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Wall-damped Faraday waves in horizontally oscillating two-layer fluid flows

Published online by Cambridge University Press:  26 December 2024

Linfeng Piao
Affiliation:
Department of Physics and Astronomy and Manchester Centre for Nonlinear Dynamics, The University of Manchester, Oxford Road, Manchester M13 9PL, UK
Anne Juel*
Affiliation:
Department of Physics and Astronomy and Manchester Centre for Nonlinear Dynamics, The University of Manchester, Oxford Road, Manchester M13 9PL, UK
*
Email address for correspondence: anne.juel@manchester.ac.uk

Abstract

We study experimentally the onset of Faraday waves near the end walls of a rectangular vessel containing two stably stratified fluid layers, subject to horizontal oscillations. These subharmonic waves (SWs) are excited, because the horizontal inertial forcing drives a harmonic propagating wave which displaces the interface in the vertical direction at the end walls. We find that the onset of SWs is regulated by a balance between capillary and viscous forces, where the rate of damping is set by the Stokes layer thickness at the wall rather than the wavelength of the SWs. We model the onset of SWs with a weakly damped Mathieu equation and find that the dimensional critical acceleration scales as $\nu _m^{1/2} \omega ^{3/2}$, where $\nu _m$ is the mean viscosity and $\omega$ is the frequency of forcing, in excellent agreement with the experiment over a wide range of parameters.

Information

Type
JFM Rapids
Creative Commons
Creative Common License - CCCreative Common License - BY
This is an Open Access article, distributed under the terms of the Creative Commons Attribution licence (http://creativecommons.org/licenses/by/4.0), which permits unrestricted re-use, distribution and reproduction, provided the original article is properly cited.
Copyright
© The Author(s), 2024. Published by Cambridge University Press.
Figure 0

Figure 1. A snapshot of interfacial instabilities occurring on the interface between two immiscible fluids subject to the horizontal forcing with frequency $f=50$ Hz and amplitude $A=1.67$ mm.

Figure 1

Figure 2. (a) Schematic diagram of the experimental set-up. (b) Visualisation set-up for interfacial dynamics near the end-wall regions and wavy pattern detection method.

Figure 2

Table 1. Physical properties of the liquids used in the experiments. The viscosities of silicone oils were measured at $21\pm 1\,^\circ {\rm C}$ using a Kinexus rheometer.

Figure 3

Figure 3. (a) Schematic diagrams showing the $x$-position of the centre of the container over one period (top) and the ROI (bottom). (ad) Snapshot images of the ROI in different views (see figure 2b) for the HT135-SO50 fluid pair, with the $x$ displacement of the end wall (vertical yellow line) indicating the instantaneous displacement of the vessel. (b) Harmonic wave front of uniform height along $y$, visualised in angled side view ($\,f=35$ Hz, $A=1.30$ mm). (c) Development of SWs on the harmonic wave front in angled side view ($\,f=35$ Hz, $A=1.45$ mm). (d) Experimental snapshots of the SWs visualised in angled top view ($\,f=40$ Hz, $A=1.30$ mm). (e) Superimposed 180$^\circ$ out-of-phase images for patterns observed in (d).

Figure 4

Figure 4. SW patterns near the end walls for fluid pairs (a) HT135-SO10 and (b) HT135-SO50, where images are captured in angled top view (see figure 2b) with the container at its leftmost position (blue circle as in figure 3), for different forcing frequencies: $f=25$ Hz (upper row) and $f=40$ Hz (lower row). In (a), the forcing amplitude $A$ increased from 1.5 mm (1.30$A_c$) to 1.7 mm (1.48$A_c$) at $f=25$ Hz, and from 0.85 mm (1.06$A_c$) to 1.0 mm (1.25$A_c$) at $f=40$ Hz. In (b), $A$ increased from 1.9 mm (1.00$A_c$) to 2.0 mm (1.05$A_c$) at $f=25$ Hz and from 1.3 mm (1.00$A_c$) to 1.4 mm (1.08$A_c$) at $f=40$ Hz. The coordinate system shown was defined in figure 3(a). The yellow line indicates the position of the end wall and the yellow arrow points to the appearance of SWs outside the near-end-wall region (${\sim }3l_{ca}$, as indicated by the red boxes).

Figure 5

Figure 5. Critical acceleration (a) and critical wavenumber (b) as a function of forcing frequency indicating the onset of SWs in the experiment for five fluid pairs with different mean kinematic viscosity, $\nu _{m}$, represented by different symbols. Experimental measurements in (b) are compared with the Faraday wave dispersion relation (lines) for each fluid pair. The red line sits slightly below the black lines because the density of HT270 is approximately 5 % larger than that of HT135 (see table 1).

Figure 6

Figure 6. (a) Log–log plot of non-dimensional acceleration vs non-dimensional frequency for different fluid pairs. A least-squares fit yields $a_{c}^* \sim \omega ^{*1.46 \pm 0.01}$ (dashed line) and the solid line indicates $a_{c}^*\omega ^{*3/2}$ predicted by (3.4) (solid line). Inset: Non-dimensional wavenumber vs $\omega ^*$. The solid lines indicate the Faraday wave dispersion relation on the capillary–viscous scale. (b) Experimental critical acceleration $a_{c}$ plotted against the prediction of (3.4).

Figure 7

Figure 7. Sequence of top-view images showing how droplets are shed from the crests of SWs in the fluid pair HT135-SO100 for $f=25$ Hz ($T=0.04$ s) and $A= 1.07A_{c}=2.65$ mm. The snapshots are taken when the container at its leftmost position (blue circle as in figure 3) and the first image is captured while the SWs are still developing.

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