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FLOW AROUND A CYLINDER - istiarto

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4.1 Governing equations<br />

– 4.2 –<br />

The flow model that is developed in this work is based on the approximate solution of the<br />

time-averaged equations of motion and continuity for incompressible flows by using<br />

finite-volume method. In the Cartesian coordinate system these equations read:<br />

�u<br />

�t<br />

�v<br />

�t<br />

�w<br />

�t<br />

�u<br />

�x<br />

� �uu<br />

�x<br />

� �uv<br />

�x<br />

� �uw<br />

�x<br />

� �vu<br />

�y<br />

� �vv<br />

�y<br />

� �vw<br />

�y<br />

� �wu<br />

�z<br />

� �wv<br />

�z<br />

� �ww<br />

�z<br />

1 �p<br />

� �<br />

� �x<br />

1 ��xx 1 ��yx 1 ��zx � � �<br />

� �x � �y � �z � gx 1 �p 1 �� xy 1 ��yy 1 ��zy � � � � �<br />

� �y � �x � �y � �z � gy 1 �p 1 �� xz 1 �� yz 1 ��zz � � � � �<br />

� �z � �x � �y � �z � gz (4.1)<br />

(4.2)<br />

(4.3)<br />

�v �w<br />

� � � 0 (4.4)<br />

�y �z<br />

in which x, y, and z are Cartesian co-ordinates in the horizontal, transversal, and vertical,<br />

respectively; u, v, and w are the corresponding (time-averaged) velocity components, p is<br />

the (time-averaged) pressure, � is the mass density of water, g x , g y , g z are the x, y , z<br />

components of the gravitational acceleration, and �ij‘s are the j direction components of<br />

the shear stress acting on the surface normal to the i direction. These stresses are due to<br />

the molecular viscosity and turbulent fluctuation. For flows having sufficiently high<br />

Reynolds number, the viscous stresses are much smaller in comparison with those of the<br />

turbulence and thus can be neglected. Using Boussinesq‘s eddy viscosity concept, these<br />

stresses are proportional to the velocity gradients according to the following expressions<br />

(see Rodi, 1984, p. 10):<br />

� xx<br />

� � �t 2 �u 2 � 3<br />

�x k,<br />

� yy<br />

� � �t 2 �v 2<br />

� 3 k,<br />

�y<br />

�zz � � �t2 �w 2<br />

� 3 k,<br />

�z<br />

� xy<br />

� � � yx<br />

� xz<br />

� � � zx<br />

� yz<br />

� � � zy<br />

� � � ���v<br />

�u��<br />

t �� � ��,<br />

���x<br />

�y ��<br />

� � � ���w<br />

�u��<br />

t �<br />

���x<br />

�z �� ,<br />

� � � ���w<br />

�v��<br />

t �<br />

��<br />

��<br />

�y �z��<br />

��.<br />

(4.5)<br />

in which �t is the turbulent or eddy viscosity and k is the turbulent kinetic energy defined<br />

as k � 1 2�u<br />

�� u ���<br />

v �� v ���<br />

w ��w<br />

���<br />

where superscripts mean the fluctuating components.<br />

Inserting the definitions in Eq. 4.5 into the momentum equations, Eqs. 4.1 to 4.3, one<br />

obtains:

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