The effect of porous media particle size on forced convection from a circular cylinder without assuming local thermal equilibrium between phases

被引:41
作者
Al-Sumaily, Gazy F. [1 ]
Nakayama, Akira [2 ]
Sheridan, John [1 ]
Thompson, Mark C. [1 ]
机构
[1] Monash Univ, Dept Mech & Aerosp Engn, Fluids Lab Aeronaut & Ind Res FLAIR, Clayton, Vic 3800, Australia
[2] Shizuoka Univ, Dept Mech Engn, Hamamatsu, Shizuoka 4328561, Japan
关键词
Forced convection; Porous media; Non-Darcian effects; Local thermal non-equilibrium; Particle diameter; NONEQUILIBRIUM NATURAL-CONVECTION; HEAT-TRANSFER; MIXED CONVECTION; HORIZONTAL CYLINDER; NON-DARCIAN; FLUID-FLOW; INCOMPRESSIBLE-FLOW; BOUNDARY-CONDITIONS; LAYER; TEMPERATURE;
D O I
10.1016/j.ijheatmasstransfer.2012.03.007
中图分类号
O414.1 [热力学];
学科分类号
摘要
A detail numerical analysis of the effect of particle diameter of a packed bed of spherical particles on forced convection about an embedded circular cylinder is presented. This parametric study focusses on the two-phase energy (LTNE local thermal non-equilibrium) model, which does not assume local thermal equilibrium (LTE) between the solid medium and the fluid. The investigation is performed for a cylinder-to-particle diameter ratio D-cy/d(p) = 10-100, at a wide ranges of Reynolds number Re-D = 1-250 and solid-to-fluid thermal conductivity ratio k(r) = 0.01-1000. A comparison of predictions from the LTNE and LTE energy models is also made. This paper quantifies the influence of the key non-dimensional parameters on the heat transfer rate. It is also shown that although the presence of the porous materials around the heated cylinder enhances the overall heat transfer and increases the pressure drop in the bed compared to an empty channel, using a porous medium with large particle diameters increases considerably this enhancement in heat transfer and decreases significantly the unfavorable pressure drop. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3366 / 3378
页数:13
相关论文
共 56 条
[1]   HEAT AND FLOW CHARACTERISTICS OF PACKED-BEDS [J].
ACHENBACH, E .
EXPERIMENTAL THERMAL AND FLUID SCIENCE, 1995, 10 (01) :17-27
[2]   Constant wall heat flux boundary conditions in porous media under local thermal non-equilibrium conditions [J].
Alazmi, B ;
Vafai, K .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2002, 45 (15) :3071-3087
[3]   EFFECTS OF BOUNDARY-CONDITIONS ON NON-DARCIAN HEAT-TRANSFER THROUGH POROUS-MEDIA AND EXPERIMENTAL COMPARISONS [J].
AMIRI, A ;
VAFAI, K ;
KUZAY, TM .
NUMERICAL HEAT TRANSFER PART A-APPLICATIONS, 1995, 27 (06) :651-664
[4]   Transient analysis of incompressible flow through a packed bed [J].
Amiri, A ;
Vafai, K .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1998, 41 (24) :4259-4279
[5]   ANALYSIS OF DISPERSION EFFECTS AND NONTHERMAL EQUILIBRIUM, NON-DARCIAN, VARIABLE POROSITY INCOMPRESSIBLE-FLOW THROUGH POROUS-MEDIA [J].
AMIRI, A ;
VAFAI, K .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1994, 37 (06) :939-954
[6]  
[Anonymous], 1995, PRINCIPLES HEAT TRAN
[7]  
[Anonymous], PARALLEL VECTOR COMP
[8]   Onset of Darcy-Benard convection using a thermal non-equilibrium model [J].
Banu, N ;
Rees, DAS .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2002, 45 (11) :2221-2228
[9]   Thermal non-equilibrium natural convection in a square enclosure filled with a heat-generating solid phase, non-Darcy porous medium [J].
Baytas, AC .
INTERNATIONAL JOURNAL OF ENERGY RESEARCH, 2003, 27 (10) :975-988
[10]   Free convection in a square porous cavity using a thermal nonequilibrium model [J].
Baytas, AC ;
Pop, L .
INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2002, 41 (09) :861-870