An Equivalent Spherical Particle System to Describe Characteristics of Flow in a Dense Packing of Non-spherical Particles

被引:4
作者
Guo, Peijun [1 ]
Stolle, Dieter [1 ]
Guo, Shannon X. [1 ]
机构
[1] McMaster Univ, Dept Civil Engn, Hamilton, ON L8S 4L7, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
Granular material; Non-spherical particles; Equivalent diameter; Ergun equation; Kozeny-Carman equation; LATTICE-BOLTZMANN SIMULATIONS; THROUGH POROUS-MEDIA; NON-DARCY FLOW; SIZE DISTRIBUTION; DRAG COEFFICIENT; REYNOLDS-NUMBER; FLUID-FLOW; EFFECTIVE POROSITY; FRICTION FACTOR; PERMEABILITY;
D O I
10.1007/s11242-019-01286-y
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Effective characteristics, such as the effective particle diameter and hydraulic radius, are usually used to determine the pressure loss associated with single-phase flow through an isotropic, dense non-spherical granular packing. These quantities can be considered as those of an equivalent spherical particle system. This paper reviews different methods to select effective particle diameters taking into account the effect of particle shape. A new method is proposed to determine an equivalent spherical particle system with both the hydraulic radius and the pressure loss equivalent to those in the actual non-spherical particle packing. This equivalent system can be used to determine the characteristics of flow in the actual system. The analyses provide theoretical justification for adoption of proper effective particle diameters and porosity as well as the dependency of Ergun-Kozeny constant on the shape factor of particles. It is also shown theoretically that the critical Reynolds number for Darcian flow depends on the porosity and the shape factor of particles.
引用
收藏
页码:253 / 280
页数:28
相关论文
共 88 条
[1]   EVALUATION OF SPATIAL-DISTRIBUTION OF HYDRAULIC CONDUCTIVITY USING EFFECTIVE POROSITY DATA [J].
AHUJA, LR ;
CASSEL, DK ;
BRUCE, RR ;
BARNES, BB .
SOIL SCIENCE, 1989, 148 (06) :404-411
[2]   Packed bed pressure drop dependence on particle shape, size distribution, packing arrangement and roughness [J].
Allen, K. G. ;
von Backstroem, T. W. ;
Kroeger, D. G. .
POWDER TECHNOLOGY, 2013, 246 :590-600
[3]  
Andersson A. C., 1984, R42 BYGGF
[4]  
[Anonymous], 1990, INTRO MODELING TRANS, DOI DOI 10.1007/978-94-009-1926-6_7
[5]  
[Anonymous], 1927, Akad. Wiss. Wien, Math-naturw.
[6]   On the drag of freely falling non-spherical particles [J].
Bagheri, Gholamhossein ;
Bonadonna, Costanza .
POWDER TECHNOLOGY, 2016, 301 :526-544
[7]  
Barree RD, 2004, SOC PETR ENG ANN TEC
[8]  
Bear J., 1972, Dynamics of Fluids in Porous Media
[9]   Permeability Description by Characteristic Length, Tortuosity, Constriction and Porosity [J].
Berg, Carl Fredrik .
TRANSPORT IN POROUS MEDIA, 2014, 103 (03) :381-400
[10]  
BEYER W, 1966, Z ANGEW GEOL, V12, P599