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Effect of the geometric dimensionality of computational domain on the results of CFD- modeling of steam methane reforming

机译:计算域的几何尺寸对蒸汽甲烷重整的CFD-建模结果的影响

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A numerical investigation of the steam methane reforming process using RANS is presented. The effect of the geometric dimensionality of the reformer on the numerical results is investigated by performing CFD simulations with 1D, 2D and 3D computational domains. The commercial software ANSYS Fluent is used for this comparative analysis. The numerical study is performed for the wide range of the residence time and the relative length (radius/length). The comparison study of 1D, 2D and 3D models on steam methane reforming is performed for same CFD-code, initial conditions, catalyst type, approximation scheme, the convergence criteria, the turbulence model, the type of solution initialization. The results show the distributions of the mole fraction of the reformate products, temperature, methane conversion rate and diffusion flux inside a 150 mm length and 10 mm radius of steam methane reformer that is filled by nickel based catalyst. The differences between the results for 1D and 3D geometry become insignificant at the residence time of about 8 kg(cat)s/mol(CH4) and the relative length of 15. The difference between the results for 2D and 3D geometry is not significant as for 1D and 3D geometries. Almost similar results are achieved with residence time 4 kg(cat)s/mol(cH4) and relative length 15. Therefore, for engineering calculations of steam methane reforming, it is sufficient to use a 1D model if the residence time is more than 8 kg(cat)s/mol(CH4) and the relative length is more than 15. The 3D and 2D model should be used if the residence time and the relative length have a small value. (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
机译:提出了使用RANS进行蒸汽甲烷重整过程的数值研究。通过使用1D,2D和3D计算域进行CFD仿真,研究了重整器的几何尺寸对数值结果的影响。商业软件ANSYS Fluent用于此比较分析。对滞留时间和相对长度(半径/长度)的宽范围进行了数值研究。对于相同的CFD代码,初始条件,催化剂类型,近似方案,收敛准则,湍流模型,溶液初始化类型,对蒸汽甲烷重整的1D,2D和3D模型进行了比较研究。结果显示了重整产物的摩尔分数,温度,甲烷转化率和扩散通量在150 mm长,半径为10 mm的填充有镍基催化剂的蒸汽甲烷重整器内的分布。在大约8 kg(cat)s / mol(CH4)的停留时间和15的相对长度下,一维和3D几何的结果之间的差异不明显。2D和3D几何的结果之间的差异不显着,因为适用于1D和3D几何。停留时间为4 kg(cat)s / mol(cH4)和相对长度为15时,几乎可以获得相似的结果。因此,如果停留时间大于8,对于蒸汽甲烷重整的工程计算,只要使用一维模型就足够了。 kg(cat)s / mol(CH4),并且相对长度大于15。如果停留时间和相对长度较小,则应使用3D和2D模型。 (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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