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The significance of coherent flow structures for the turbulent mixing ...

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5 Investigation <strong>of</strong> <strong>the</strong> xy-plane<br />

<strong>the</strong> log-law holds, is quite large <strong>for</strong> both cases so that a direct interaction between <strong>the</strong> nearwall<br />

<strong>flow</strong> structure with <strong>the</strong> intermittent <strong>flow</strong> region can not take place. Thus <strong>the</strong> <strong>turbulent</strong><br />

<strong>flow</strong> state can be considered as fully developed. Fully developed <strong>flow</strong>s are characterised by<br />

a Kolmogorov cascade including an inertial range over at least one order <strong>of</strong> magnitude in <strong>the</strong><br />

wavenumber space [78]. This condition implies unsteadiness, rotational, three-dimensionality,<br />

non-deterministic, diffusion and dissipation, e.g. attributes which are generally referred to<br />

characterise <strong>turbulent</strong> <strong>flow</strong>s. <strong>The</strong> dynamic <strong>of</strong> <strong>the</strong> velocity signal as a function <strong>of</strong> <strong>the</strong> wall distance<br />

can be estimated from figure 5.3 which shows <strong>the</strong> normalised rms values <strong>of</strong> <strong>the</strong> three<br />

velocity fluctuations <strong>for</strong> both <strong>flow</strong> cases. It can be seen that <strong>the</strong> maximum can be properly<br />

resolved with state-<strong>of</strong>-<strong>the</strong>-art PIV systems, provided <strong>the</strong> magnification <strong>of</strong> <strong>the</strong> imaging system<br />

is well adjusted relative to <strong>the</strong> <strong>flow</strong> <strong>structures</strong> and <strong>the</strong> problems associated with <strong>the</strong> strong wall<br />

reflections are solved. <strong>The</strong> low Reynolds number results agree quite well with <strong>the</strong> HWA measurements<br />

kindly provided by Pr<strong>of</strong>. Dr. Fernholz. Only <strong>the</strong> first two measurement points near<br />

<strong>the</strong> wall are overestimated. This is natural due to <strong>the</strong> finite size <strong>of</strong> <strong>the</strong> measurement volume.<br />

When <strong>the</strong> high Reynolds number results are considered <strong>the</strong> deviation increases but <strong>the</strong> increase<br />

<strong>of</strong> <strong>the</strong> second peak with increasing Reynolds number is clearly visible and in agreement with<br />

<strong>the</strong> literature [21]. To validate <strong>the</strong> degree <strong>of</strong> anisotropy between different velocity components<br />

in <strong>turbulent</strong> shear <strong>flow</strong>s, <strong>the</strong> ratio between orthogonal velocity fluctuations is shown in<br />

<strong>the</strong> right graphs <strong>of</strong> <strong>the</strong> same figure. As <strong>the</strong> energy from <strong>the</strong> mean motion is first transferred into<br />

<strong>the</strong> stream-wise velocity fluctuation be<strong>for</strong>e <strong>the</strong> transfer into ³ <strong>the</strong> ´ and component takes place<br />

by means <strong>of</strong> pressure fluctuations, <strong>the</strong> value <strong>of</strong> <strong>the</strong> anisotropy parameter is usually around 0.6<br />

<strong>for</strong> large wall distances. In addition, it can be seen µ ³ ¬' ·E¬'¸ ±º¹ ¬ that increases gradually with<br />

<strong>the</strong> wall distance. Figure 5.4 shows <strong>the</strong> turbulence-level defined µ · ¬ ¸ ±º¹ ¬ » as <strong>for</strong> both<br />

~½¿¾7À<br />

<strong>flow</strong><br />

’¥ÁŒŒÂŒ and<br />

cases. <strong>The</strong> agreement with <strong>the</strong> hot-wire measurements per<strong>for</strong>med ¼ at<br />

is excellent. Only <strong>the</strong> first PIV measurement point in <strong>the</strong> left graph is far away from <strong>the</strong> HWA<br />

result, which is à · 4‘<br />

around Ä4Å

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