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Interface shape surrounding anisotropic particles held at the liquid–gas interface

Published online by Cambridge University Press:  15 October 2025

Avital Reizman Einhorn
Affiliation:
Faculty of Mechanical Engineering, Technion – Israel Institute of Technology, Haifa 3200003, Israel
Jibu Tom Jose
Affiliation:
Faculty of Mechanical Engineering, Technion – Israel Institute of Technology, Haifa 3200003, Israel
Anna Zigelman
Affiliation:
Faculty of Mechanical Engineering, Technion – Israel Institute of Technology, Haifa 3200003, Israel
Amir Daniel Gat*
Affiliation:
Faculty of Mechanical Engineering, Technion – Israel Institute of Technology, Haifa 3200003, Israel
Omri Ram*
Affiliation:
Faculty of Mechanical Engineering, Technion – Israel Institute of Technology, Haifa 3200003, Israel
*
Corresponding authors: Omri Ram, omri.ram@technion.ac.il; Amir Daniel Gat, amirgat@technion.ac.il
Corresponding authors: Omri Ram, omri.ram@technion.ac.il; Amir Daniel Gat, amirgat@technion.ac.il

Abstract

Floating particles deform the liquid–gas interface, which may lead to capillary repulsion or attraction and aggregation of nearby particles (e.g. the Cheerios effect). Previous studies employed the superposition of capillary multipoles to model interfacial deformation for circular or ellipsoidal particles. However, the induced interfacial deformation depends on the shape of the particle and becomes more complex as the geometric complexity of the particle increases. This study presents a generalised solution for the liquid–gas interface near complex anisotropic particles using the domain perturbations approach. This method enables a closed-form solution for interfacial deformation near particles with an anisotropic shape, as well as the varying height of the pinned liquid–gas contact line. We verified the model via experiments performed with fixed particles held at the water level with shapes such as a circle, hexagon and square, which have either flat or sinusoidal pinned contact lines. Although in this study we concentrate on the equilibrium configuration of the liquid–gas interface in the vicinity of particles placed at fixed positions, our methodology paves the way to explore the interactions among multiple floating anisotropic particles and, thus, the role of particle geometry in self-assembly processes of floating particles.

Information

Type
JFM Papers
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 (https://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), 2025. Published by Cambridge University Press
Figure 0

Figure 1. (a) A 3D printed particle held at the liquid–gas interface, where the outer particle’s height is prescribed by $0.5\sin (8\theta )$ mm. (b) A sketch of the rotated particle and (c) a side view of a particle which is held fixed on a liquid, where the height of its boundary is prescribed by $f(\theta )$.

Figure 1

Figure 2. (a) The experimental set-up. The particles are held at the water–air interface, where the water is painted with a low concentration of Rhodamine 6G. A Nd:Yag 532 nm laser is used to excite the Rhodamine 6G, causing it to fluoresce at a wavelength of 550 nm. An optical set-up is used to form a thin laser sheet (${\sim}0.1$ mm) that illuminates a cross-section of the water’s interface across the particle. The images were acquired by a camera with a band-pass filter attached to its lens, with a cutoff wavelength of 550 nm. (b) A raw scan of the free surface without any model present. The figure also indicates the regions captured by each camera: red indicates the area recorded by camera 1, and blue corresponds to camera 2. The standard deviation of the free-surface measurements is 0.02 mm, although this variation is too small to be discernible in the figure. (c) A raw scan result obtained for a flat hexagon, which is placed 0.5 mm higher than the air–liquid interface. The displacement is magnified by a factor of 10 for visual representation. These results are obtained by a camera which is placed at an angle of 30$^\circ$ in relation to the central plane, marked in grey, and at an angle of 10$^\circ$ to the horizon. The far side of the model was captured by the second camera.

Figure 2

Figure 3. The 3D printed particles made of Tough 1500 V1, with a reference auxiliary diameter circle of 10 mm held at the liquid–gas interface. The outer particles’ height is prescribed by $0.5\sin (8\theta )$ mm for (a) circle, (b) triangle, (c) square, (e) pentagon, (f) hexagon and by $0.5\sin (4\theta )$ mm for (d) circle.

Figure 3

Figure 4. Analytical results for the liquid–gas interface for particles placed by held at the liquid–gas interface with $r_{\kern-1pt o}=20$ mm, where the outer particles’ height is prescribed by: (a) $0.5\sin (4\theta )$ mm and (b) $0.5\sin (8\theta )$ mm. (c) Maximum heights (at any $r$) of the liquid–gas interfaces versus $r$ obtained by solving the Young–Laplace equation with different boundary conditions, given by $h\vert _{r=20}=0.5\sin (n\theta )$ mm, where the uppermost and the lowermost curves correspond to $n=2$ and $n=42$, respectively.

Figure 4

Figure 5. The perturbation functions $\varepsilon D_r(\theta )$ relative to the unit circle for (a) a hexagon, (b) a pentagon, (c) a square and (d) a triangle. The sketches of the corresponding circumferences of the particles in our experiments and in the asymptotic solutions are shown in the insets.

Figure 5

Figure 6. The liquid–gas interface obtained by the asymptotic solution for (a) hexagonal, (b) pentagonal (c) square and (d) triangular particles, whose outer heights are prescribed by $0.5\sin (8\theta )$ mm and where $r_{\kern-1pt o}=5$ mm in all cases.

Figure 6

Figure 7. A comparison between experimental (upper half of the panels ac) and theoretical (lower half of the panels ac) results for the liquid–gas interface in three cases: (a) a hexagonal particle held at the liquid–gas interface at the height of 0.5 mm, (b) a circular particle with the outer height of $0.5\sin {(8\theta )}$ mm and (c) a hexagonal particle with the outer height of $0.1+0.5\sin {(8\theta )}$ mm. In all panels the radius of the inscribed circle is $r_{\kern-1pt o}=20$ mm and the height of the particles is relative to the liquid–gas interface sufficiently far from the particle. The colour bar refers to both cases (experimental and theoretical) for all panels.

Figure 7

Figure 8. An example of the convergence analysis relative to the number of terms in the asymptotic expansion for a square-shaped particle with an outer height of $0.5\sin {(8\theta )}$ mm using (a) only the leading-order term $H^{(0)}(R,\theta )$, (b) the sum of the leading- and the first-order terms $H^{(1)}(R,\theta )$, (c) the sum of the leading-, the first- and the second-order terms $H^{(2)}(R,\theta )$ and (d) a comparison between experiment (upper half of the panel) and $H^{(2)}(R,\theta )$ (lower half of the panel). In all panels the radius of the inscribed circle is $r_{\kern-1pt o}=20$ mm.

Figure 8

Figure 9. The error, Err defined in (A8), arising from the truncation of a finite number of modes in the Fourier series of the asymptotic solution $H(r,\theta )$ versus the number of modes, $K$. The full circles represent results obtained by simulation for the hexagon, pentagon, square and triangle, which correspond to the results shown in figure 6, and the curves, which were obtained by least square fitting to the simulation results, are to guide the eyes.

Figure 9

Figure 10. The liquid–gas interface shape for a square and a hexagonal-shaped particles, for which we calculated the inclination angles in table 1, where the points $P_1$, $P_2$ and $P_3$ are indicated.

Figure 10

Table 1. The inclination angle $\alpha$, calculated according to (D1), on 3 points $P_1$, $P_2$ and $P_3$ in three cases: case (i), case (ii), and case (iii) where in case (i) the centerline of the particle is the same as of the liquid-gas interface at infinity,  in case (ii) the centerline is 0.05 mm above the liquid-gas interface at infinity, and in case (iii) the centerline is 0.05 mm below the liquid-gas interface at infinity.

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