流密度花费较少的时间来达到稳态条件。数值结果的验证是通过与实验数据进行极化曲线比较来实现的。两组都显示出良好的一致性。

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