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Three-dimensional numerical analysis of proton exchange membrane fuel cells (PEMFCs) with conventional and interdigitated flow fields

机译:具有常规和指状流场的质子交换膜燃料电池(PEMFC)的三维数值分析

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摘要

A three-dimensional, steady-state mathematical model is described to investigate the fluid flow, species transport and electrochemical reaction in the PEM fuel cells with conventional and interdigitated flow fields. The multidimensional characteristics of flow, species and current distributions are computed by method based on volume-control finite-discrete technique. After comparing the absolute value of convective and diffusion component of oxygen flux quantitatively, we found that forced convection transport mechanism is dominant for the interdigitated flow field design, however the diffusion transport is dominant for the conventional flow field design. The performance and the pressure loss of these two different designs are calculated and compared; results show that interdigitated flow field design have better performance for its advantage in mass-transport ability, however have larger pressure loss for its flow through the electrode. Finally, experimental results reported in the literature and predicted polarization curves are compared to evaluate the numerical model employed.
机译:描述了一个三维稳态数学模型,以研究具有常规和指状流场的PEM燃料电池中的流体流动,物质传输和电化学反应。通过基于体积控制的有限离散技术的方法,计算了流量,种类和电流分布的多维特征。在定量比较氧气通量的对流和扩散分量的绝对值之后,我们发现强制对流输运机制是指状流场设计的主导,而扩散输运是常规流场设计的主导。计算并比较了这两种不同设计的性能和压力损失;结果表明,叉指式流场设计具有传质能力方面的优势,具有更好的性能,但是流经电极的压力损失却更大。最后,将文献报道的实验结果与预测的极化曲线进行比较,以评估所采用的数值模型。

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