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Scale energy budget for a viscoelastic wall-bounded flow<br />
E. De Angelis ∗ ,N.Marati,C.M.Casciola,R.Piva.<br />
In isotropic conditions polymers affect the turbulent cascade of kinetic energy and<br />
deplete the inertial transfer below Lumley scale 1 . In the context of drag reduction,<br />
anisotropy and inhomogeneity can be included in the analysis by extending to dragreducing<br />
viscoelastic flows the scale energy budget for a Newtonian channel flow 2 ,<br />
∂〈δq 2 δui〉<br />
+<br />
∂ri<br />
∂〈δq2 ∗ δU〉<br />
dU<br />
+2〈δuδv〉 +<br />
∂rx<br />
dy<br />
∂〈v∗δu 2 〉<br />
= −4〈ɛ<br />
∂Y<br />
∗ 〉 +<br />
2ν ∂2 〈δq 2 〉<br />
−<br />
∂ri∂ri<br />
2 ∂〈δp δv〉<br />
+<br />
ρ ∂Y<br />
ν ∂<br />
2<br />
2 〈δq 2 〉<br />
∂Y 2 +4∂〈T ∗ ijδui〉<br />
+<br />
∂rj<br />
∂〈δTi2δui〉<br />
− 4〈ɛ<br />
∂Y<br />
∗ P 〉 ,<br />
where 〈δq 2 〉 = 〈δuiδui〉 is the scale-energy as a funtion of the separation vector ri<br />
and of the mid-point Xi = xi + ri/2, the asterisk denote a mid point average and<br />
ɛ and ɛP are the Newtonian and polymer dissipations. According to the equation,<br />
the local conservation of scale-energy implies that the local source of scale energy<br />
– the sum of local production and the amount intercepted from the spatial flux –<br />
feeds the inertial cascade and the transfer towards the microstructure, see fig. 1. In<br />
the Newtonian plug of mildly drag-reducing flows the behavior is easily explained<br />
given the budget in the log-layer of Newtonian flows 2 and the effect the polymers<br />
have on the cascade 1 . Closer to the wall the polymers are much more active and<br />
directly interfer with the production process. As will be discussed in detail, in this<br />
elastic layer an entirely different picture emerges consistent with the alteration of the<br />
energy containing scales of the flow which entails dramatic consequences for the drag<br />
experienced at the wall.<br />
Figure 1: Scale-energy budget in the Newtonain plug: Force-velocity correlation —,<br />
inertial and polymer transfer (—, —), viscous diffusion —, polymer and Newtonian<br />
dissipation (—, —).<br />
1 De Angelis E., Casciola C.M., Benzi R., Piva R., J. Fluid Mech 476, 105-114 (2003).<br />
2 Marati N., Casciola C. M., Piva R. (2004), J. Fluid Mech 521, 191-215 (2004).<br />
∗ Dip. di Meccanica e Aereonautica, “La Sapienza”, via Eudossiana 18, 00184, Roma, Italy<br />
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