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Abstracts - KTH Mechanics

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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 />

65

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