首页> 外文期刊>ACS Omega >Compact Steam-Methane Reforming for the Production of Hydrogen in Continuous Flow Microreactor Systems
【24h】

Compact Steam-Methane Reforming for the Production of Hydrogen in Continuous Flow Microreactor Systems

机译:紧凑型蒸汽-甲烷重整装置,用于连续流微反应器系统中的氢气生产

获取原文

摘要

The implementation of fuel cell deployment requires efficient conversion of fuels into hydrogen in a distributed energy system. Fortunately, continuous flow and microreactor technology provide unique opportunities for the portable production of hydrogen. This study focuses on determining the operation space for a thermally integrated methane reforming system, thereby providing a theoretical basis for the design and optimization of such systems. The steam-methane reforming over rhodium coupled with methane combustion over platinum in a thermally integrated microchannel reactor arranged with rectangular-shaped protuberances was studied numerically in order to improve its operability and stability. Computational fluid dynamic simulations were carried out with detailed reaction mechanisms to identify conditions for the maximum hydrogen yield and the highest output power. Various operating lines were presented, and various performance metrics were evaluated accordingly. The results indicated that the efficient production of hydrogen is made possible through improving transport performance for highly active catalysts. The flow disturbance elements designed for the reactor are of great benefit to intensification of the reforming process. There exists a trade-off between fuel utilization and output power. Autothermal operation advantages from improved transport performance in small physical dimensions were demonstrated for the system, but careful thermal management is always necessary to ensure its efficient and stable operation. The thermal conductivity of the wall separating the exothermic and endothermic reactions plays a significant role in determining the performance of the system. Highly active catalysts are required to intensify the overall reforming process and to achieve efficient thermal management. Adjustment of fluid velocities can serve as a convenient means to achieve efficient operation of the system.
机译:燃料电池部署的实施要求在分布式能源系统中将燃料有效地转化为氢。幸运的是,连续流和微反应器技术为便携式生产氢气提供了独特的机会。这项研究的重点是确定热集成甲烷重整系统的操作空间,从而为此类系统的设计和优化提供理论依据。为了提高其可操作性和稳定性,在数值上研究了铑的蒸汽-甲烷重整以及铂在具有矩形突起的热集成微通道反应器中的甲烷燃烧。用详细的反应机理进行了计算流体动力学模拟,以确定最大氢产量和最高输出功率的条件。介绍了各种操作线,并相应地评估了各种性能指标。结果表明,通过提高高活性催化剂的传输性能,可以有效地生产氢气。设计用于反应器的流动干扰元件对强化重整过程非常有益。在燃料利用率和输出功率之间需要权衡。该系统在较小的物理尺寸上改善了运输性能,因此具有自热运行的优势,但始终需要仔细进行热管理以确保其高效稳定地运行。分隔放热和吸热反应的壁的热导率在确定系统性能方面起着重要作用。需要高活性催化剂来增强整个重整过程并实现有效的热管理。流体速度的调节可以用作实现系统有效运行的便利手段。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号