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Metal Foams: A Design Guide

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Chapter 13<br />

Thermal management and heat transfer<br />

13.1 Introduction<br />

The thermal conductivities of metal foams (see Table 4.1(b)) are at least an<br />

order of magnitude greater than their non-metallic counterparts, so they are<br />

generally unsuited for simple thermal insulation though they can provide some<br />

fire protection. The thermal conductivities of closed-cell foams are, however,<br />

lower than those of the fully dense parent metal by a factor of between 8<br />

and 30, offering a degree of fire protection in, for instance, an automobile<br />

bulkhead between engine and passenger compartment. More important, opencell<br />

metal foams can be used to enhance heat transfer in applications such<br />

as heat exchangers for airborne equipment, compact heat sinks for power<br />

electronics, heat shields, air-cooled condenser towers and regenerators (Antohe<br />

et al., 1996; Kaviany, 1985). The heat-transfer characteristics of open-cell<br />

metal foams are summarized in this chapter.<br />

Examples of the use of metfoams for thermal management can be found in<br />

the case studies of Sections 16.4, 16.5, 16.6 and 16.8.<br />

Figure 13.1 illustrates a prototypical heat-transfer configuration. Heat<br />

sources are attached to thin conducting substrates between which is bonded<br />

a layer of open-celled foam of thickness b and length L. A fluid is pumped<br />

at velocity vf through the foam, entering at temperature T0 and exiting at<br />

temperature Te. An idealization of the foam structure is shown below: the<br />

relative density is Q D c/ s and the diameter of the cell edges is d. Thelocal<br />

heat-transfer coefficient at the surface of a cell edge is h.<br />

There are three guiding design principles.<br />

1. High conductivity ligaments are needed that transport the heat rapidly into<br />

the medium: the preference is for metals such as Cu or Al.<br />

2. A turbulent fluid flow is preferred that facilitates high local heat transfer<br />

from the solid surface into the fluid.<br />

3. A low-pressure drop is needed between the fluid inlet and outlet such that<br />

the fluid can be forced through the medium using a pumping system with<br />

moderate power requirements making low fluid viscosity desirable.<br />

Heat transfer to the fluid increases as either the ligament diameter, d,<br />

becomes smaller or the relative density, / s, increases because the internal

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