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Measurement of effective gas diffusion coefficients of catalyst layers of PEM fuel cells with a Loschmidt diffusion cell

机译:用Loschmidt扩散池测量PEM燃料电池催化剂层的有效气体扩散系数

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摘要

In this work, using an in-house made Loschmidt diffusion cell, we measure the effective coefficient of dry gas (O\u2082\u2013N\u2082) diffusion in cathode catalyst layers of PEM fuel cells at 25 \ub0C and 1 atmosphere. The thicknesses of the catalyst layers under investigation are from 6 to 29\u3bcm. Each catalyst layer is deposited on an Al\u2082O\u2083 membrane substrate by an automated spray coater. Diffusion signal processing procedure is developed to deduce the effective diffusion coefficient, which is found to be (1.47\ub10.05)\ud710\u2212\u2077m\ub2 s\u2212\ub9 for the catalyst layers. Porosity and pore size distribution of the catalyst layers are also measured using Hg porosimetry. The diffusion resistance of the interface between the catalyst layer and the substrate is found to be negligible. The experimental results show that the O\u2082\u2013N\u2082 diffusion in the catalyst layers is dominated by the Knudsen effect.
机译:在这项工作中,我们使用内部制造的Loschmidt扩散池,测量了在25 ub0C和1个大气压下,PEM燃料电池阴极催化剂层中干气(O 2)扩散的有效系数。研究中的催化剂层的厚度为6至29立方厘米。每个催化剂层通过自动喷涂机沉积在Al \ u2082O \ u2083膜基材上。建立了扩散信号处理程序,推导了催化剂层的有效扩散系数,发现其为(1.47 \ ub10.05)\ ud710 \ u2212 \ u2077m \ ub2 s \ u2212 \ ub9。催化剂层的孔隙率和孔径分布也使用Hg孔隙率法测量。发现催化剂层和基底之间的界面的扩散阻力可忽略不计。实验结果表明,催化剂层中的O \ u2082 \ u2013N \ u2082扩散受克努森效应支配。

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