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Variation of Nu <strong>in</strong> porous medium<br />

us<strong>in</strong>g porous media for <strong>heat</strong> <strong>transfer</strong><br />

Nu/Pe^.5<br />

14.4<br />

14.2<br />

14<br />

13.8<br />

13.6<br />

q''=2.53 kw/m^2<br />

q''=2.12 kw/m^2<br />

q''=1.86 kw/m^2<br />

q''=1.53 kw/m^2<br />

q''=1.27 kw/m^2<br />

problems is emphasized.<br />

3.50<br />

Comparison of Nu for both <strong>heat</strong> <strong>transfer</strong> <strong>in</strong> porous<br />

medium and <strong>in</strong> a clear flow<br />

13.4<br />

3.00<br />

13.2<br />

2.50<br />

13<br />

1200 1610 1810<br />

Re<br />

Nu/pe^.5<br />

2.00<br />

1.50<br />

1.00<br />

With porous<br />

Clear flow<br />

Figure 3:<br />

and <strong>heat</strong> fluxes<br />

For the clear fluid<br />

for various Reynolds<br />

versus<br />

Reynolds number is presented <strong>in</strong> figure 4.<br />

In this case the results show conformity<br />

with the similarity solution. That is, the<br />

relation<br />

exists <strong>in</strong> the clear fluid [2].<br />

Figure 4: versus Reynolds<br />

number <strong>in</strong> clear fluid.<br />

0.50<br />

0.00<br />

Figure 5: Comparison of Nusselt number<br />

for <strong>heat</strong> <strong>transfer</strong> <strong>in</strong> porous media and clear<br />

fluid.<br />

4. Conclusions<br />

The steady state <strong>forced</strong> <strong>convection</strong> <strong>heat</strong><br />

<strong>transfer</strong> around the cyl<strong>in</strong>drical <strong>heat</strong>er<br />

<strong>embedded</strong> <strong>in</strong> the porous media was<br />

exam<strong>in</strong>ed experimentally. The results<br />

compared with the clear fluid case shows<br />

that the porous media enhances the <strong>heat</strong><br />

<strong>transfer</strong> rate. The value of<br />

porous media <strong>in</strong>creases by <strong>in</strong>creas<strong>in</strong>g the<br />

<strong>heat</strong> fluxes and it rema<strong>in</strong>s approximately<br />

constant by <strong>in</strong>creas<strong>in</strong>g the Reynolds<br />

number.<br />

1200 1610 1800<br />

Re<br />

<strong>in</strong><br />

The comparison of Nusselt number is<br />

plotted <strong>in</strong> figure 5. It is evident that porous<br />

media enhance the <strong>heat</strong> <strong>transfer</strong> <strong>from</strong> the<br />

<strong>embedded</strong> <strong>cyl<strong>in</strong>der</strong>. Thus the superiority of<br />

5

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