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Modeling of assisted cold start processes with anode catalytic hydrogen-oxygen reaction in proton exchange membrane fuel cell

机译:质子交换膜燃料电池阳极催化氢氧反应辅助冷启动过程的建模

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摘要

Catalytic hydrogen-oxygen reaction is a potentially effective way to help start up proton exchange membrane fuel cells (PEMFCs) from sub-zero temperatures. In this study, the anode hydrogen-oxygen catalytic reaction is implemented in a three-dimensional multiphase cold start model. It is found that successful cold start from -20 ℃ can be achieved with the assist of the catalytic reaction in galvanostatic mode. With anode catalytic reaction, the start-up current density must be moderate, because a high current density lowers the assisted heating effect, and a low current density slows down the start-up process. The temperature difference between the anode and cathode catalyst layers (CLs) is negligible, which indicates that the heating location in the electrodes for the catalytic reaction makes no significant difference. The humidification of anode due to the catalytic reaction also reduces the ohmic resistance of the membrane, leading to enhanced performance during the start-up processes.
机译:催化氢氧反应是帮助从零以下温度启动质子交换膜燃料电池(PEMFC)的潜在有效方法。在这项研究中,阳极氢-氧催化反应是在三维多相冷启动模型中实现的。发现在恒电流模式下的催化反应可以成功地从-20℃开始冷启动。在阳极催化反应中,启动电流密度必须适中,因为高电流密度会降低辅助加热效果,而低电流密度会减慢启动过程。阳极和阴极催化剂层(CLs)之间的温差可以忽略不计,这表明电极中用于催化反应的加热位置没有明显的差异。由于催化反应而导致的阳极加湿也降低了膜的欧姆电阻,从而在启动过程中提高了性能。

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