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首页> 外文期刊>International journal of hydrogen energy >3D non-isothermal dynamic simulation of high temperature proton exchange membrane fuel cell in the start-up process
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3D non-isothermal dynamic simulation of high temperature proton exchange membrane fuel cell in the start-up process

机译:3D高温质子交换膜燃料电池在启动过程中的非等温动态仿真

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摘要

High temperature proton exchange membrane fuel cell (HT-PEMFC) with phosphoric acid doped polybenzimidazole (PBI) electrolyte shows multiple advantages over conventional PEMFC working at below 373 K, such as faster electrochemical kinetics, simpler water management, higher carbon monoxide tolerance. However, starting HT-PEMFC from room temperature to the optimal operating temperature range (433.15 K-453.15 K) is still a serious challenge. In present work, the start-up strategy is proposed and evaluated and a three-dimensional non-isothermal dynamic model is developed to investigate start-up time and temperature distribution during the start-up process. The HT-PEMFC is pre-heated by gas to 393.15 K, followed by discharging a current from the cell for electrochemical heat generation. Firstly, different current loads are applied when the average temperature of membrane reaches 393.15 K. Then, the start-up time and temperature distribution of co-flow and counter-flow are compared at different current loads. Finally, the effect of inlet velocity and temperature on the start-up process are explored in the case of counter-flow. Numerical results clearly show that applied current load is necessary to reduce start-up time and just 0.1 A/cm(2) current load can reduce startup time by 45%. It is also found that co-flow takes 18.8% less time than counter-flow to heat membrane temperature to 393.15 K, but the maximum temperature difference of membrane is 39% higher than the counter-flow. Increasing the inlet gas flow velocity and temperature can shorten the start-up time but increases the temperature difference of the membrane. (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:高温质子交换膜燃料电池(HT-PEMFC)与磷酸掺杂的聚苯哌咪唑(PBI)电解质显示出在低于373K的常规PEMFC上的多种优点,例如更快的电化学动力学,更简单的水管理,高碳一氧化碳耐受性。然而,从室温开始HT-PEMFC到最佳工作温度范围(433.15 k-453.15 k)仍然是一个严峻的挑战。在目前的工作中,提出并评估了启动策略,并且开发了一种三维非等温动态模型来研究启动过程中的启动时间和温度分布。 HT-PEMFC通过气体预热至393.15k,然后排出来自电池的电流以进行电化学发热。首先,当膜的平均温度达到393.15k时,施加不同的电流载荷。然后,在不同电流负载下比较汇流和反流的启动时间和温度分布。最后,在反流的情况下探讨了入口速度和温度对启动过程的影响。数值结果清楚地表明,施加的电流负载是减少启动时间,只需0.1A / cm(2)电流负荷可以将启动时间降低45%。还发现,与逆流到热膜温度至393.15k的逆流,汇流量减少18.8%,但膜的最高温度差比计数器高出39%。增加入口气体流速和温度可以缩短启动时间,但增加了膜的温差。 (c)2020氢能源出版物LLC。 elsevier有限公司出版。保留所有权利。

著录项

  • 来源
    《International journal of hydrogen energy》 |2021年第2期|2577-2593|共17页
  • 作者单位

    Chongqing Univ Chongqing Automot Collaborat Innovat Ctr State Key Lab Mech Transmiss Sch Automot Engn Chongqing 400044 Peoples R China;

    Chongqing Univ Chongqing Automot Collaborat Innovat Ctr State Key Lab Mech Transmiss Sch Automot Engn Chongqing 400044 Peoples R China;

    China Automot Technol & Res Ctr Co Ltd Tianjin 300300 Peoples R China;

    Hong Kong Polytech Univ Bldg Energy Res Grp Dept Bldg & Real Estate Hung Hom Kowloon Hong Kong Peoples R China;

    Chongqing Changan New Energy Vehicle Technol Co L Chongqing 400000 Peoples R China;

    Chongqing Fuel Cell Technol Innovat & Ind Res Co Chongqing Peoples R China;

    Nanjing Tech Univ Coll Mat Sci & Engn 30 Puzhu Rd Nanjing 211816 Jiangsu Peoples R China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    HT-PEMFC; Start-up process; Temperature distribution; Counter-flow;

    机译:HT-PEMFC;启动过程;温度分布;反流;

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