This paper presents the results of heat transfer measurement and analy
sis for two 5 x 5 x 1 cm porous channels. The channels were made of si
ntered bronze beads with two different mean diameters, d(p) = 0.72 and
1.59 mm. The local wall temperature distribution, inlet and outlet pr
essures and temperatures, and heat transfer coefficients were measured
for heat flux of 0. 8, 1.6, 2.4, and 3.2 W/cm2 with air velocity rang
ing from 0. 16 to 5 m/s and inlet air pressure of 1 approximately 3 at
m. The measurement covers the data in both thermal entrance and therma
lly fully developed regions. The local Nusselt numbers were correlated
in the fully developed region. The fully developed Nusselt numbers we
re analyzed theoretically by using a non-Darcy, two-equation flow mode
l. Heat transfer between the solid and fluid phases was modeled by a r
elation of the form h(loc) = ARe(n). A wall function was introduced to
model the transverse thermal dispersion process for the wall effect o
n the lateral mixing of fluid. The predicted fully developed Nusselt n
umbers are in good agreement with the measured values.