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Kinetics study of the copper/hydrochloric acid reaction for thermochemical hydrogen production

机译:铜/盐酸反应热化学制氢的动力学研究

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摘要

The exothermic reaction of hydrochloric acid with paniculate copper occurs during the hydrogen production step in the thermochemical copper-chlorine water splitting cycle. In this paper, this chemical reaction is modeled kinetically, and a parametric study is performed to determine the influences of particle size, temperature and molar ratios on the hydrogen conversion aspects. It is obtained that the residence time of copper particles varies between 10 and 100 s, depending on the operating conditions. The hydrogen conversion at equilibrium varies between 55% and 85%, depending on the reaction temperature. The heat flux at the particle surface, caused by the exothermic enthalpy of reaction, reaches over 3000 W/m2 when the particle shrinks to 0.1% from its initial size. The estimated Biot number varies from 0.001 to 0.1, depending on the operating conditions and the accuracy of thermophysical data of the substances. A numerical algorithm is developed to solve the moving boundary Stefan problem with a chemical reaction that models the shrinking of copper particles in the hypothesis that the chemical reaction and heat transfer are decoupled. The model allows for the estimation of the temperature of a copper particle, assumed spherical, in the radial direction on the hypothesis of large Biot numbers. For small Biot numbers, the transient heat transfer equation results in a lumped capacitance model. In all cases, the particle decomposes in about 10-20s.
机译:在热化学铜-氯水分解循环的制氢步骤中,盐酸与片状铜发生放热反应。在本文中,对该化学反应进行了动力学建模,并进行了参数研究以确定颗粒尺寸,温度和摩尔比对氢转化率的影响。获得的铜粒子的停留时间在10到100 s之间变化,这取决于操作条件。取决于反应温度,平衡时的氢转化率在55%至85%之间变化。当反应物从初始尺寸缩小到0.1%时,由于反应的放热焓而引起的粒子表面热通量达到3000 W / m2以上。估计的毕奥特数在0.001到0.1之间变化,具体取决于操作条件和该物质的热物理数据的准确性。提出了一种数值算法,通过化学反应来解决运动边界Stefan问题,该化学反应对铜颗粒的收缩进行了建模,假设化学反应和传热是分离的。该模型允许在大比奥数假设的情况下,估算径向上呈球形的铜粒子的温度。对于小毕奥数,瞬态传热方程式产生集总电容模型。在所有情况下,颗粒都会在约10-20s内分解。

著录项

  • 来源
    《International journal of hydrogen energy》 |2010年第10期|P.4853-4860|共8页
  • 作者单位

    Faculty of Engineering and Applied Science, University of Ontario Institute of Technology, 2000 Simcoe Street North, Oshawa, ON, Canada L1H 74K;

    rnFaculty of Engineering and Applied Science, University of Ontario Institute of Technology, 2000 Simcoe Street North, Oshawa, ON, Canada L1H 74K;

    rnFaculty of Engineering and Applied Science, University of Ontario Institute of Technology, 2000 Simcoe Street North, Oshawa, ON, Canada L1H 74K;

  • 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

    Cu-Cl thermochemical cycle; Cu-HCl reaction; transport phenomena; fluidized bed reactors; hydrogen;

    机译:Cu-Cl热化学循环;Cu-HCl反应;运输现象;流化床反应器;氢;
  • 入库时间 2022-08-18 00:29:23

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