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Millisecond methane steam reforming for hydrogen production: A computational fluid dynamics study

机译:毫秒级甲烷蒸汽重整用于制氢:计算流体动力学研究

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摘要

The potential of methane steam reforming to produce hydrogen in thermally integrated micro-chemical systems at short contact times was theoretically explored. Methane steam reforming coupled with methane catalytic combustion in microchannel reactors for hydrogen production was studied numerically. A two-dimensional computational fluid dynamics model with detailed chemistry and transport was developed. To provide guidelines for optimal design, reactor behavior was studied, and the effect of design parameters such as catalyst loading, channel height, and flow arrangement was evaluated. To understand how steam reforming can happen at millisecond contact times, the relevant process time scales were analyzed, and a heat and mass transfer analysis was performed. The importance of energy management was also discussed in order to obtain a better understanding of the mechanism responsible for efficient heat exchange between highly exothermic and endothermic reactions. The results demonstrated the feasibility of the design of millisecond reforming systems, but only under certain conditions. To achieve this goal, process intensification through miniaturization and the improvement in catalyst performance is very important, but not sufficient; very careful design and implementation of the system is also necessary to enable high thermal integration. The channel height plays an important role in determining the efficiency of heat exchange. A proper balance of the flow rates of the combustible and reforming streams is an important design criterion. Reactor performance is significantly affected by flow arrangement, and co-current operation is recommended to achieve a good energy balance within the system. The catalyst loading must be carefully designed to avoid insufficient reactant conversion or hot spots. Finally, operating windows were identified, and engineering maps for designing devices with desired power were constructed. (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:理论上探讨了甲烷蒸汽重整在短时间接触热集成微化学系统中产生氢气的潜力。数值研究了甲烷蒸汽重整与甲烷在微通道反应器中的催化燃烧相结合以产生氢气的现象。建立了具有详细化学和运输的二维计算流体动力学模型。为了提供优化设计的指导,研究了反应器的行为,并评估了设计参数(如催化剂的负载,通道高度和流动安排)的影响。为了了解在几毫秒的接触时间内如何进行蒸汽重整,分析了相关的过程时间尺度,并进行了传热和传质分析。还讨论了能量管理的重要性,以便更好地了解负责在高放热和吸热反应之间进行有效热交换的机理。结果证明了仅在某些条件下设计毫秒级重整系统的可行性。为了实现这一目标,通过小型化增强工艺和改善催化剂性能非常重要,但还不够。为了实现高热集成,还必须非常仔细地设计和实施系统。通道高度在确定热交换效率中起重要作用。燃烧和重整流的流量的适当平衡是重要的设计标准。反应堆的性能受流量安排的影响很大,建议并流运行以在系统内实现良好的能量平衡。必须精心设计催化剂的装载量,以避免反应物转化不足或出现热点。最后,确定了操作窗口,并构造了用于设计具有所需功率的设备的工程图。 (C)2018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》 |2018年第29期|12948-12969|共22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

    Microchannel reactors; Steam reforming; Hydrogen production; Process intensification; Micro-combustion; Computational fluid dynamics;

    机译:微通道反应器;蒸汽重整;制氢;工艺强化;微燃烧;计算流体力学;
  • 入库时间 2022-08-18 00:18:29

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