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Particle dynamics and dune formation in Rayleigh–Bénard convection: a particle-resolved simulation study

Published online by Cambridge University Press:  07 August 2025

Xianyang Chen*
Affiliation:
Department of Mechanical and Aerospace Engineering, University of Houston, Houston, TX 77204, USASchool of Aerospace Engineering and Applied Mechanics, Tongji University, Shanghai 200092, PR China
Rodolfo Ostilla-Mónico
Affiliation:
Departamento de Ingeniería Mecánica y Diseño Industrial, Escuela Superior de Ingeniería, Universidad de Cádiz, Puerto Real 11519, Spain
Daniel Floryan*
Affiliation:
Department of Mechanical and Aerospace Engineering, University of Houston, Houston, TX 77204, USA
Myoungkyu Lee
Affiliation:
Department of Mechanical and Aerospace Engineering, University of Houston, Houston, TX 77204, USA
Andrea Prosperetti
Affiliation:
Department of Mechanical and Aerospace Engineering, University of Houston, Houston, TX 77204, USAFaculty of Science and Technology, University of Twente, Enschede 7500 AE, The NetherlandsDepartment of Mechanical Engineering, Johns Hopkins University, Baltimore, MD 21218, USA
*
Corresponding authors: Xianyang Chen, tomchen95@tongji.edu.cn; Daniel Floryan, dfloryan@uh.edu
Corresponding authors: Xianyang Chen, tomchen95@tongji.edu.cn; Daniel Floryan, dfloryan@uh.edu

Abstract

This paper presents numerical results for Rayleigh–Bénard convection with suspended particles at Rayleigh numbers $Ra=10^7$ and $10^8$, and unit Prandtl number. Accounting for their finite size makes it possible to investigate in detail the mechanism by which the particles, which are 10 % heavier than the fluid, get resuspended after settling, thus maintaining a two-phase circulating flow. It is shown that an essential component of this mechanism is the formation of particle accumulations, or ‘dunes’, on the bottom of the Rayleigh–Bénard cell. Ascending plumes become localised on these dunes. Particles are dragged up the dune slopes, and when they reach the top, are entrained into the rising plumes. Direct resuspension of particles from the cell bottom, if it happens at all, is very rare. For $Ra=10^7$, aspect ratios (width/height) $\Gamma =1,2,4$ are considered. It is found that in these and in the other cases simulated, at steady state, a single dune evolves, the largest linear dimension of which is comparable to the cell size. A remarkable consequence is that even at the low volume fraction considered here, 3.27 %, the particles are able to structure the flow and to determine the size and position of the largest ascending plumes. Their effect on the Nusselt number, however, remains small. This and other results are explained on the basis of the ratio of the cell-bottom viscous boundary-layer thickness to the particle diameter.

Information

Type
JFM Papers
Copyright
© The Author(s), 2025. Published by Cambridge University Press
Figure 0

Table 1.The parameters used for the five simulations discussed in this paper: $N_x\times N_y \times N_z$ is the grid resolution used in each direction, and $N_p$ is the total number of finite-sized particles. In all the simulations, the Prandtl number is kept at $Pr=1$.

Figure 1

Figure 1.Snapshots of the configurations of sedimented particles for aspect ratios (a) $\Gamma =1$ at $t^*=50$, (b) $\Gamma =2$ at $t^*=70.1$ and (c) $\Gamma =4$ at $t^*=122.5$; colour indicates the particle height above the cell bottom. The times chosen are typical of configurations at steady state.

Figure 2

Figure 2.The PDF of the normalised particle height $z_c/{d}_p$ above the cell base at the moment when they are resuspended, where $z_c$ is the $z$ coordinate of the particle centre.

Figure 3

Figure 3.The number of sedimented particles $N_{p,sed}$, normalised by the total number of particles $N_p$, versus time (solid lines), for different aspect ratios in increasing order; the dotted lines are the normalised number of particles forming the biggest dune.

Figure 4

Figure 4.Sequence of snapshots documenting the evolution of the sedimented particles for $\Gamma =4$; colour indicates the particle height above the cell bottom.

Figure 5

Figure 5.Top-down view of the fluid vertical velocity on a horizontal plane $1.25{d}_p$ above the bottom wall at three instants of time for the $\Gamma =4$ simulation. The particles within the region between the plane and the bottom wall are also shown, coloured by their temperature.

Figure 6

Figure 6.Top-down view of the fluid vertical velocity, indicated by colour, on a horizontal plane $1.25{d}_p$ above the bottom wall at $t^*=5.3$ for $\Gamma =4$. Arrows indicate the horizontal velocity vectors for all the particles within the region between the horizontal plane and the bottom wall. The red, green and purple boxes indicate attraction, saddle and repulsion regions; see text.

Figure 7

Figure 7.(a) Streamlines near the bottom wall coloured by vertical velocity at $t^*=5.3$ for $\Gamma =4$, red and blue indicating upward and downward plumes, respectively. (b) The two-dimensional streamlines in the region of the horizontal plane contained in the pink box (which is $1.25{d}_p$ above the bottom wall) are plotted with a top-down view. The purple, red and green dots represent the stagnation points of the downward plumes, attraction points and saddle points, respectively. The red streamlines show the pathways connecting the saddle points and the attraction points, and correspond to the thin rising plumes.

Figure 8

Figure 8.Here, $\Delta N_{res}$ is the number of particles resuspended during one time unit $H/U_f$. The time evolution of this quantity, normalised by the number of settled particles $N_{p,sed}$, is shown here for, in descending order, $\Gamma =1,2,4$.

Figure 9

Figure 9.Temporal evolution of the number of particles resuspended during one time unit $H/U_f$, normalised by the number of settled particles $N_{p,sed}$, for $Ra=10^7$,with $H/{d}_p=20$, and $Ra=10^8$ with $H/{d}_p=43.2$.

Figure 10

Figure 10.Particle configuration of sedimented particles for $Ra=10^8$ and $\Gamma =2$ at $t^*=90.1$. Particles are coloured by their height above the cell base. Suspended particles are neglected in the plot.

Figure 11

Figure 11.Temporal evolution of the number of particles resuspended during one time unit $H/U_f$, normalised by the number of settled particles $N_{p,sed}$, for normal-sized particles with $H/{d}_p=20$, and smaller particles with $H/{d}_p=28.3$. Here, $\Gamma =1$ and $Ra=10^7$.

Figure 12

Figure 12.The number of sedimented particles normalised by the total number of particles, for smaller and normal-sized particles for $\Gamma =1$.

Figure 13

Figure 13.Number of suspended particles settling during one time unit $H/U_f$ normalised by the number of suspended particles versus time for aspect ratios $\Gamma =2,4$. The vertical red dash-dotted line at $t^* = 45$ indicates the time at which the two elongated dunes visible at time $U_ft/H=34.0$ in figure 4(c) begin to merge into a single dune spanning the diagonal of the domain for $\Gamma =4$.

Figure 14

Figure 14.$(a)$ Warm particles with $(T_p-T_0)/(T_h-T_c)\gt 0.125$ at $t^*=30.13$. $(b)$ Streamlines coloured by the vertical velocity. $(c)$ Mid-height vertical velocity, time-averaged over $23.8 \leqslant t^* \leqslant 36.5$. $(d)$ Warm particles with $(T_p-T_0)/(T_h-T_c)\gt 0.125$ at $t^*=116.2$. $(e)$ Streamlines coloured by the vertical velocity. $(f)$ Mid-height vertical velocity, time-averaged over $109.9 \leqslant t^* \leqslant 122.5$. Here, $\Gamma =4$.

Figure 15

Figure 15.$(a)$ Warm particles with $(T_p-T_0)/(T_h-T_c)\gt 0.125$ at $t^*=75.2$. $(b)$ Streamlines coloured by the vertical velocity, time-averaged over $68.9 \leqslant t^* \leqslant 81.5$. $(c)$ Time-averaged mid-height vertical velocity. Here, $\Gamma =2$.

Figure 16

Figure 16.Time evolution of the correlation coefficient between the mid-height vertical velocity field $u_{z,m}$ and the temperature field $T_b$ on a horizontal plane near $1.25{d}_p$ above the cell bottom, denoted as $(u_{z,m},T_{b})$, for $\Gamma = 2,4$. The red dash-dotted line at $t^* = 45$ indicates when the two elongated dunes merge into a single dune spanning the diagonal of the domain for $\Gamma =4$.

Figure 17

Figure 17.(a) The Nusselt number $Nu$ and (b) the Reynolds number $Re$, versus aspect ratio, both with and without particles. The single-phase results are shown in black. Red and blue lines represent particulate flows with $Ra=10^7$ and $H/{d}_p=20.0$, and $Ra=10^7$ and $H/{d}_p=28.3$, respectively. In (b), solid lines with triangles represent the vertical Reynolds number, and dash-dotted lines with diamonds represent the horizontal Reynolds number.

Supplementary material: File

Chen et al. supplementary movie 1

The right frame displays the 3D particle configuration for the case with Ra=107, Pr=1 and Γ=4, where only warm particles ((Tp-T0)/(Th-Tc)≥ 0.0625) are shown and color-coded according to their temperatures. Red represents hotter particles, while blue indicates relatively cooler ones. Note that the apparent disappearance of particles near the top wall occurs because the particles are discarded as long as their temperatures drop below the threshold when they approach the top wall. The left frame illustrates the vertical velocity contour on a horizontal plane located 1.25dp above the bottom plate, along with particles sit between this plane and the bottom wall, corresponding to the same case as depicted in the right frame. In the contour, yellow and purple denote ascending and descending plumes, respectively. Meanwhile, the particles are colored based on their temperatures, with yellow representing hot particles and blue representing cooler ones.
Download Chen et al. supplementary movie 1(File)
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