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Particle clustering and dispersion in dense turbulent interfacial suspensions

Published online by Cambridge University Press:  20 June 2025

Seunghwan Shin*
Affiliation:
Department of Mechanical and Process Engineering, ETH Zurich, Zurich 8092, Switzerland
Laura Stricker
Affiliation:
Institute of Process Engineering, Otto von Guericke University, 39106 Magdeburg, Germany
Filippo Coletti
Affiliation:
Department of Mechanical and Process Engineering, ETH Zurich, Zurich 8092, Switzerland
*
Corresponding author: Seunghwan Shin, seshin@ethz.ch

Abstract

We investigate suspensions of non-Brownian, millimetric monodisperse spherical particles floating at quasi-two-dimensional fluid interfaces, from dilute to dense concentrations. Building upon the phase diagram in the capillary number ($Ca$) and areal fraction ($\phi$) constructed by Shin & Coletti (2024 J. Fluid Mech. 984, R7), we analyse the dynamics of both aggregation and dispersion. In the capillary-driven clustering regime ($Ca \lt 1$), strong inter-particle bonds yield large, fractal-like clusters that grow by hit-and-stick collisions. In the drag-driven break-up regime ($Ca \gt 1$, $\phi \lt 0.4$), turbulent fluctuations overcome capillarity and result in particles moving similarly to passive tracers and forming clusters by random adjacency. In the lubrication-driven clustering regime ($Ca \gt 1$, $\phi \gt 0.4$), the close inter-particle proximity amplifies lubrication forces and results in large, crystal-like clusters. Above a threshold concentration that depends on $Ca$, self-similar percolating clusters span the entire domain. The particle transport exhibits a classic ballistic-to-diffusive transition, with the long-time diffusivity hindered by the reduced fluctuating energy at high concentrations. Nearby particles separate at initially slow rates due to strong capillary attraction, and then follow a super-diffusive dispersion regime. In dense suspensions, the process is characterised by the time scale associated with inter-particle collisions and by the energy dissipation rate defined by the lubrication force between adjacent particles. Our results provide a framework for predicting particle aggregation in interfacial suspensions such as froth flotation and pollutant dispersion, and may inform the design of advanced materials through controlled colloidal self-assembly.

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

Table 1. Summary of the experimental parameters.

Figure 1

Figure 1. Choice of a searching radius. (a) Distance to the nearest neighbour $d_{NN}$ sorted in descending order. The dashed line represents the mean particle diameter (${d}_p$), and the dash-dot line indicates the cutoff distance used to identify clustered neighbours. (b) An example of cluster detection from the corresponding experiment at $Ca = 0.33$ and $\phi = 0.44$. Particles within the same cluster are indicated with the same colour.

Figure 2

Figure 2. (a) Range of Reynolds numbers $Re$ and $Re_{\alpha }$ for the SL (black) and DL (red) configurations in this study. (b) Normalised third-order longitudinal structure function, $\langle \delta u_L^3\rangle / u_{rms,f}^3$), and (c) energy spectrum, $\langle E(k) \rangle$, at varying levels of forcing for the DL configuration.

Figure 3

Figure 3. (a) Schematic of the three distinct clustering/break-up regimes within the $Ca-\phi$ phase space, adapted from Shin & Coletti (2024). (b) Examples of detected clusters from each regime. Particles within the same cluster are indicated with the same colour.

Figure 4

Figure 4. (a) Clustered particle fraction ($\chi _{cl}$) as a function of areal fraction ($\phi$) across different capillary numbers ($Ca$). (b) Normalised cluster size ($\langle 2R_g \rangle _w/{d}_p$) as a function of $\phi$ at various $Ca$ levels. In each case, the dotted line represents the clustering fractions from random configurations for the respective $\phi$ values, established through RSA up to $\phi = 0.54$.

Figure 5

Figure 5. Probability density functions (PDFs) of the cluster size, $R_g$, normalised by the exponential decay length, ($l_{exp }$): (a) RSA-generated random configurations at $\phi = 0.27$, 0.44 and 0.53. The corresponding values of $l_{exp }/{d}_p$ are 0.20, 0.33 and 0.87, respectively. (b) The PDFs at $\phi = 0.27$ for various experimental capillary numbers: $Ca= 0.16$ , 0.23, 0.29, 0.87, 1.22, 1.51, 1.82, 2.10, 2.49 and 2.69, with the corresponding values of $l_{exp }/{d}_p= 5.66$ , 4.16, 3.76, 0.41, 0.37, 0.33, 0.29, 0.32, 0.25 and 0.21, respectively. (c) The PDFs at $\phi =0.53$ for $Ca = 0.59$, 0.87, 1.22, 1.51, 1.82, 2.10, 2.49 and 2.69 with the corresponding values of $l_{exp }= 1.17$ , 1.00, 1.00, 0.95, 0.88, 0.83, 0.79 and 0.74. The black dashed line in each panel represents an exponential decay, $\exp (-R_g/l_{exp })$.

Figure 6

Figure 6. Snapshots with identified clusters at the same $Ca = 0.33$ but different areal fractions: (a) $\phi = 0.44$, and (b) $\phi = 0.53$. Particles within the same cluster are indicated with the same colour. (c) Fraction of frames $\chi _p$ where a system-spanning cluster is present as a function of $\phi$ at fixed $Ca = 0.33$. (d) Examples of cluster morphology for systems with $\phi \approx 0.44$ at different capillary numbers: $Ca = 0.29$, 0.59 and 1.82 (from left to right). At this $\phi$, $Ca \ll 1$ entails the formation of a percolating structure, while higher $Ca$ results in non-connected structures. (e) Value of $\chi _p$ in the $Ca-\phi$ space. Panels (a) and (b) correspond to the points inside the red solid rectangle, and panel (d) corresponds to cases inside the red dotted rectangle.

Figure 7

Figure 7. Examples of the Eulerian velocity autocorrelation for the DL configuration. The dashed line represents tracers ($Re=1047$), while the red line corresponds to a dense suspension of particles at the same level of forcing ($Ca=2.69$ and $\phi =0.62$), where they form a large, system-spanning cluster.

Figure 8

Figure 8. (a) Cluster size distributions for a particle area fraction $\phi \approx 0.44$ at different capillary numbers $Ca$. Here, $n_p$ is the number of particles within a cluster, characterising the cluster size and $f(n_p)$ is the areal number density of clusters of size $n_p$. Dashed lines denote experiments in the SL configuration, while solid lines are from the DL2 set-up. (b) Normalised form of the same data, where $n_{p,max}$ is the size of the largest cluster, $A_p = \pi {d}_p^{2}/4$ is the projected area of a particle and $\theta = 1$ is a trivial exponent from dimensional analysis. Two limiting values of the polydispersity exponents, $\xi =2.05$ (dash-dot) and $\xi =5/2$ (dotted), which correspond to the predicted Fisher’s exponent (Fisher 1967), are indicated.

Figure 9

Figure 9. Fractal dimension $d_{frac}$ obtained via the box-counting method. (a) An example of normalised box count as a function of box side length for a cluster (inset), (b) $d_{frac}$ mapped in the $Ca-\phi$ space and (c) $d_{frac}$ as a function of the mean cluster size. The red dotted line indicates the mean $d_{frac}$ from varying $\phi$ values obtained via RSA.

Figure 10

Figure 10. Hexatic order parameter ($\psi _6$) of the clustered particles. (a) The PDFs of $\psi _6$ at $\phi = 0.44$ but different $Ca$ values: 0.09 (red) and 2.69 (blue). The black dashed line represents values from RSA for comparison. (b) Value of $\langle \psi _6 \rangle$ mapped in the $Ca-\phi$ space. (c) Value of $\langle \psi _6 \rangle$ as a function of $\phi$ across varying $Ca$. The black dashed line represents values obtained from RSA.

Figure 11

Figure 11. (a) Temporal evolution of the cluster size $\langle R_g(t)/R_{g,0} \rangle$ and cluster anisotropy $\langle [s_2(t)/s_1(t)]/[s_{2,0}/s_{1,0}] \rangle$ for an example case with $Ca = 2.49$ and $\phi = 0.44$. (b) Contour map of the weighted average cluster lifetime $\langle \tau _{{cl}} \rangle _w$ normalised by the flow turnover time $L_F/u_{{rms},f}$ across the $Ca-\phi$ space.

Figure 12

Figure 12. An example of (a) the Lagrangian velocity autocorrelation function (VACF) and (b) the MSD of particles for the case $Ca = 0.87$ and $\phi = 0.27$. The blue dotted line and red dash-dot line represent the short-term ballistic and long-term diffusive predictions, respectively, based on an exponentially decaying VACF with characteristic time scale $t_{L,p}$. The time is normalised by $t_{L,p}$, and the MSD is normalised by $L_p^{2} = (u_{rms,p} t_{L,p})^{2}$.

Figure 13

Figure 13. Contour maps in the $Ca-\phi$ space of (a) the ratio of Lagrangian time scales $t_{L,p} / t_{L,f}$, (b) the ratio of particle to fluid kinetic energy $\langle E_{k,p} \rangle / \langle E_{k,f} \rangle$ and (c) the normalised particle turbulence diffusivity $K_p / K_f$.

Figure 14

Figure 14. Examples of the second-order velocity structure functions ($S_2$) of particles from different experiments: (a) $Ca = 0.16$ and $\phi = 0.14$, (b) $Ca = 1.82$ and $\phi = 0.27$ and (c) $Ca = 2.69$ and $\phi = 0.62$. In each panel, $S_2^L$ (black squares) and $S_2^T$ (red circles) are normalised by $u_{rms,p}^{2}$. The dashed and dash-dot lines represent $S_2^L$ and $S_2^T$ of tracers at the same level of forcing, respectively, normalised by $u_{rms,f}^{2}$.

Figure 15

Figure 15. (a) Relationship between the enstrophy dissipation rate divided by the kinematic viscosity ($\zeta / \nu$) and $u_{rms,f}^{2} / L_F^{4}$. Markers are obtained from PIV analysis of tracer experiments, and the red dotted line represents the estimation based on Taylor–Green vortices with a slope of $4\pi ^{4}$. (b) Examples of the MSS of tracers in the DL configuration at different levels of forcing, with an initial separation of 1.84 mm. The dashed and dash-dot lines indicate $t^{2}$ and $t^3$ scalings, respectively. (c) Compensated MSS, where the MSS is divided by $(t / t_\zeta )^3$, highlighting the $t^3$ scaling as a plateau.

Figure 16

Figure 16. Examples of the MSS of particle pairs with an initial separation of ${d}_p = 1.84$ mm: (a) $\phi = 0.27$, and (b) $\phi = 0.71$. The dashed line corresponds to the MSS of tracers from the most turbulent flow in the experiments. (c) The MSS curves for high $\phi = 0.62$ across varying $Ca$ values, with time normalised by the collision time scale $t_{col} = h / u_{rel}$ and MSS by $h^{2}$. The dotted line indicates the MSS prediction by (3.12). (d) The MSS curves at $Ca = 2.49$ across different areal fractions, with lines indicating the MSS predictions by (3.12) at $\phi = 0.09$, 0.27, 0.44 and 0.71 (dash-dot), respectively.