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Management of the gas-phase and surface chemistry in methane-fueled catalytic micro-combustors

机译:甲烷燃料催化微燃烧器中气相和表面化学的管理

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摘要

Design guidelines for the management of gas-phase and surface chemistry in methane-fueled catalytic micro-combustors were developed. To find out how the interplay between gas-phase and surface chemistry is affected by different operating conditions, computational fluid dynamics (CFD) simulations were performed using a two-dimensional model with detailed chemistry and transport. The effects of feed composition, inlet velocity, combustor dimension, and heat loss were studied to determine the relative role of gas phase and surface chemistry and to understand the important factors controlling chemistry. To delineate the homogeneous-heterogeneous coupling mechanisms, comparisons were made between results for cases where only heterogeneous reactions were allowed, only homogeneous reactions were allowed, and where both mechanisms were allowed. The competition and synergism between gas-phase and surface chemistry were delineated for obtaining design insights. It was shown that the contribution of gas-phase chemistry depends strongly upon the operating conditions; it decreases with decreasing channel size, increasing the heat loss to the surroundings, and the composition away from the stoichiometric point. The crucial factor controlling chemistry is the maximum temperature. To minimize gas-phase chemistry, temperatures should be kept as low as possible in the stable operating regime. Gas-phase chemistry can be either promoted or inhibited by surface chemistry, depending on flow velocity; it can be sustained in catalytic micro-channels (as low as 0.2 mm) well below the quenching distance due to the promoting effect induced by surface heating. Surface chemistry alone can occur under appropriate operating conditions such as compositions, flow velocities, and heat exchange/heat loss rates. Contribution diagrams were constructed and design recommendations were finally made. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:制定了甲烷燃料催化微型燃烧器中气相和表面化学管理的设计指南。为了发现气相和表面化学之间的相互作用如何受到不同操作条件的影响,使用具有详细化学和传输的二维模型进行了计算流体动力学(CFD)模拟。研究了进料组成,入口速度,燃烧器尺寸和热损失的影响,以确定气相和表面化学的相对作用,并了解控制化学的重要因素。为了描述均相-异质偶联机理,在仅允许异质反应,仅允许均相反应以及允许两种机理的情况下的结果之间进行了比较。描绘了气相和表面化学之间的竞争和协同作用以获得设计见解。结果表明,气相化学的贡献在很大程度上取决于操作条件。它随着通道尺寸的减小而减小,从而增加了向周围环境的热损失,并使成分远离化学计量点。控制化学反应的关键因素是最高温度。为了最大程度地减少气相化学反应,应在稳定的操作条件下将温度保持在尽可能低的水平。取决于流速,气相化学可以通过表面化学促进或抑制。由于表面加热引起的促进作用,它可以维持在远低于淬灭距离的催化微通道(低至0.2 mm)中。单独的表面化学反应可以在适当的操作条件下发生,例如组成,流速和热交换/热损失率。绘制了贡献图并最终提出了设计建议。 (C)2017氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

著录项

  • 来源
    《International journal of hydrogen energy》 |2017年第30期|19079-19095|共17页
  • 作者单位

    Henan Polytech Univ, Sch Mech & Power Engn, Dept Energy & Power Engn, 2000 Century Ave, Jiaozuo 454000, Henan, Peoples R China;

    Henan Polytech Univ, Sch Mech & Power Engn, Dept Energy & Power Engn, 2000 Century Ave, Jiaozuo 454000, Henan, Peoples R China;

    Henan Polytech Univ, Sch Mech & Power Engn, Dept Energy & Power Engn, 2000 Century Ave, Jiaozuo 454000, Henan, Peoples R China;

    Henan Polytech Univ, Sch Mech & Power Engn, Dept Energy & Power Engn, 2000 Century Ave, Jiaozuo 454000, Henan, 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

    Micro-combustion; Catalytic combustion; Gas-phase chemistry; Surface chemistry; Reactor design; Computational fluid dynamics;

    机译:微燃烧;催化燃烧;气相化学;表面化学;反应器设计;计算流体力学;
  • 入库时间 2022-08-18 00:19:24

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