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Langmuir-type vortices in wall-bounded flows driven by a criss-cross wavy wall topography

Published online by Cambridge University Press:  07 August 2020

Andreas H. Akselsen*
Affiliation:
Department of Energy and Process Engineering, Norwegian University of Science and Technology, N-7491Trondheim, Norway
Simen Å. Ellingsen
Affiliation:
Department of Energy and Process Engineering, Norwegian University of Science and Technology, N-7491Trondheim, Norway
*
†Email address for correspondence: andreas.h.akselsen@ntnu.no

Abstract

We investigate a mechanism to manipulate wall-bounded flows whereby wave-like undulations of the wall topography drives the creation of bespoke longitudinal vortices. A resonant interaction between the ambient vorticity of the undisturbed shear flow and the undulation of streamlines enforced by the wall topography serves to slightly rotate the spanwise vorticity of the mean flow into the streamwise direction, creating a swirling motion, in the form of regular streamwise rolls. The process is kinematic and essentially identical to the ‘direct drive’ CL1 mechanism for Langmuir circulation (LC) proposed by Craik (J. Fluid Mech., vol. 41, issue 4, 1970, pp. 801–821). Wall shear is modelled by selecting suitable primary flow profiles. A simple, easily integrable expression for the cross-plane streamfunction is found in two asymptotic regimes: the resonant onset of the essentially inviscid instability at early times, and the fully developed steady-state viscous flow. Linear-order solutions for flow over undulating boundaries are obtained, fully analytical in the special case of a power-law profile. These solutions allow us to quickly map out the circulation response to boundary design parameters. The study is supplemented with direct numerical simulations which verify the manifestation of boundary induced Langmuir vortices in laminar flows with no-slip boundaries. Simulations show good qualitative agreement with theory. Quantitatively, the comparisons rest on a displacement length closure parameter adopted in the perturbation theory. While wall-driven LC appear to become unstable in turbulent flows, we propose that the mechanism can promote swirling motion in boundary layers, a flow feature which has been reported to reduce drag in some situations.

Information

Type
JFM Papers
Copyright
© The Author(s), 2020. Published by Cambridge University Press
Figure 0

Figure 1.Sketch of the problem set-up. (Magnitudes of $\eta _\textrm {s}$ and $\eta _\textrm {b}$ are exaggerated.) (a) Wall bounded and (b) free surface.

Figure 1

Figure 2.Boundary topography and the orientation of vortices relative to it: (a) bottom topography with wave vectors $(k_{1x},\pm k_{1y})$ indicated; (b) schematic illustration of swirling streamlines in the cross-flow plane.

Figure 2

Figure 3.Primary flow profiles $U(z)$ from (3.9a,b) with $\delta$ values such that $U(0) = 0.20$.

Figure 3

Figure 4.Free surface flow. Normalised streamfunction (a–c) and normalised streamwise velocity perturbation (d–f) as a function of vertical position. $k_1=3\pi$, $\arctan (k_{1y}/k_{1x})=\pi /8$: (a,d) inviscid; (b,e) viscous, no-slip; (c,f) viscous, full-slip. Power-law (3.9a,b) primary flow profile; solid, dot–dashed, dashed and stippled dotted lines respectively show $q=0.1$ , $0.5$, $1.0$ and $5.0$ with $\delta$ values such that $U(0) = 0.20$ (cf. figure 3).

Figure 4

Figure 5.Similar to figure 4, but with increased wavelength (reduced depth) $k_1 = \pi$: (a,d) inviscid; (b,e) viscous, no-slip; (c,f) viscous, full-slip.

Figure 5

Figure 6.Similar to figure 5, but with increased wavelength (reduced depth) $k_1 = 1.0$: (a,d) inviscid; (b,e) viscous, no-slip; (c,f) viscous, full-slip.

Figure 6

Figure 7.Streamlines $\hat \psi = {{\rm constant}}$ in free surface flow for the $q=1.0$ power-law profile (cf. figures 3–6): (a–c) $k_1 = 3\pi$; (d–f) $k_1 = \pi$; (g–i) $k_1 = 1.0$. Here $\arctan (k_{1y}/k_{1x})=\pi /8$. Isoline values of $\hat {\psi }$ can be inferred from the graphs in figures 4–6 as these give the streamfunction values in a vertical line running through the vortex centre: (a,d,g) inviscid; (b,e,h) viscous, no-slip; (c,f,i) viscous, full-slip.

Figure 7

Figure 8.Extremum of appropriate normalised streamfunctions as a function of the wave vector angle $\theta =\arctan (k_{1y}/k_{1x})$ in free surface flow. This value is proportional to the vortex volume flow through a cross-section from the vortex centre out: $ (a\!-\!c) \ k=3\pi; \ (d\!-\!f) \ k=\pi; \ (g\!-\!i) \ k=1$. Power-law (3.9a,b) primary flow profile; solid, dot–dashed, dashed and stippled dotted lines respectively show $q=0.1$, $0.5$, $1.0$ and $5.0$ with $\delta$ values such that $U(0) = 0.20$ (cf. figure 3): (a,d,g) inviscid; (b,e,h) viscous, no-slip; (c,f,i) viscous, full-slip.

Figure 8

Figure 9.Vertical position of vortex centre as a function of the wave vector angle $\theta =\arctan (k_{1y}/k_{1x})$ in free surface flow: (a,d,g) inviscid; (b,e,h) viscous, no-slip; (c,f,i) viscous, full-slip. See caption of figure 8 for further details.

Figure 9

Figure 10.Normalised (a) streamfunction and (b) streamlines at a value of $\theta$ near the point where the rotational direction of vortices switches. Viscous, no-slip case with $k_1 = 1.0$$\theta =50^\circ$, $q=0.1$ and $U(0)=0.20$.

Figure 10

Figure 11.Free surface flow for varying values of displacement parameter $\delta$ with $\delta$-values such that $U(0) = 0.20$, $0.4$, $0.6$ and $0.8$, respective markers indicated in (a). Solid, $q=0.1$; dashed, $q=1.0$. (a) Primary flow profiles U(z) from (3.9a,b). (b–g) Normalised streamfunction (b–d) and normalised streamwise velocity perturbation (d–g) as a function of vertical position, graphed for various values of $\delta$ with the power-law model (3.9a,b): (b,e) inviscid; (c,f) viscous, no-slip; (d,g) viscous, full-slip. Here $k_1=\pi$, $\arctan (k_{1y}/k_{1x})=\pi /8$. (Curves occasionally overlap.)

Figure 11

Figure 12.Parabolic current profile.

Figure 12

Figure 13.Sketch of the relative wall phase shift when looking along the streamwise direction.

Figure 13

Figure 14.A doubly wall-bounded flow. Normalised streamfunction and streamwise velocity perturbation for three values of $\delta$. Parabolic current profile (figure 12) and a wall-bounded domain with $\vartheta =0$ (see figure 13): (a,d) inviscid; (b,e) viscous, no-slip; (c,f) viscous, full-slip. Here $k_1 = 2\pi$, $\theta =\pi /8$.

Figure 14

Figure 15.Same as figure 14, but with $\vartheta =\pi /2$: (a,d) inviscid; (b,e) viscous, no-slip; (c,f) viscous, full-slip.

Figure 15

Figure 16.A wall-bounded flow. Streamlines $\hat \psi = {{\rm constant}}$ for $\vartheta =0$ (a–c; cf. figure 14), $\vartheta =\pi /4$ (d–f) and $\vartheta =\pi /2$ (g–i; cf. figure 15): (a,d,g) inviscid; (b,e,h) viscous, no-slip; (c,f,i) viscous, full-slip. Here $\delta = 0.05$ and $k_1 = 2\pi$, $\theta =\pi /8$.

Figure 16

Figure 17.Conceptual representation near the boundary with no-slip at the walls with a slip velocity reference boundary located some distance $\delta$ within the flow. Streamlines resemble the actual boundary curvature more closely when $\delta$ is smaller than the amplitude $a$ (a), although this makes the perturbation amplitudes large relative to the assumptions of the linear theory. The situation is the opposite if $\delta >a$ (b).

Figure 17

Figure 18.A double wall-bounded flow. Normalised streamfunctions $\tilde \psi /(Re\,a^2)$ estimated from the steady states of lattice–Boltzmann simulations using (7.1): (a) $\vartheta =0$, $a= 0.0391$, (b) $\vartheta =0$, $a= 0.0625$, (c) $\vartheta =0$, $a= 0.0938$, (d) $\vartheta =\pi /2$, $a= 0.0391$, (e) $\vartheta =\pi /2$, $a= 0.0625$, (f) $\vartheta =\pi /2$, $a= 0.0938$. Here $k_1 \approx 2\pi$, $\theta \approx \pi /8$.

Figure 18

Figure 19.Numerically computed streamlines of the two-dimensional velocity field obtained when averaging along the streamwise dimension: (a) $\vartheta =0$, $a = 0.0391$, (b) $\vartheta =0$, $a = 0.0625$, (c) $\vartheta =0$, $a = 0.0938$, (d) $\vartheta =\pi /2$, $a = 0.0391$, (e) $\vartheta =\pi /2$, $a = 0.0625$, (f) $\vartheta =\pi /2$, $a = 0.0938$. Here $Re_\tau = 20$, $k_1 \approx 2\pi$, $\theta \approx \pi /8$.

Figure 19

Figure 20.Streamline slices of a full three-dimensional flow field: (a) $Re_\tau =15$, $\vartheta =0$, (b) $Re_\tau =30$, $\vartheta =0$, (c) $Re_\tau =15$, $\vartheta =\pi /2$, (d) $Re_\tau =30$, $\vartheta =\pi /2$. Here $a\approx 0.0625$, $k_1 \approx 2\pi$, $\theta \approx \pi /8$. Slice at $x=\pi /6k_{1x}$.

Figure 20

Figure 21.‘Rotating the boundary topography’; $\theta = 3\pi /8$. This will, according to theory, cause rotation in the opposite direction relative to the boundary undulations. Here $k_1=\pi$, $\vartheta = 0$. (a) Theoretical, viscous, no-slip and (b) simulated, $a = 0.0625$.

Figure 21

Figure 22.Unstable vortex field: $Re_\tau = 40$, $\vartheta =\pi /2$, $\theta = \pi /8$, $k_1 = 2\pi$.

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