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Numerical investigation on the transient characteristics of hydrogen production from catalytic autothermal reforming of methane in a micro combustor with multiple cylinders

机译:多缸微型燃烧室中甲烷催化自热重整制氢瞬态特性的数值研究

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The transient characteristics of autothermal reforming of methane in a cube micro combustor with multiple cylinders are numerically investigated. The effects of mixture gas composition, catalytic wall temperature and inlet velocity of the mixture feed gas on autothermal reforming of methane are thoroughly discussed. The results demonstrate that the yield of hydrogen decreases and the time to steady state slightly decreases with the increasing of steam content at a constant O2/CH4 molar ratio, while the yield of hydrogen decreases and the time to steady state slightly increases with the increasing of oxygen content at a constant H2O/CH4 molar ratio. Methane conversion significantly increases with the increasing of catalytic wall temperature, meanwhile, the reaction time to steady state sharply decreases, which are 61 ms and 29 ms at 790 K and 1190 K, respectively. The flow velocity has a determined influence on autothermal reforming of methane. As the velocity decreases from 0.5 m/s to 0.05 m/s, methane conversion increases from 62.60% to 98.88% and the yield of hydrogen increases from 56.21% to 90.48%. Higher inlet velocity leads to short residence time, which may not be sufficient to complete the reaction.
机译:数值研究了多缸立方微型燃烧室中甲烷自热重整的瞬态特性。彻底讨论了混合气体组成,催化壁温度和混合进料气体入口速度对甲烷自热重整的影响。结果表明,在恒定的O2 / CH4摩尔比下,随着蒸汽含量的增加,氢的收率降低,稳态的时间略有减少,而随着H2的增加,氢的产率降低,稳态的时间略有增加。 H2O / CH4摩尔比恒定时的氧含量甲烷转化率随着催化壁温度的升高而显着增加,同时,达到稳态的反应时间急剧缩短,分别在790 K和1190 K时分别为61 ms和29 ms。流速对甲烷的自热重整具有确定的影响。随着速度从0.5 m / s降低到0.05 m / s,甲烷转化率从62.60%增加到98.88%,氢气产率从56.21%增加到90.48%。较高的入口速度导致较短的停留时间,这可能不足以完成反应。

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