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The computation of turbulent natural convection flows - Turbulence ...

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<strong>Turbulence</strong> modelling 74<br />

<strong>The</strong> <strong>turbulent</strong> kinetic energy, k, is related to the normal Reynolds stresses by<br />

k = u2 +v 2 +w 2<br />

2<br />

(3.12)<br />

In table 3.1, all the constants and functions <strong>of</strong> the high-Reynolds-number<br />

k-ε model are listed.<br />

cµ cε1 cε2 σk σε<br />

0.09 1.44 1.92 1.0 1.3<br />

Table 3.1 – Values <strong>of</strong> constants in High-Rek-ε, model.<br />

Effect <strong>of</strong> molecular viscosity is not considered in the high-Reynolds-number<br />

k-ε model therefore can not be integrated right across the wall sub-layer. <strong>The</strong><br />

wall-function method is used to provide wall boundary conditions and in-<br />

clude the effect <strong>of</strong> molecular viscosity. <strong>The</strong>se will be discussed in the next<br />

Chapter in detail.<br />

3.3.2 Further modification in High-Re k-ε model for 3D simu-<br />

lations<br />

In cases where there are large strain rates equation 3.4 can become non-<br />

realizable, for example producing negative value for normal stresses. It can<br />

also return a stress field that violates the Schwarz inequality <strong>of</strong> equation 3.13:<br />

uiuj 2 ≤ u 2 i u2 j<br />

(3.13)<br />

when i = j. To prevent the High-Rek-ε from producing non-realizable results<br />

in circumstances that strong shear flow exists, the following constraint can be<br />

used for calculation <strong>of</strong> the <strong>turbulent</strong> viscosity in 3D simulations[43]:<br />

⎧<br />

⎨<br />

µt = min<br />

⎩ cµ<br />

k 2<br />

ε ,<br />

<br />

∂U max ∂y<br />

∂V + ∂x<br />

2/3k<br />

<br />

<br />

, ∂U<br />

∂z<br />

+ ∂W<br />

∂x<br />

<br />

<br />

,<br />

∂V<br />

∂z<br />

+ ∂W<br />

∂y<br />

⎫<br />

⎬<br />

<br />

<br />

<br />

⎭<br />

(3.14)

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