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FLOW AROUND A CYLINDER - istiarto

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– 4.51 –<br />

��<br />

�� �� �� NIT<br />

u,v,w 10 �6 [m 4 /s 2 ] 10 �3 2<br />

p 10 �5 [m 3 /s] 10 �2 20<br />

k� 10 �6 [m 5 /s 3 ] 10 �3 5<br />

� 10 �6 [m 5 /s 4 ] 10 �3 5<br />

The calculation sequence is presented in the calculation diagram depicted in Fig. 4.14,<br />

and is summarized as follows:<br />

a) Initialize all dependent variable: ����� o �(u,v,w,p,k,� are given).<br />

b) Define the geometrical properties, discretise the spatial domain.<br />

c) Compute initial discharges, qcf, and eddy viscosity, �t.<br />

d) Assign estimated pressures p � ,.<br />

e) Construct coefficients of the discretized momentum equations.<br />

f) Solve the momentum equations for u � , v � , and w � , consecutively.<br />

g) Construct coefficients of the discretized pressure correction equation.<br />

h) Solve the pressure-correction equation for p c and subsequently update the pressure, p,<br />

and velocities at the cell centers, u, v, and w.<br />

i) Compute the new discharge across cell faces, q cf .<br />

j) Return to step ‗d‘ if the velocity components and pressure do not satisfy the<br />

momentum and continuity equations.<br />

k) Construct coefficients of the discretized k transport equation and solve for k; do the<br />

same procedure to get �.<br />

l) Compute the eddy viscosity, �t, from the new k and �<br />

m) Update the water surface if the solution has converged, otherwise assign the new u, v,<br />

w, p, k, and � as the new ‗old‘ values and return to step ‗d‘.<br />

n) Stop the iteration if the steady-state solution has been reached, otherwise proceed to<br />

the next time step, return to step ‗d‘.

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