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Falling liquid films with blowing and suction

Published online by Cambridge University Press:  15 December 2015

Alice B. Thompson*
Affiliation:
Department of Mathematics, Imperial College London, London SW7 2AZ, UK
Dmitri Tseluiko
Affiliation:
Department of Mathematical Sciences, Loughborough University, Loughborough LE11 3TU, UK
Demetrios T. Papageorgiou
Affiliation:
Department of Mathematics, Imperial College London, London SW7 2AZ, UK
*
Email address for correspondence: alice.thompson1@imperial.ac.uk

Abstract

Flow of a thin viscous film down a flat inclined plane becomes unstable to long-wave interfacial fluctuations when the Reynolds number based on the mean film thickness becomes larger than a critical value (this value decreases as the angle of inclination to the horizontal increases, and in particular becomes zero when the plate is vertical). Control of these interfacial instabilities is relevant to a wide range of industrial applications including coating processes and heat or mass transfer systems. This study considers the effect of blowing and suction through the substrate in order to construct from first principles physically realistic models that can be used for detailed passive and active control studies of direct relevance to possible experiments. Two different long-wave, thin-film equations are derived to describe this system; these include the imposed blowing/suction as well as inertia, surface tension, gravity and viscosity. The case of spatially periodic blowing and suction is considered in detail and the bifurcation structure of forced steady states is explored numerically to predict that steady states cease to exist for sufficiently large suction speeds since the film locally thins to zero thickness, giving way to dry patches on the substrate. The linear stability of the resulting non-uniform steady states is investigated for perturbations of arbitrary wavelength, and any instabilities are followed into the fully nonlinear regime using time-dependent computations. The case of small amplitude blowing/suction is studied analytically both for steady states and their stability. Finally, the transition between travelling waves and non-uniform steady states is explored as the amplitude of blowing and suction is increased.

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© 2015 Cambridge University Press
Figure 0

Figure 1. Sketch of flow domain showing coordinate system. We consider a fluid layer with mean height $h_{s}$, bounded along $y=0$ by a rigid planar wall inclined at angle ${\it\theta}$ to the horizontal, and at $y=h(x,t)$ by a free surface. Fluid is injected through the wall, and so the normal velocity at the wall is given by the prescribed function $v=F(x,t)$.

Figure 1

Figure 2. The steady-state deflection of a uniform film for $F=A\cos (2{\rm\pi}x/L)$ for $A\ll 1$, with $L=10$ (a) and $L=40$ (b), $C=0.05$, ${\it\theta}={\rm\pi}/4$ and $R=2$. The $O(A)$ correction $\text{Re}({\hat{H}})$ is shown for the Benney equations (solid line) and the weighted-residual equations (dashed line), with ${\hat{H}}$ defined in (4.2) and (4.3), respectively. The dotted line indicates the scaled suction profile $F(x)/A$.

Figure 2

Figure 3. Bifurcation structure for steady solutions to the weighted-residual equations as $A$ increases, subject to fixed mean layer height of 1, and calculated in a periodic domain of length $2L$. Here $F=A\cos (2{\rm\pi}x/L)$, $L=10$, $C=0.05$, ${\it\theta}={\rm\pi}/4$, with $R=0$, 3, 6, 9 in (ad), respectively. The shaded inset solutions lie on the dashed branch of subharmonic steady solutions, which is unstable; all other solutions are harmonic, with period $L$. Solutions filled in black are stable, while white solutions are unstable. We also indicate pitchfork bifurcations at $A=A_{P}$ (♦), limit points at $A=A_{LP}$ (●), Hopf bifurcations within the domain of length $L$ (▪) and states with $\min q=0$ ($\star$).

Figure 3

Figure 4. Time evolution subject to periodic-boundary conditions, for $R=0$, $L=10$, $C=0.05$, $F=A\cos (2{\rm\pi}x/L)$, with (a) initial condition $h=1$ in a domain of length $L$ for $A_{LP} ($A=0.8$) so that there are no steady states, and (b) initial condition $h=1+0.001\cos {\rm\pi}x/10$ in a domain of length $2L$ with $A_{P} ($A=0.72$) so that steady states exist but are unstable. In both cases, the film height vanishes in finite time at a single point in the domain.

Figure 4

Figure 5. The bifurcation structure for steady solutions to the weighted residual equations as $A$ increases, subject to fixed mean height (a,c) and fixed mean flux (b,d). Here $L=10$, $C=0.05$ and ${\it\theta}={\rm\pi}/4$. The symbols mark the same bifurcations as in figure 3, but we do not show Hopf bifurcations here. Solution branches terminate at a point where the minimum layer height vanishes. (a$\bar{h}=1$, $R=0$. (b$\bar{q}=2/3$, $R=0$. (c$\bar{h}=1$, $R=2$. (d$\bar{q}=2/3$, $R=2$.

Figure 5

Figure 6. Solutions for the interface shape, velocity field and stagnation points for ${\it\theta}={\rm\pi}/4$, $C=0.05$, $L=10$, $R=0$. Periodicity is enforced with $L=10$, but solutions are plotted over two periods and are shown with aspect ratio 1. Stagnation points with $q(x)F^{\prime }(x)<0$ and with $q(x)F^{\prime }(x)>0$ are indicated by ○ and ▫, respectively. (a) Steady state for $A=0.2$, (b$A=0.4$, (c$A=0.5$, (d$A=0.6$, (e) there are no steady states for $A=0.8$; this is a final snapshot before drying. In (a,b), $q>0$ everywhere, so a streamline emanating from the stagnation point with $q(x)F^{\prime }(x)>0$ divides fluid into particles which never meet the wall (yellow), and particles which enter and leave through the wall (blue). For $A>A^{\ast }=0.46$, all steady solutions have regions of negative $q$, corresponding to a region of upstream flow near the stagnation point (between the vertical lines), and all fluid particles must reach the wall.

Figure 6

Figure 7. Effect of small $A$ blowing and suction with wavelength $L$ on the critical Reynolds number for perturbations of underlying wavenumber $k$ as measured through the weighted-residual results for $W$, with $C=0.05$. The filled circles on each curve mark the point where $k=2{\rm\pi}/L$. The dashed lines show the long-wave asymptotic estimate (5.16). (a${\it\theta}={\rm\pi}/4$, (b${\it\theta}={\rm\pi}/2$, (c${\it\theta}=3{\rm\pi}/4$.

Figure 7

Figure 8. The effect of small amplitude blowing and suction with wavenumber $m$ on perturbations with $k=0$ and with $k=m$ in the Benney and weighted-residual (WR) models, as described by the quantity $W$ defined in (5.14); $W>0$ in the shaded regions, so small-amplitude blowing and suction increases the critical Reynolds number, and has a stabilising effect on the flow. Results for ${\it\theta}={\rm\pi}/4$, ${\rm\pi}/2$, $3{\rm\pi}/4$ are shown in rows (ad), (eh) and (il) respectively. (a,e,i) Benney, $k=0$; (bfj) WR, $k=0$; (c,g,k) Benney, $k=m$; (d,h,l) WR, $k=m$.

Figure 8

Figure 9. Stability properties for steady solutions as $R$ and $A$ vary at fixed ${\it\theta}={\rm\pi}/4$ and $C=0.05$, for the weighted-residual model. Steady solutions are divided into three linear-stability categories as indicated by the legend, with finite-$A$ stability boundaries shown by solid black lines. Two small-$A$ estimates for these boundaries are shown: the full result from (5.14) correct to $O(A^{2})$ (solid white line), and the long-wave, small $A$ estimates (5.19) and (5.20) (dash-dotted line). We also indicate solutions with $\min (q)=0$ (dashed line), and the pitchfork bifurcation $A_{P}$ (dotted line). (a$L=10$, (b$L=40$.

Figure 9

Figure 10. Finite $A$ stability results across a range of blowing and suction wavenumber $m$, with $F=A\cos mx$, $C=0.05$ and ${\it\theta}={\rm\pi}/4$. Each black dot indicates that for the given $R$ and $m$, there is some $A$ for which there is a steady state stable to linear perturbations of all wavelengths. The dashed line is obtained by explicit tracking of the maximum stable $R$ for fixed Floquet number $k=0.01$; this curve follows the stability boundary relatively well until it diverges at $m\approx 0.05$. In the small-amplitude long-wave limit, fixed ${\it\alpha}=A/m$ corresponds to fixing the amplitude of interface deflection as $m$ varies. We find that along the dashed line, ${\it\alpha}$ is between 0.5 and 1. To provide an indication of the effectiveness of the small-$A$, long-wave stability prediction (5.19), the solid blue line shows the stability boundary that would be obtained if ${\it\alpha}=1$, which is an overestimate of $A$, but in fact the blue line under predicts the range of stable $R$ for small $m$.

Figure 10

Figure 11. Travelling wave $H({\it\zeta})$ and perturbation functions $J({\it\zeta})$ and $K({\it\zeta})$ as defined in (6.27) for ${\it\theta}={\rm\pi}/4$, $C=0.05$, $R=3$ using the weighted-residual equations, and corresponding superpositions of the travelling wave $H({\it\zeta})$ and $O(A)$ perturbation ${\hat{h}}(x,t)$ as defined in (6.10) for various $A$. $H({\it\zeta})$ has wavelength 30, but blowing and suction are applied with wavelength 20; we show solutions in a domain of length 60. The black contours indicate $h=1$, and the same colour map is used in the first three figures. Both travelling wave and perturbation are periodic in time and space. Nonlinear time-dependent results for $A=0.02$ are shown in figure 13 for various initial conditions.

Figure 11

Figure 12. Contour plots of $h(x,t)$ from nonlinear time-dependent calculations (ae) and using the small-$A$ asymptotic solutions for perturbed travelling waves given by (6.10) and (6.27) (fj) for $R=1.7$, $C=0.05$, ${\it\theta}={\rm\pi}/4$, in a domain of length 60 with suction wavelength $L_{F}=20$. The colour map is scaled to the maximum and minimum value in each column. Here the travelling wave is stable in the absence of suction. Time-dependent results for a larger $R$, for which the uniform film solution is unstable to multiple perturbations, are shown in figure 13. (af$A=0$; (b,g$A=0.02$; (c,h$A=0.04$; (d,i$A=0.10$; (ej$A=0.18$.

Figure 12

Figure 13. Time-dependent simulations in a domain of length 60, with $F=0.02\cos (2{\rm\pi}x/20)$, with $R=3$, $C=0.05$ and ${\it\theta}={\rm\pi}/4$, and varying initial conditions: we set $h(x,0)=1+0.1\cos (2{\rm\pi}nx/60)$ and $q(x,0)=2/3+0.2\cos (2{\rm\pi}nx/60)$, with $n=1,2,3$ in (ac) respectively. These initial conditions correspond to neither travelling waves nor steady states, so nonlinear evolution is required if the system is to reach a periodic state. These plots shows the single contour $h(x,t)=1$, with $h>1$ in the shaded region. The same periodic state is reached eventually, regardless of the initial conditions.

Figure 13

Figure 14. Nonlinear time-dependent calculations subject to blowing and suction $F=A\cos 2{\rm\pi}x/L$, with $L=10$, $C=0.05$, ${\it\theta}={\rm\pi}/4$. The simulations are conducted in a domain of length $6L$, and the initial conditions for $h$ and $q$ includes a small perturbation proportional to $\sin (2{\rm\pi}x/(6L))$. The stable, steady solution shown in (b) can be accessed by either increasing the Reynolds number from (c), or the amplitude of blowing and suction from (a). Time-dependent waves persist at long times in both (a) and (c); in (a), the waves propagate more rapidly and have more than one temporal period; in (c) the waves propagate more slowly, and there is just one propagating wave. (a$A=0.25$, $R=4$; (b$A=0.45$, $R=4$; (c$A=0.45$, $R=2$.

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