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Surfactant- and gravity-dependent instability of two-layer channel flows: linear theory covering all wavelengths. Part 1. ‘Long-wave’ regimes

Published online by Cambridge University Press:  23 January 2019

Alexander L. Frenkel
Affiliation:
Department of Mathematics, University of Alabama, Tuscaloosa, AL 35487, USA
David Halpern*
Affiliation:
Department of Mathematics, University of Alabama, Tuscaloosa, AL 35487, USA
Adam J. Schweiger
Affiliation:
Department of Mathematics, University of Alabama, Tuscaloosa, AL 35487, USA
*
†Email address for correspondence: dhalpern@ua.edu

Abstract

A linear stability analysis of a two-layer plane Couette flow of two immiscible fluid layers with different densities, viscosities and thicknesses, bounded by two infinite parallel plates moving at a constant relative velocity to each other, with an insoluble surfactant monolayer along the interface and in the presence of gravity is carried out. The normal modes approach is applied to the equations governing flow disturbances in the two layers. These equations, together with boundary conditions at the plates and the interface, yield a linear eigenvalue problem. When inertia is neglected the velocity amplitudes are the linear combinations of certain hyperbolic functions, and a quadratic dispersion equation for the increment, that is the complex growth rate, is obtained, where coefficients depend on the aspect ratio, the viscosity ratio, the basic velocity shear, the Marangoni number $Ma$ that measures the effects of surfactant and the Bond number $Bo$ that measures the influence of gravity. An extensive investigation is carried out that examines the stabilizing or destabilizing influences of these parameters. Since the dispersion equation is quadratic in the growth rate, there are two continuous branches of the normal modes: a robust branch that exists even with no surfactant, and a surfactant branch that, to the contrary, vanishes when $Ma\downarrow 0$. Regimes have been uncovered with crossings of the two dispersion curves, their reconnections at the point of crossing and separations as $Bo$ changes. Due to the availability of the explicit forms for the growth rates, in many instances the numerical results are corroborated with analytical asymptotics.

Information

Type
JFM Papers
Copyright
© 2019 Cambridge University Press 
Figure 0

Figure 1.Definition sketch of a two-layer Couette flow of two horizontal liquid layers with different thicknesses $d_{i}$ ($i=1$ for the bottom layer and $i=2$ for the top layer), viscosities $\unicode[STIX]{x1D707}_{i}$ and densities $\unicode[STIX]{x1D70C}_{i}$. The disturbed interface is located at $z^{\ast }=\unicode[STIX]{x1D702}^{\ast }(x^{\ast },t^{\ast })$, and is coated by an insoluble surfactant monolayer indicated by dots. Gravity acts in the spanwise direction.

Figure 1

Figure 2.Typical dispersion curves of the two normal modes: (i) the unstable mode, which has a maximum growth rate $\unicode[STIX]{x1D6FE}_{R}=\unicode[STIX]{x1D6FE}_{Rmax}$ at a wavenumber $\unicode[STIX]{x1D6FC}=\unicode[STIX]{x1D6FC}_{max}$ and then decays, eventually becoming stable for $\unicode[STIX]{x1D6FC}>\unicode[STIX]{x1D6FC}_{0}$, and (ii) the stable mode, which has negative growth rates for all wavenumbers.

Figure 2

Figure 3.Partition of the $(n,m)$-plane of the system, $n\geqslant 1$ and $m>0$, into three sectors ($Q$, $R$ and $S$) and their borders corresponding to differences in stability properties of the flow.

Figure 3

Figure 4.(a) Values of $\unicode[STIX]{x1D6FE}_{Rmax}$, (b) $\unicode[STIX]{x1D6FC}_{max}$, (c) $\unicode[STIX]{x1D6FC}_{0}$, for $Bo=0$ and $Bo=0.1$, along with their small-$s$ asymptotics (given by (4.28) for $\unicode[STIX]{x1D6FC}_{0}$ with $Bo=0.1$, equation (4.31) for $\unicode[STIX]{x1D6FC}_{0}$ with $Bo=0$, equation (4.34) for $\unicode[STIX]{x1D6FE}_{Rmax}$ and $\unicode[STIX]{x1D6FC}_{max}$ with $Bo=0$, equation (4.35) for $\unicode[STIX]{x1D6FE}_{Rmax}$ and $\unicode[STIX]{x1D6FC}_{max}$ with $Bo=0.1$), and (d) $\unicode[STIX]{x1D6FE}_{R}$ at $\unicode[STIX]{x1D6FC}=0.01$ and $Bo=0.1$, versus $s$. Here $n=2$ and $m=2$ (which is in the $R$ sector), with $Ma=1$.

Figure 4

Figure 5.Values of (a) $\unicode[STIX]{x1D6FE}_{Rmin}$, (b) $\unicode[STIX]{x1D6FC}_{min}$, (c) $\unicode[STIX]{x1D6FC}_{0}$, for $Bo=-0.001$ and $Bo=-0.1$, along with their small-$s$ asymptotics, and (d) $\unicode[STIX]{x1D6FE}_{R}$ at $\unicode[STIX]{x1D6FC}=0.01$ and $Bo=-0.1$, versus $s$ for $n=2$ and $m=5$ (which is in the $Q$ sector), with $Ma=1$.

Figure 5

Figure 6.Marginal wavenumber $\unicode[STIX]{x1D6FC}_{0}$ versus the shear parameter $s$, along with its asymptotics, at larger $s$, due to the capillary effects, and at smaller $s$, due to the combined gravity–surfactant effects, for $n=2$, $m=2$, $Ma=0.05$ and $Bo=-0.05$.

Figure 6

Figure 7.Values of (a) $\unicode[STIX]{x1D6FE}_{Rmax}$, (b) $\unicode[STIX]{x1D6FC}_{max}$ and (c) $\unicode[STIX]{x1D6FC}_{0}$ versus $\unicode[STIX]{x1D6E5}$ for the same $n$, $m$ and $Ma$ as in figure 4, and $s=1$. The solid lines represent the full solutions, equation (3.17), and the dashed lines represent the asymptotics given by (4.38).

Figure 7

Figure 8.The exact dispersion curve (3.7) (solid line) and the asymptotic expression of the growth rate around the marginal wavenumber (4.52) (dashed line) of $\unicode[STIX]{x1D6FE}_{R}$ for $m=1$, $n=2$, $s=1$, $Ma=1$ and $Bo=1000$.

Figure 8

Figure 9.Dependence on gravity (represented by $Bo$) of the maximum growth rate $\unicode[STIX]{x1D6FE}_{Rmax}$, the corresponding wavenumber $\unicode[STIX]{x1D6FC}_{max}$ and the marginal wavenumber $\unicode[STIX]{x1D6FC}_{0}$ in the $R$, $S$ and $Q$ sectors. Here $s=1$, $Ma=0.1$ and the values of the $(n,m)$ pairs for the $R$ (a,d,g), $S$ (b,e,h), and $Q$ (c,f,i) sectors are $(2,2)$, $(2,0.5)$ and $(2,5)$, respectively.

Figure 9

Figure 10.Dispersion curves given by (3.7) in the $S$ sector ($n=2$, $m=0.5$) for selected values of $Bo$ showing occurrence of two local maxima and a jump in the global maximum. Here $s=1$ and $Ma=0.1$.

Figure 10

Figure 11.Values of (a,b) $\unicode[STIX]{x1D6FE}_{Rmax}$, (c,d) $\unicode[STIX]{x1D6FC}_{max}$ and (e,f) $\unicode[STIX]{x1D6FC}_{0}$ versus $Ma$ for $Bo=1.0$ in the $R$ sector (a,c,e) and $S$ sector (b,d,f). Here $s=1$ and the values of the $(n,m)$ pairs in the $R$ and $S$ sectors are $(2,2)$ and $(2,0.5)$, respectively.

Figure 11

Figure 12.Values of (a,b) $\unicode[STIX]{x1D6FE}_{Rmax}$, (c,d) $\unicode[STIX]{x1D6FC}_{max}$ and (e,f) $\unicode[STIX]{x1D6FC}_{0}$ as functions of $Ma$ for $Bo=-1.0$ in the $R$ sector (a,c,e) and $S$ sector (b,d,f), for the same $s$ and $(n,m)$ points as in figure 11.

Figure 12

Figure 13.The influence of $s$ on (a) the maximum of $\unicode[STIX]{x1D6FE}_{Rmax}$ over all $\unicode[STIX]{x1D6FC}$ and $Ma$ in the $R$ sector (at $n=2$ and $m=2$) and the $S$ sector (at $n=2,m=0.5$) for two different values of $Bo$ as indicated in the legend. Panels (b,c) show the corresponding $\unicode[STIX]{x1D6FC}$ and $Ma$.

Figure 13

Figure 14.The curves (a) $Bo=Bo(\unicode[STIX]{x1D6FC})$ and (b) $Ma=Ma(\unicode[STIX]{x1D6FC})$ such that the discriminant $\unicode[STIX]{x1D701}=0$ are plotted for the values of viscosity ratio $m$ indicated in the legend. Here $n=2$ and $s=1$.

Figure 14

Figure 15.The zero discriminant curve corresponding to the $m=2$ projection curves shown in (a,b) of figure 14.