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16 S. Men<strong>de</strong>z and F. Nicoud<br />

ROWS<br />

1 3 5 7 9 11<br />

a<br />

12<br />

10<br />

b<br />

8<br />

y/d<br />

6<br />

4<br />

2<br />

P b<br />

P a<br />

P c<br />

0.4 0.6 0.8 1.0<br />

< U > /V j<br />

Figure 10. Experimental measurements: (a): perforated zone of the LARA plate with the<br />

measurements locations (+ ,⋄ , • , ), (b): time-averaged streamwise velocity profiles evolution<br />

in the injection region: + : fifth row, ⋄ : seventh row, • : ninth row, : eleventh row. Profiles are<br />

measured 3 diam<strong>et</strong>ers downstream of each row, on the centreline plane.<br />

located as in the experiment (figure 4c) and the RMS peak is well reproduced (figure 5c)<br />

in both shape and level. At the same time, significant differences can be found in the film<br />

core region (y > 2 d) where the numerical streamwise mean velocity is systematically<br />

larger than the experimental values. A closer investigation of the experimental data<br />

base supports the i<strong>de</strong>a that this difference is mainly due to the difference b<strong>et</strong>ween the<br />

configurations that are studied: recall that <strong>simulation</strong>s characterise the flow around an<br />

infinite perforated plate while measurements correspond to the ninth row of a spatially<br />

evolving flow. From figure 10, which displays the mean streamwise velocity profiles at<br />

several locations along the perforated plate, the velocity of the film core (above the j<strong>et</strong>)<br />

tends to increase with the number of upstream rows. Measurements are performed 3<br />

diam<strong>et</strong>ers downstream of the centre of the hole located in the middle of each row, far<br />

from the lateral walls (see figure 10a). Velocity profiles show the formation of a film<br />

created by effusion through the plate. The j<strong>et</strong>s interact tog<strong>et</strong>her to form a film that<br />

<strong>de</strong>velops in the ‘hot’ si<strong>de</strong>, modifying the primary flow in the neighborhood of the plate.<br />

Time-averaged streamwise velocity profiles (figure 10b) are characterised by three peaks:<br />

the first one (P a ), next to the wall, represents the j<strong>et</strong> core (y/d ≈ 1). The second peak<br />

(y/d ≈ 3) represents the film core (P b ), which results from the interaction of all the<br />

upstream j<strong>et</strong>s with the main flow. The presence of a secondary velocity peak, located<br />

below the j<strong>et</strong> core and due to the entrainment process, can also be observed (P c ) at<br />

y/d ≈ 0.5.<br />

An important feature visible from figure 10 is that the peaks behave differently: the<br />

peak related to the j<strong>et</strong> just upstream does not change a lot from one row to the other,<br />

whereas the peaks corresponding to the film core and the entrainment process are highly<br />

influenced by the number of rows upstream of the measurement location. Since P a is<br />

related to the j<strong>et</strong> just upstream and the flow rate is roughly uniform along the plate, this<br />

peak does not <strong>de</strong>pend on the position over the plate. On the contrary, P b and P c are<br />

directly related to the velocity of the main flow just upstream the hole and thus their<br />

amplitu<strong>de</strong> <strong>de</strong>pend on the number of row upstream, viz. on the position over the plate. It<br />

is also obvious from figure 10 that the experimental results are not established at row 9:<br />

the j<strong>et</strong> core is rapidly established, but peaks P b and P c continue to evolve. Now, since in

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