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Natural convection in enclosures with localized heating from below ...

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HFF<br />

10,5<br />

520<br />

Figure 1.<br />

Geometry and boundary<br />

conditions of the<br />

problem<br />

analyzed steady natural <strong>convection</strong> <strong>in</strong> an enclosure heated <strong>from</strong> <strong>below</strong> and<br />

symmetrically cooled <strong>from</strong> the sides. The effects of the Rayleigh number, the<br />

Prandtl number and aspect ratio on the flow and energy transport were<br />

determ<strong>in</strong>ed. Ramos and Milanez (1998) performed an experimental and<br />

numerical analysis for natural <strong>convection</strong> flow caused by heat sources<br />

dissipat<strong>in</strong>g energy at a constant rate simulat<strong>in</strong>g electronic components<br />

mounted at the bottom surface of a cavity symmetrically cooled <strong>from</strong> the sides<br />

and <strong>in</strong>sulated at the top.<br />

In the present study, natural <strong>convection</strong> <strong>in</strong> a square enclosure <strong>with</strong> <strong>localized</strong><br />

heat<strong>in</strong>g <strong>from</strong> <strong>below</strong> and symmetrical cool<strong>in</strong>g <strong>from</strong> the sides is considered. As it<br />

appears <strong>from</strong> the exist<strong>in</strong>g literature, this study is the first attempt at study<strong>in</strong>g<br />

the natural <strong>convection</strong> phenomenon <strong>in</strong> an enclosure under the above mentioned<br />

thermal conditions. Symmetrical cool<strong>in</strong>g <strong>from</strong> the sides is expected to be an<br />

efficient cool<strong>in</strong>g option, while partial heat<strong>in</strong>g at the lower surface simulates the<br />

electronic components such as chips. S<strong>in</strong>ce natural <strong>convection</strong> flows <strong>in</strong><br />

<strong>enclosures</strong> arise <strong>in</strong> many eng<strong>in</strong>eer<strong>in</strong>g processes, the results to be obta<strong>in</strong>ed here<br />

may be applicable to other fields of <strong>in</strong>terest. The effects of the Rayleigh number<br />

and the nondimensional isothermal heat source length on the fluid flow and<br />

heat transfer are determ<strong>in</strong>ed. For = 0, which means that the whole part of the<br />

lower wall is heated, the boundary conditions applied here are identical to those<br />

considered by Ganzorolli and Milanez (1995).<br />

Analysis<br />

Consider the motion of a viscous fluid <strong>with</strong><strong>in</strong> a square enclosure <strong>with</strong> equal<br />

length and height, L=H, which is depicted <strong>in</strong> Figure 1. The size of the<br />

y<br />

T c<br />

x<br />

I<br />

T H<br />

adiabatic<br />

L<br />

adiabatic<br />

T c<br />

H

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