Metal Foams: A Design Guide
Metal Foams: A Design Guide
Metal Foams: A Design Guide
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Thermal management and heat transfer 183<br />
the cellular metal as a geometric variant on a staggered bank of cylinders<br />
(BOC) oriented normal to the fluid flow. The modified BOC solution has<br />
proportionality coefficients that reflect the geometric differences between the<br />
foam and the cylinder. This approach has been validated experimentally and<br />
the unknown coefficients calibrated. Only the results are given here.<br />
The heat transfer coefficient, Hc, for the cellular metal is (Lu et al., 1998):<br />
Hc D 2Q<br />
d keff<br />
� �<br />
� 2b�<br />
Bieff tanh Bieff<br />
⊲13.2⊳<br />
d<br />
Here Q / s, keff is an effective thermal conductivity related to the actual<br />
thermal conductivity of the constituent metal, ks, by:<br />
keff D 0.28 ks<br />
⊲13.3⊳<br />
and b is the thickness of the medium (Figure 13.1). The coefficient of 0.28<br />
has been determined by experimental calibration, using infrared imaging of<br />
the cellular medium (Bastawros and Evans, 1997; Bastawros et al., in press).<br />
The heat transfer that occurs from the metal ligaments into the fluid can be<br />
expressed through a non-dimensional quantity referred to as the Biot number:<br />
Bi D h<br />
⊲13.4⊳<br />
dks<br />
where h is the local heat transfer coefficient. The Biot number is governed by<br />
the dynamics of fluid flow in the cellular medium. The established solutions<br />
for a staggered bank of cylinders (e.g. Holman, 1989) are:<br />
Bi D 0.91Pr 0.36 Re 0.4 ⊲ka/ks⊳ ⊲Re � 40⊳ ⊲13.5⊳<br />
D 0.62Pr 0.36 Re 0.5 ⊲ka/ks⊳ ⊲Re > 40⊳<br />
where Re, the Reynolds number, is<br />
Re D vfd<br />
a<br />
⊲13.6⊳<br />
with vf the free stream velocity of the fluid, a its kinematic viscosity, ka<br />
its thermal conductivity and Pr is the Prandtl number (of order unity). For<br />
the cellular metal, Bi will differ from equation (13.5) by a proportionality<br />
coefficient (analogous to that for the thermal conductivity) resulting in an<br />
effective value:<br />
Bieff D 1.2 Bi ⊲13.7⊳<br />
where the coefficient 1.2 has been determined by experimental calibration<br />
(Bastawros et al., in press).<br />
This set of equations provides a complete characterization of the heat<br />
transfer coefficient. The trends are found upon introducing the properties of