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Metal Foams: A Design Guide

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~<br />

P<br />

~<br />

Re 2.6<br />

1000<br />

800<br />

600<br />

400<br />

200<br />

0<br />

0<br />

0.002<br />

0.004<br />

d ~<br />

0.006<br />

0.008<br />

Present<br />

materials<br />

Thermal management and heat transfer 187<br />

0.01<br />

Figure 13.4 The power dissipation plotted as a function of the relative<br />

density, Q, and the dimensionless cell-edge diameter, Qd D d/L<br />

where a is the cell size<br />

a D 1.24d � 3 /Q ⊲13.14⊳<br />

The exponent m and the coefficient have been calibrated by experimental<br />

measurements. They are:<br />

m D 0.4<br />

D 4 ⊲13.15⊳<br />

Some typical results are plotted in Figure 13.3. Pressure drops for other conditions<br />

can be predicted from equations (13.13) to (13.15), again with the proviso<br />

that the fluid flow scaling (13.5) retains its validity. The expected behavior is<br />

illustrated in Figure 13.4.<br />

13.5 Trade-off between heat transfer and pressure drop<br />

For any system there is a trade-off between heat flux and pressure drop. A<br />

cross-plot of these two quantities in accordance with the non-dimensional<br />

0<br />

0.1<br />

0.2<br />

0.3<br />

r ~<br />

0.4<br />

0.5

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