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Very-rough-wall boundary layers<br />
Ian P Castro ∗ and Ryan Reynolds ∗<br />
Rough-wall boundary layers are ubiquitous. It is therefore striking that despite<br />
their practical importance a number of the most fundamental questions concerning<br />
the effects of surface roughness on the nature of the turbulent boundary layer remain<br />
unanswered. The classical view was expounded by Townsend 1 , who argued that the<br />
major effect is simply to change the surface stress, altering the value of the constant<br />
in the usual log-law relation for the mean velocity profile, but without structural<br />
changes in the turbulence. This amounts essentially to the assumption that the inner<br />
and outer regions do not interact strongly. For small ratios of roughness height to<br />
boundary layer depth, h/δ < 0.03,say,thereismuchevidencethatthisviewis<br />
reasonable 2,3 . But it must inevitably become increasingly less so as h/δ rises and<br />
thereisevidencethatforlargeenoughh/δ not only can structural features change<br />
throughout the flow, but also that these differences (from the smooth wall boundary<br />
layer) may depend on the topology of the roughness 4,5 . It remains generally unclear<br />
exactly how and under what circumstances the roughness effects extend throughout<br />
the flow.<br />
In this presentation we will discuss these issues, provide further evidence that<br />
roughness effects on the outer flow depend on h/δ and highlight the current uncertainties<br />
about such flows. An example of current work is provided by figures 1(a) and<br />
(b), which show PIV data in the boundary layer flow over a staggered array of cubes<br />
(with h/δ = 14). Such data yield turbulence structural information and differences<br />
from the usual smooth-wall behaviour will be emphasised.<br />
∗ School of Engineering Sciences, University of Southampton, Southampton, UK<br />
1 Townsend AA, The structure of turbulent shear flows, CUP<br />
2 Jimenez J, Ann. Rev. Fluid Mech. 36, 173-196 (2004).<br />
3 Raupach et al., Appl. Mech. Rev. 44, 1-25 (1997).<br />
4 Krogstad P-A & Antonia RA, Expts. in Fluids, 27, 450-460 (1999)<br />
5 Smalley et al., Expts. in Fluids, 33, 31-37 (2002)<br />
Z(mm)<br />
40 VelMag: 0.0 0.2 0.5 0.7 0.9 1.2 1.4 1.6 1.8 2.1 2.3 2.5 2.8 3.0<br />
35<br />
30<br />
25<br />
20<br />
15<br />
10<br />
5<br />
3920 3930<br />
5.0<br />
3940<br />
X(mm)<br />
3950 3960<br />
Z(mm)<br />
Ruu (dx,dz)<br />
40<br />
CrossCorr: -0.20 -0.08 0.04 0.16 0.28 0.40 0.52 0.64 0.76 0.88 1.00<br />
35<br />
30<br />
25<br />
20<br />
15<br />
10<br />
5<br />
3920 3930 3940<br />
X(mm)<br />
3950 3960<br />
Figure 1: (a) PIV ’snapshot’ of fluctuating velocity vectors behind cube in a staggered<br />
array; (b) Spatial correlation contours of the axial mean velocity - fixed ’probe’ above<br />
centre of cube.<br />
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