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KURENAI : Kyoto University Research Information Repository

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'<br />

u = (i)l/7<br />

u~ S 1.7(69)<br />

T -TT= 1 - (s)1/7(70)<br />

wt<br />

Here, S v and St are thicknesses of turbulent velocity boundary layer and<br />

turbulent thermal boundary layer repectively. The thickness of velocity<br />

boundary layer is related to the wall shear stress for turbulent flow` which<br />

is given by Eq.(58). Then (5 vis given by<br />

= 0 .380 x Re xO.2(71)<br />

v On the other hand, the eddy diffusivity of momentum,54, is defined by<br />

eMp = do<br />

dy )(72)<br />

Now, one considers the turbulent region near wall where Eq.(69) can<br />

be applicable. In this near wall region, one may approximate shear stress<br />

T;: by wall shear stress, Tw. Based on this assumption, and substituting<br />

Eqs.(58) and (69) into Eq.(72),one obtains,'<br />

cM<br />

()= 0.545(.)(S)6/7(73)<br />

cov<br />

On the other hand, turbulent diffusivity of heat is defined by<br />

£HOPP=dT<br />

(d )(73)<br />

y)<br />

Again, one considers the turbulent region near wall where Eq.(70) can be<br />

applicable. When the heat capacity of the viscous sublayer is much smaller<br />

than the heat capacity of turbulent thermal boundary layer, the heat flux<br />

q, in Eq.(74) can be approximated by wall heat flux, qw, without serious<br />

130

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