Convective heat transfer and friction drag in a duct inserted with aluminum foams have been studied experimentally. The combined effects of foam porosity (ε=0.7, 0.8, and 0.95) and flow Reynolds number (1900⩽Re⩽7800) are examined. Frictional drags for flow across the aluminum foam are measured by pressure taps, while interstitial heat transfer coefficients in the aluminum foam are determined using a transient single-blow technique with a thermal non-equilibrium two-equation model. Solid material temperature distribution is further measured for double check of the heat transfer results. To understand the frictional drag mechanisms, smoke-wire flow visualization is conducted in the aluminum-foam ducts. Results show that both the friction factor and the volumetric heat transfer coefficient increase with decreasing the foam porosity at a fixed Reynolds number. In addition, the aluminum foam of ε=0.8 has the best thermal performance under the same pumping power constraint among the three aluminum foams investigated. Finally, empirical correlations for pore Nusselt number are developed in terms of pore Reynolds number under various foam porosities.

1.
Koh
,
J. C. Y.
, and
Stevens
,
R. L.
,
1975
, “
Enhancement of Cooling Effectiveness by Porous Medium in Coolant Passages
,”
ASME J. Heat Transfer
,
96
, pp.
309
311
.
2.
Cheng
,
P.
,
1982
, “
Mixed Convection About a Horizontal Cylinder and a Sphere in Fluid Saturated Porous Medium
,”
Int. J. Heat Mass Transf.
,
28
, pp.
1245
1247
.
3.
Jones
,
D. P.
, and
Krier
,
H.
,
1983
, “
Gas Flow Resistance Measurements Through Packed Beds at High Reynolds Number
,”
ASME J. Fluids Eng.
,
105
, pp.
168
173
.
4.
Cheng
,
P.
, and
Zhu
,
H.
,
1987
, “
Effects of Radial Thermal Dispersion on Fully Developed Forced Convection in Cylindrical Packed Bed
,”
Int. J. Heat Mass Transf.
,
30
, pp.
2373
2383
.
5.
Renken
,
K. J.
, and
Poulikakos
,
D.
,
1988
, “
Experimental and Analysis of Forced Convection Heat Transport in Packed Bed of Spheres
,”
Int. J. Heat Mass Transf.
,
31
, pp.
1399
1408
.
6.
Vafai
,
K.
, and
Sozen
,
M.
,
1990
, “
Analysis of Energy and Momentum Transport for Fluid Flow through a Porous Bed
,”
ASME J. Heat Transfer
,
112
, pp.
690
699
.
7.
Amiri
,
A.
, and
Vafai
,
K.
,
1994
, “
Analysis of Dispersion Effect and Nonthermal Equilibrium, Non-Darcy Variable Porosity Incompressible Flow Through Porous Media
,”
Int. J. Heat Mass Transf.
,
37
, pp.
939
954
.
8.
Hwang
,
G. J.
, and
Chao
,
C. H.
,
1994
, “
Heat Transfer Measurement and Analysis for Sintered Porous Channel
,”
ASME J. Heat Transfer
,
116
, pp.
456
464
.
9.
Varahasamy
,
M.
, and
Fand
,
R. M.
,
1996
, “
Heat Transfer by Forced Convection in Pipes Packed with Porous Media Whose Matrices Are Composed of Spheres
,”
Int. J. Heat Mass Transf.
,
39
, pp.
3931
3947
.
10.
Peterson
,
G. P.
, and
Chang
,
S. W.
,
1998
, “
Two-Phase Heat Dissipation Utilizing Porous-Channels of High Conductivity Material
,”
ASME J. Heat Transfer
,
120
, pp.
243
252
.
11.
Hunt
,
M. L.
, and
Tien
,
C. L.
,
1988
, “
Effects of Thermal Dispersion on Forced Convection in Fibrous Media
,”
Int. J. Heat Mass Transf.
,
31
, pp.
301
309
.
12.
Younis
,
L. B.
, and
Viskanta
,
R.
,
1993
, “
Experimental Determination of the Volumetric Heat Transfer Coefficient Between Stream of Air and Ceramic Foam
,”
Int. J. Heat Mass Transf.
,
36
, pp.
1425
1434
.
13.
Ichimiya
,
K.
,
1999
, “
A New Method for Evaluation of Heat Transfer Between Solid Material and Fluid in a Porous Medium
,”
ASME J. Heat Transfer
,
121
, pp.
978
983
.
14.
Calmidi
,
V. V.
, and
Mahajan
,
R. L.
,
2000
, “
Forced Convection in High Porosity Metal Foams
,”
ASME J. Heat Transfer
,
122
, pp.
557
565
.
15.
Genetti, A. J., 1999, “Engineering and Design—Groundwater Hydrology,” USACE, Washington DC.
16.
Hadim
,
A.
,
1994
, “
Forced Convection in a Porous Channel with Localized Heat Sources
,”
ASME J. Heat Transfer
,
116
, pp.
465
472
.
17.
Golombok
,
M.
,
Jariwala
,
H.
, and
Shirvill
,
L. C.
,
1990
, “
Gas-Solid Heat Exchange in a Fibrous Metallic Material Measured by a Heat Regenerator Technique
,”
Int. J. Heat Mass Transf.
,
33
, pp.
243
252
.
18.
Gamson
,
B. W.
,
Thodos
,
G.
, and
Hougen
,
O. A.
,
1943
, “
Heat, Mass and Momentum Transfer in the Flow of Gases Through Granular Solids
,”
AIChE J.
,
39
, pp.
1
35
.
19.
Antohe
,
B. V.
,
Lage
,
J. L.
,
Price
,
D. C.
, and
Weber
,
R. M.
,
1997
, “
Experimental Determination of Permeability and Inertia Coefficients of Mechanically Compressed Aluminum Porous Matrices
,”
ASME J. Fluids Eng.
,
119
, pp.
404
412
.
20.
Lage
,
J. L.
,
Antohe
,
B. V.
, and
Nield
,
D. A.
,
1997
, “
Two Type of Nonlinear Pressure-Drop Versus Flow Rate Relation Observed For Saturated Porous Media
,”
ASME J. Fluids Eng.
,
119
, pp.
700
706
.
21.
Patankar, S. V., 1980, Numerical Heat Transfer and Fluid Flow, Hemisphere, New York.
22.
Kline
,
S. J.
, and
McClintock
,
F. A.
,
1953
, “
Describing the Uncertainties in Single-Sample Experiments
,”
Mech. Eng. (Am. Soc. Mech. Eng.)
,
pp.
3
8
.
23.
Hwang
,
J. J.
,
1998
, “
Heat Transfer-Friction Characteristic Comparison in Rectangular Ducts With Slit and Solid Ribs Mounted on One Wall
,”
ASME J. Heat Transfer
,
120
, pp.
709
716
.
24.
Hwang
,
J. J.
,
1997
, “
Turbulent Heat Transfer and Fluid Flow in a Porous-Baffled Channel
,”
J. Thermophys. Heat Transfer
,
11
, pp.
429
436
.
25.
Hwang
,
J. J.
, and
Chao
,
C. H.
,
2000
, “
Passive Control of Convective Transport Phenomena Utilizing an Attached-Detached Rib-Array
,”
J. Thermophys. Heat Transfer
,
14
, pp.
579
583
.
26.
Wakao, N., and Kaguei, S., 1993, Heat and Mass Transfer in Packed Beds, Gordon and Breach Science.
You do not currently have access to this content.