Revisited analysis of pressure drop in flow through crushed rocks

被引:35
作者
Legrand, J [1 ]
机构
[1] Univ Nantes, GEPEA, Chem & Environm & Food Engn Lab, CNRS,UMR 6144,CRTT, F-44602 St Nazaire, France
来源
JOURNAL OF HYDRAULIC ENGINEERING-ASCE | 2002年 / 128卷 / 11期
关键词
Darcy's law; friction factor; hydraulic gradients; models; porous media; rocks;
D O I
10.1061/(ASCE)0733-9429(2002)128:11(1027)
中图分类号
TU [建筑科学];
学科分类号
0813 ;
摘要
Experimental data of pressure drop in flow through crushed rocks are reanalyzed with the capillary model in comparison with a model based on the square root of permeability as characteristic length. The capillary model is described by two parameters: the pore diameter and the tortuosity. The comparison leads to relationships between the structural parameters, Reynolds number, and friction factor of each model. The interest of the capillary model is that a single equation can predict all the experimental data expressed in terms of a pore friction factor as a function of pore Reynolds number. The equation, which is the sum of a viscous term and an inertial one, is valid for the whole Reynolds number domain. The equation can be used for the determination of the limits of the Darcy and turbulent flow regimes. According to the criterion used to neglect the viscous or the inertial term,. the flow regimes limits can be expressed by a simple numerical value.
引用
收藏
页码:1027 / 1031
页数:5
相关论文
共 17 条
[1]  
Ahmed N., 1969, Journal of the Hydraulic Division: Proceedings of the American Society of Civil Engineers, V95, P1847, DOI [10.1061/JYCEAJ.0002193, DOI 10.1061/JYCEAJ.0002193]
[2]  
Bird R.B., 2006, TRANSPORT PHENOMENA, Vsecond, DOI 10.1002/aic.690070245
[3]   A NEW MODEL FOR DETERMINING MEAN STRUCTURE PARAMETERS OF FIXED-BEDS FROM PRESSURE-DROP MEASUREMENTS - APPLICATION TO BEDS PACKED WITH PARALLELEPIPEDAL PARTICLES [J].
COMITI, J ;
RENAUD, M .
CHEMICAL ENGINEERING SCIENCE, 1989, 44 (07) :1539-1545
[4]   PRESSURE-DROP PREDICTION FOR FLOW-THROUGH HIGH-POROSITY METALLIC FOAMS [J].
DUPLESSIS, P ;
MONTILLET, A ;
COMITI, J ;
LEGRAND, J .
CHEMICAL ENGINEERING SCIENCE, 1994, 49 (21) :3545-3553
[5]  
ERGUN S, 1952, CHEM ENG PROG, V48, P89
[6]  
JAYACHANDRA K, 1995, THESIS SRI VENKATESW
[7]   Darcy's experiments and the deviation to nonlinear flow regime [J].
Lage, JL ;
Antohe, BV .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 2000, 122 (03) :619-625
[8]  
MCCORQUODALE JA, 1978, J HYDRAUL RES, V14, P123
[9]   Friction factor in static mixer and determination of geometric parameters of SMX Sulzer mixers [J].
Morancais, P ;
Hirech, K ;
Carnelle, G ;
Legrand, J .
CHEMICAL ENGINEERING COMMUNICATIONS, 1999, 171 :77-93
[10]  
Nasser M.S., 1970, THESIS U WINDSOR WIN