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FLOW AROUND A CYLINDER - istiarto

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– 3.29 –<br />

3.4 Bed shear-stresses along the plane of symmetry<br />

Determination of the bed shear-stress, � o , from the experimental data is a rather difficult<br />

task. While a direct measurement technique would be most desirable, here we must<br />

content ourselves with the estimate values based on available data from the velocity and<br />

shear-stress distributions (see Fig. 3.1 and Fig. 3.9). Three alternative methods were used:<br />

1. Based on the velocities, u and w, measured closest to the bed, z ≈ 4 [mm], a velocity<br />

parallel to the bed —at a distance of � n — was calculated, V t ; the bed shear-stress<br />

was calculated as:<br />

���Vt<br />

��<br />

�o,1 � � �t ���n<br />

�� � � � ��Vt<br />

��<br />

t ���n<br />

��<br />

(3.5)<br />

where � t �1.3 �10 �5 [m 2 s 2 ] was taken as the measured eddy-viscosity in the<br />

approach flow.<br />

2. Based on the measured shear-stress distribution (see Fig. 3.9), a (rather subjective)<br />

extrapolation towards the bed was used to obtain the bed shear-stress, or:<br />

�o,2 � �� u ��w<br />

��<br />

� � bed cos� (3.6)<br />

3. Based on a relation for the velocity distribution (see Graf and Altinakar, 1998, pp.<br />

73-74) the bed shear-stress was evaluated by:<br />

�o,3 � ��u �,3�<br />

2<br />

� � U g<br />

C 2<br />

�� ��<br />

�� ��<br />

�� ��<br />

2<br />

� ��0.07 U�<br />

2 (3.7)<br />

where U is the local depth-averaged flow velocity and C is Chezy coefficient taken as<br />

C = 44 [m 1 2 s] (uniform sand bed with d 50 = 2.1 [mm]).<br />

A numerical simulation of the flow around the cylinder has also been performed (see<br />

Chapter 5), from which the bed shear-stresses can also be obtained; this is denoted as<br />

� o,4 . Its value was obtained with a similar equation as Eq. 3.5, in which the k-�<br />

turbulence model-equation and the logarithmic law-of-the-wall were used to get the eddy<br />

viscosity, � t , and the velocity gradient, �V t �n, (see Chapter 4, Eq. 4.82). For clarity, the<br />

expression used to compute � o,4 is rewritten below:<br />

3 4 1 2<br />

�o,4 � �c � k<br />

�V t<br />

� � (4.82)<br />

�<br />

ln E �n where c � = 0.09 is a k-� model constant, k turbulent kinetic-energy, � = 0.4 Karman<br />

constant, E roughness coefficient of the bed, � n<br />

� � u� � n � dimensionless normal<br />

distance from the bed, and � the kinematic viscosity of water. The sign convention of<br />

� o,4 is the same as that of the velocity.

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