1. Introduction
Cylindrical packed beds consisting of spherical particles are encountered in industrial applications such as in pebble bed reactors in the nuclear industry, in operations in chemical processes requiring interphase contact (for example, separation and heterogeneous catalysis), and practical applications such as packed columns for chromatography and regenerative heat exchangers [
1,
2,
3]. A proper understanding of the characteristics of the porous structure of cylindrical packed beds is imperative in the analysis and design of the processes involving fluid flow, and heat and mass transfer [
1]. It has been found that the container wall has a significant effect on the packing structure in the near-wall region, which affects the flow distribution and heat and mass transfer [
2,
4]. The most important characteristic is the porosity or void fraction and the radial variation in porosity is of specific interest [
5]. The radial variation in porosity has been determined directly from experimental measurements using various approaches [
2,
5,
6,
7]. When the positions and sizes of the spheres are known, the radial variation in porosity can be determined using numerical techniques. The positions and diameters of the spheres have been determined experimentally [
1,
8,
9] as well as numerically using packing algorithms [
10,
11] and the discrete element method [
12,
13]. The radial variation in porosity can be determined numerically using volume-based [
8,
14,
15], area-based [
16,
17,
18,
19], or line-based [
20,
21,
22] approaches. In this study, the focus is on the area-based methods of Mariani et al. [
16], Mueller [
18], and Du Toit [
17,
19], which employ the intersection between the spheres and selected cylindrical planes to determine the radial variation in porosity. The focus is specifically on the calculation of the area of the curved elliptic intersection between a sphere and a cylindrical plane.
Using geometrical considerations, Mariani et al. [
16] derived an analytical integral expression in terms of the axial direction based on the analytical expression describing the lengths of the in-plane arcs as a function of axial position, defining the intersection. The integral cannot be evaluated analytically and was transformed to expressions involving Legendre complete elliptic integrals of the first and second kind. Mariani et al. [
16] evaluated the elliptic integrals using an efficient numerical procedure to calculate the area. Du Toit [
19], following a similar approach, calculated the area by integrating the derived analytical integral expression numerically.
Using the same geometrical considerations, Du Toit [
17,
19] derived an integral expression in terms of the circumferential or angular direction based on the analytical expression describing the in-plane vertical or axial lines, as function of angular position, defining the intersection. Since the integral cannot be evaluated analytically, Du Toit [
17,
19] integrated the analytical integral expression numerically to determine the area.
Mueller [
18] derived an integral expression in terms of the radial direction based on the analytical expression for the axial height of the area, as a function of the radial position, obtained from the equations describing the surfaces of the sphere and the cylindrical plane. This integral can also not be evaluated analytically, and Mueller [
18] therefore evaluated it numerically to determine the intersection area.
Mariani et al. [
16], Du Toit [
17,
19], and Mueller [
18] only provided indirect validation of the calculation of the intersection area by comparing the radial porosity profiles they obtained with available corresponding experimental results or by calculating the number of spheres in the bed. This study, in the first place, provides direct validation of the calculation of the intersection area through the refined numerical integration employing Simpson’s rule [
23] of the primary integral expressions of Mariani et al. [
16], Du Toit [
17,
19], and Mueller [
18] and the evaluation of the area employing computer-aided design software. Secondly, the characteristics and the performance of the respective approaches are compared in terms of the number of uniformly spaced integration points that are required to obtain an accurate result. Four test cases representing typical sphere—cylindrical plane configurations that can be encountered are used to perform the analysis.
4. Conclusions
Cylindrical packed beds consisting of spherical particles are found in various industrial and practical applications [
1,
2,
3]. The container wall has a significant influence on the packing structure in the near-wall region affecting the flow distribution and heat and mass transfer [
2,
4]. This requires an understanding of the characteristics of the radial variation in in the porosity [
1,
5]. When the positions and the diameters of the spheres forming the packed bed are known, numerical techniques [
14,
15,
16,
17,
18,
19,
20,
21,
22] can be used to obtain the radial variation in porosity. Employing area-based methodologies, Mariani et al. [
16], Mueller [
18], and Du Toit [
17,
19] determine the radial variation in porosity by considering the areas of the intersections between the spheres in the packed bed and selected cylindrical planes. The accurate calculation of the area of the curved elliptical intersection between a sphere and a cylindrical plane is of critical importance for the success of these methodologies.
This study endeavoured to provide a direct validation of the calculation of the intersection through the refined numerical integral using Simpson’s Rule [
23] of the primary integral expressions of Equation (4) [
17,
19], Equation (8) [
19], Equation (15) [
16], and Equation (23) [
18]. Four representative sphere–cylindrical plane configurations were chosen to evaluate the ability of the methodologies to calculate the intersection area. The first step in the analyses was to find the maximum size of the integration interval for each case that gave a converged value for the intersection area. The second step in the analyses was to compare the intersection areas that were obtained for the different cases with the corresponding areas obtained using the finite element code COMSOL Multiphysics [
27] and the computer aided design (CAD) codes SOLIDWORKS [
28] and NX [
29]. It was found that the corresponding intersection areas obtained by the methodologies of Mariani et al. [
16], Du Toit [
17,
19], and Mueller [
18] are in excellent agreement and also in very good agreement with the corresponding areas obtained using the Measuring Geometry Tool in COMSOL Multiphysics, and the CAD packages SOLIDWORKS and NX.
The study also considered the performance of the methodologies of Mariani et al. [
16], Du Toit [
17,
19], and Mueller [
18] by comparing the number of integration points required in each case to obtain an accurate solution for the intersection area. The number of integration points is considered to be a representative reflection of the computational effort and of interest for the practical implementation of the methodologies. It was found that the numerical integration of Equation (15) requires the least number of integration points followed by Equation (4), then Equation (8), and lastly Equation (23). It was further observed that the number of integration points required in the case of Equation (15) is independent of the sphere–cylindrical plane configuration.
It can thus be stated that in this study the calculation of the area of the intersection surface between a cylindrical plane and a sphere using the approaches of Mariani et al. [
16], Du Toit [
17,
19], and Mueller [
18] have been validated. It can also be concluded that the procedure of Mariani et al. [
16], compared to the methodologies of Du Toit [
17,
19] and Mueller [
18], requires the least computational effort to obtain an accurate solution for the intersection area based on Simpson’s rule [
23], which was employed to perform the numerical integration of the relevant integral expressions.
As a natural extension of the study, it is recommended that the computational effort of more advanced numerical integration methods [
23,
31,
32] be evaluated in view of the fact that it has been shown that the methodologies of Mariani et al. [
16], Du Toit [
17,
19], and Mueller [
19] give the correct results for the area of the intersection between a sphere and a cylindrical plane. However, it is recommended that this be done in the context of the calculation of the radial variation in porosity for a selection of cylindrical packed beds consisting of varying numbers of spheres. The study should include the pebble bed model consisting of 450,000 spheres generated by Suikkanen et al. [
13].