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FLOW AROUND A CYLINDER - istiarto

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– 4.33 –<br />

� extrapolate all variables at P to E: � E � � P<br />

�<br />

�<br />

� the outflowing discharge results:<br />

��<br />

qout � Ve<br />

Pressure and velocity corrections<br />

�Se � VP<br />

�<br />

� Se<br />

The contribution of the discharge across the east face, q e , to the continuity equation, Eq.<br />

4.66, is replaced by the outflowing discharge, q out . In forming the coefficients in Eq. 4.68,<br />

the following steps are done:<br />

p<br />

� set the coefficient at node E to zero: aE � 0<br />

� set the contribution of the inflowing discharge to the source term: b p<br />

� � e � �q out<br />

For the velocity correction, Eq. 4.57, the pressure correction gradient, �p c �x i , is<br />

computed by the finite-volume technique, Eq. 4.20, which requires the value of<br />

p c � � � p<br />

e c<br />

� � ; this latter is obtained by the upwinding: p<br />

E c � � � p<br />

E c � � .<br />

P<br />

4.5.4 Wall boundary<br />

Wall function approach<br />

The wall function approach (Launder and Spalding, 1974) is applied to the cell whose<br />

face is a rigid wall. Major assumptions used in this approach merit to be put forward<br />

before presenting the derivation of the wall function; they are: (1) the no-slip flow<br />

condition prevails at the wall with the universal logarithmic velocity distribution normal<br />

to the wall, (2) the production of the turbulent kinetic energy is merely due to the<br />

(turbulent) shear stress, thus neglecting the effect of the normal stress, and (3) a local<br />

energy balance exists, i.e. the dissipation of the turbulent kinetic energy is equal to the<br />

production. Given in the following paragraphs are the derivations of the wall function in<br />

which those assumptions are further highlighted.

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