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首页> 外文期刊>International journal of hydrogen energy >Parametric studies on the membrane arrangement and porous properties of the flowing electrolyte channel in a flowing electrolyte-direct methanol fuel cell
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Parametric studies on the membrane arrangement and porous properties of the flowing electrolyte channel in a flowing electrolyte-direct methanol fuel cell

机译:流动电解质直接甲醇燃料电池中流动电解质通道的膜排列和多孔特性的参数研究

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摘要

A parametric study is conducted using a previously described one-dimensional, multi-phase model of a flowing electrolyte-direct methanol fuel cell (FE-DMFC). The anode and cathode membrane (AM and CM) thicknesses and porous properties (porosity and permeability) of the flowing electrolyte channel (FEC) were each individually varied, and recommendations on conditions which yield maximum power density and minimal methanol and water crossover are provided. The results of this study suggest that a thin AM and thick CM arrangement should be used; on the order of 25.4 mu m and 183 mu m respectively - corresponding to Nafion (R) 112 and 117 membranes respectively. The results also suggest that a fully open FEC (porosity of one) will provide the greatest performance. Although this configuration contradicts existing experimental data, considerations such as the choice of catalyst layer (CL) wettability and back pressure within the FEC are provided to achieve a membraneless FE-DMFC with a fully open FEC. If a porous FEC is to be used, the results suggest that a permeability greater than 10(-11) m(2) provide sufficient hydration within the CM. The trends regarding the membrane arrangement and FEC permeability are consistent with trends found from previous experimental studies. Copyright (c) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
机译:使用先前描述的流动电解质直接甲醇燃料电池(FE-DMFC)的一维,多相模型进行参数研究。流动电解质通道(FEC)的阳极膜和阴极膜(AM和CM)的厚度和多孔性(孔隙率和渗透性)各不相同,并提供了产生最大功率密度以及最小化甲醇和水交叉的条件的建议。这项研究的结果表明,应该使用薄的AM和厚的CM排列。分别约为25.4μm和183μm的量级-分别对应于Nafion112和117膜。结果还表明,完全开放的FEC(孔隙率为1)将提供最佳性能。尽管此配置与现有的实验数据相矛盾,但为了实现具有完全开放式FEC的无膜FE-DMFC,需要考虑诸如FEC内催化剂层(CL)润湿性和背压的选择等因素。如果要使用多孔FEC,则结果表明,渗透率大于10(-11)m(2)时,CM内具有足够的水合作用。关于膜排列和FEC渗透性的趋势与先前实验研究发现的趋势一致。 Hydrogen Energy Publications,LLC版权所有(c)2015。由Elsevier Ltd.出版。保留所有权利。

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