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Energy dissipation rate limits for flow through rough channels and tidal flow across topography

Published online by Cambridge University Press:  04 November 2016

R. R. Kerswell*
Affiliation:
School of Mathematics, Bristol University, Bristol BS8 1TW, UK
*
†Email address for correspondence: R.R.Kerswell@bristol.ac.uk

Abstract

An upper bound on the energy dissipation rate per unit mass, $\unicode[STIX]{x1D700}$ , for pressure-driven flow through a channel with rough walls is derived for the first time. For large Reynolds numbers, $Re$ , the bound – $\unicode[STIX]{x1D700}\leqslant cU^{3}/h$ where $U$ is the mean flow through the channel, $h$ the channel height and $c$ a numerical prefactor – is independent of $Re$ (i.e. the viscosity) as in the smooth channel case but the numerical prefactor $c$ , which is only a function of the surface heights and surface gradients (i.e. not higher derivatives), is increased. Crucially, this new bound captures the correct scaling law of what is observed in rough pipes and demonstrates that while a smooth pipe is a singular limit of the Navier–Stokes equations (data suggest $\unicode[STIX]{x1D700}\sim 1/(\log Re)^{2}U^{3}/h$ as $Re\rightarrow \infty$ ), it is a regular limit for current bounding techniques. As an application, the bound is extended to oscillatory flow to estimate the energy dissipation rate for tidal flow across bottom topography in the oceans.

Information

Type
Papers
Copyright
© 2016 Cambridge University Press 
Figure 0

Figure 1.The flow geometry. The top boundary is given by $z=g(x,y)$ and the bottom by $z=f(x,y)$. The intermediate surface shown in outline is parametrised by $\unicode[STIX]{x1D706}$ and defined by $z=F(x,y,\unicode[STIX]{x1D706}):=(1-\unicode[STIX]{x1D706})f(x,y)+\unicode[STIX]{x1D706}g(x,y)$.

Figure 1

Figure 2.(a) The 2-D ridge tidal problem with the ocean represented by the region $z\leqslant 1/2$. (b) A cartoon of the Moody diagram for pipe flow (Moody 1944): $C_{f}:=\unicode[STIX]{x1D700}/(U^{3}/h)$, laminar flow has $C_{f}\sim 1/Re$, turbulent smooth pipe data suggest $C_{f}\sim 1/(\log Re)^{2}$ at least to $Re=O(10^{8})$ and turbulent rough pipe data have $C_{f}\sim O(1)$ as $Re\rightarrow \infty$. Three lines are shown for rough pipe flow with the data increasing to higher $C_{f}$ as the representative height of the roughness increases.