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首页> 外文期刊>International journal of hydrogen energy >Optimal design of a sleeve-type steam methane reforming reactor for hydrogen production from natural gas
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Optimal design of a sleeve-type steam methane reforming reactor for hydrogen production from natural gas

机译:用于天然气制氢的套筒式蒸汽甲烷重整反应器的优化设计

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The three-dimensional computational fluid dynamics (CFD) model was used in a sleeve type steam methane reforming (SMR) reactor for H-2 production of 2.5 Nm(3)/h from natural gas. The feed and combustion gases acted as a counter-current heat exchange owing to a narrow sleeve equipped between the combustor and catalyst-bed. The CFD results were validated against the experimental data of the SMR reactor with a sleeve gap size of 3 mm. The effect of the sleeve gap size and the flame shape on process performances such as H-2 production rate, thermal efficiency, and uniformity of catalyst-bed temperature was investigated using the CFD model. The sleeve gap size influenced the gas velocity inside the sleeve gap and the convective heat transfer. The SMR reactor with a sleeve gap size of 7 mm showed the highest H-2 production rate and thermal efficiency when comparing six sleeve gap sizes ranging from 2 to 10 mm. A new flame shape for the SMR reactor with the sleeve gap size of 7 mm was proposed to improve the process performances. (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:三维计算流体动力学(CFD)模型用于套筒型蒸汽甲烷重整(SMR)反应器中,以H-2从天然气中产生2.5 Nm(3)/ h。由于在燃烧室和催化剂床之间装有狭窄的套筒,进料和燃烧气体起到了逆流热交换的作用。 CFD结果已针对套筒间隙尺寸为3 mm的SMR反应器的实验数据进行了验证。使用CFD模型研究了套筒间隙尺寸和火焰形状对工艺性能(如H-2生产率,热效率和催化剂床温均匀性)的影响。套筒间隙的大小影响了套筒间隙内的气体速度和对流传热。套筒间隙尺寸为7毫米的SMR反应器在比较2至10毫米范围内的六个套筒间隙尺寸时显示出最高的H-2生产率和热效率。提出了一种用于套筒间隙尺寸为7 mm的SMR反应器的新火焰形状,以改善工艺性能。 (C)2018氢能出版物有限公司。由Elsevier Ltd.出版。保留所有权利。

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