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Zienkiewicz O.C., Taylor R.L. Vol. 3. The finite - tiera.ru

Zienkiewicz O.C., Taylor R.L. Vol. 3. The finite - tiera.ru

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the ¯uid and of the solid are coupled. For a survey of this problem the reader is<br />

referred to the recent book by <strong>Zienkiewicz</strong> et al. 44<br />

Here we use the averaged governing equations derived by many investigators to<br />

solve buoyancy driven convection in a porous medium. 45;46 <strong>The</strong>se equations can be<br />

summarized for a variable porosity medium as 46<br />

continuity<br />

momentum<br />

f<br />

"<br />

energy<br />

@ui @<br />

‡<br />

@t @xj ˆÿ 1<br />

"<br />

@<br />

@x i<br />

u ju i<br />

"<br />

…p"†‡ 1<br />

"<br />

@<br />

@x i<br />

R h<br />

@u i<br />

@x i<br />

@T<br />

@t ‡ u @T<br />

i<br />

@ui ˆ 0 …5:17†<br />

@xi ÿ u i ÿ C f<br />

p<br />

@x i<br />

ˆ @<br />

@x i<br />

p<br />

ukuk " 3=2 ui ‡ gi …T1 ÿ T† …5:18†<br />

k @T<br />

@x i<br />

…5:19†<br />

where u i are the averaged velocity components, " is the porosity of the medium, is<br />

the medium permeability, C is a constant derived from experimental correlations and<br />

here we use Ergun's relations 47 in our calculations (some investigators vary the nonlinear<br />

term using a non-dimensional parameter called the Forchheimer number;<br />

interested readers can consult reference 48), k is the thermal conductivity of the<br />

porous medium and R h is the averaged heat capacity given as<br />

R h ˆ "… c p† f ‡…1 ÿ "†… c p† s<br />

…5:20†<br />

In the above equations, subscripts f and s correspond to ¯uid and solid respectively.<br />

<strong>The</strong> following relation for permeability can be used if the porosity and average<br />

particle size are known<br />

ˆ<br />

" 3 d 2 p<br />

150…1 ÿ " 2 †<br />

Buoyancy driven ¯ows 159<br />

…5:21†<br />

where d p is the particle size. Some researchers use a value for di€erent from the ¯uid<br />

viscosity. However, here we generally use the ¯uid viscosity. More details on the<br />

derivation of the above equations can be found in the cited articles.<br />

As the st<strong>ru</strong>cture of the above governing equations is similar to that of the singlephase<br />

¯ow equations, the application of the CBS algorithm is obvious. 49ÿ55 However<br />

the fully explicit or semi-implicit forms cannot be used e ciently due to strong porous<br />

medium terms. Here, to overcome the time step limitations imposed by these terms<br />

(last two terms before the body force in the momentum equation) we need to solve<br />

them implicitly, though quasi-implicit schemes 47;49 can be used. Although the CBS<br />

algorithm is an obvious choice here, use of convection stabilizing terms can be<br />

neglected in low Rayleigh number (Reynolds number) porous media ¯ows.

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