Analytical and numerical study of mean porosity variations in annular packed beds of spherical pellets

IF 5.1 2区 工程技术 Q2 ENGINEERING, CHEMICAL
Pablo Díaz-Ulloa, Rodrigo Unzueta, Iván Cornejo
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Abstract

Annular packed beds are used in pebble-bed nuclear reactors, annular membrane reactors for hydrogen production and annular chromatography columns, yet, unlike the cylindrical geometry, no validated model predicts their mean porosity across a wide range of confinement ratios, and the only available correlation was calibrated from a single experimental point. This study uses rigid-body simulation (RBS) to generate annular packed beds of spherical pellets at 52 confinement ratios between 2.25 and 15, with three independent realizations each and a fixed inner radius-to-particle diameter ratio of 2. The generation procedure is validated against annular experimental data comprising an unadjusted radial porosity profile and an independent mean porosity measurement. The mean porosity oscillates non-monotonically with a decaying amplitude, and the first extremum interval is markedly shorter than the subsequent ones. A layer-stacking analytical framework, previously developed for cylindrical beds, is extended to the annular geometry through circular monolayer, zig-zag monolayer and two-coupled-rows regimes, with the first transition located analytically at a confinement ratio of approximately 2.74. The model reproduces the simulated mean porosity within its domain and explains its largest deviation through a nesting threshold at 2+3≈3.73, the annular counterpart of the cylindrical threshold. Beyond this domain, an empirical correlation combining a damped oscillation with a quadratic decay envelope describes the full range with a coefficient of determination of 0.970, against 0.690 for the existing annular correlation. These models provide the mean porosity required by pressure drop and transport models for annular reactors and columns.
球形球团环形充填床平均孔隙度变化的分析与数值研究
环形填充床用于球床核反应堆、用于制氢的环形膜反应器和环形色谱柱,然而,与圆柱形结构不同,没有经过验证的模型可以预测其在大范围约束比下的平均孔隙度,并且唯一可用的相关性是从单个实验点校准的。本研究使用刚体模拟(RBS)生成球形球团的环形填充床,约束比为2.25 ~ 15之间的52个,每个有三个独立的实现,固定的内半径与颗粒直径比为2。生成过程通过环空实验数据进行验证,实验数据包括未经调整的径向孔隙度剖面和独立的平均孔隙度测量值。平均孔隙度呈非单调衰减振荡,且第一个极值区间明显短于其后几个极值区间。先前为圆柱形层开发的层-层分析框架,通过圆形单层、之字形单层和双耦合行结构扩展到环形几何结构,第一次过渡的解析位置约为2.74。该模型在其域内再现了模拟的平均孔隙度,并通过2+3≈3.73的嵌套阈值(圆柱形阈值的环形对应)解释了其最大偏差。在此域之外,结合阻尼振荡和二次衰减包络的经验相关描述了整个范围,其决定系数为0.970,而现有的环形相关为0.690。这些模型提供了压力降和输送模型对环形反应器和塔的平均孔隙度要求。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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来源期刊
Chemical Engineering Science
Chemical Engineering Science 工程技术-工程:化工
CiteScore
7.50
自引率
8.50%
发文量
1025
审稿时长
50 days
期刊介绍: Chemical engineering enables the transformation of natural resources and energy into useful products for society. It draws on and applies natural sciences, mathematics and economics, and has developed fundamental engineering science that underpins the discipline. Chemical Engineering Science (CES) has been publishing papers on the fundamentals of chemical engineering since 1951. CES is the platform where the most significant advances in the discipline have ever since been published. Chemical Engineering Science has accompanied and sustained chemical engineering through its development into the vibrant and broad scientific discipline it is today.
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