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Clustering and preferential concentration of finite-size particles in forced homogeneous-isotropic turbulence

Published online by Cambridge University Press:  11 January 2017

Markus Uhlmann*
Affiliation:
Institute for Hydromechanics, Karlsruhe Institute of Technology, 76131 Karlsruhe, Germany
Agathe Chouippe
Affiliation:
Institute for Hydromechanics, Karlsruhe Institute of Technology, 76131 Karlsruhe, Germany
*
†Email address for correspondence: markus.uhlmann@kit.edu

Abstract

We have performed interface-resolved direct numerical simulations of forced homogeneous-isotropic turbulence in a dilute suspension of spherical particles in the Reynolds number range $Re_{\unicode[STIX]{x1D706}}=115{-}140$ . The solid–fluid density ratio was set to $1.5$ , gravity was set to zero and two particle diameters were investigated corresponding to approximately $5$ and $11$ Kolmogorov lengths. Note that these particle sizes are clearly outside the range of validity of the point-particle approximation, as has been shown by Homann & Bec (J. Fluid Mech., vol. 651, 2010, pp. 81–91). At the present parameter points the global effect of the particles upon the fluid flow is weak. We observe that the dispersed phase exhibits clustering with moderate intensity. The tendency to cluster, which was quantified in terms of the standard deviation of Voronoï cell volumes, decreases with the particle diameter. We have analysed the relation between particle locations and the location of intense vortical flow structures. The results do not reveal any significant statistical correlation. Contrarily, we have detected a small but statistically significant preferential location of particles with respect to the ‘sticky points’ proposed by Goto & Vassilicos (Phys. Rev. Lett., vol. 100 (5), 2008, 054503), i.e. points where the fluid acceleration field is acting such as to increase the local particle concentration in one-way coupled point-particle models under Stokes drag. The presently found statistical correlation between the ‘sticky points’ and the particle locations further increases when focusing on regions with high local concentration. Our results suggest that small finite-size particles can be brought together along the expansive directions of the fluid acceleration field, as previously observed only for the simplest model for sub-Kolmogorov particles. We further discuss the effect of density ratio and collective particle motion upon the basic Eulerian and Lagrangian statistics.

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Papers
Copyright
© 2017 Cambridge University Press 
Figure 0

Table 1.The main physical parameters in the present simulations: length scale ratio $D/\unicode[STIX]{x1D702}$, Taylor-scale Reynolds number $Re_{\unicode[STIX]{x1D706}}=\unicode[STIX]{x1D706}u_{rms}/\unicode[STIX]{x1D708}$, global solid volume fraction $\unicode[STIX]{x1D6F7}_{s}$, density ratio $\unicode[STIX]{x1D70C}_{p}/\unicode[STIX]{x1D70C}_{f}$. Cases S5 and S11 are the corresponding single-phase simulations with the same turbulence-forcing parameters as D5 and D11, respectively, cf. table 2.

Figure 1

Table 2.Imposed parameters related to the turbulence-forcing scheme of Eswaran & Pope (1988) in the notation of Chouippe & Uhlmann (2015): the forcing cutoff wavenumber $\unicode[STIX]{x1D705}_{f}$, normalized by the smallest discrete wavenumber $\unicode[STIX]{x1D705}_{1}$; the characteristic time of the random forcing, $T_{L}$; the dissipation-rate parameter $\unicode[STIX]{x1D700}^{\ast }$.

Figure 2

Table 3.The principal numerical parameters pertaining to the present simulations: number of particles $N_{p}$, number of Eulerian grid nodes per linear dimension $N_{x}$, ratio between large-eddy length scale and box size $L/{\mathcal{L}}_{x}$, ratio between Kolmogorov scales and grid width $\unicode[STIX]{x1D702}/\unicode[STIX]{x0394}x$, ratio between box size and particle diameter ${\mathcal{L}}_{x}/D$, particle resolution $D/\unicode[STIX]{x0394}x$, observation time normalized with large-eddy time scale $T_{obs}/T$ and normalized with particle time scale $T_{obs}/\unicode[STIX]{x1D70F}_{p}$.

Figure 3

Figure 1.Time evolution of the terms in the equation for kinetic energy $E_{k}=\boldsymbol{u}\boldsymbol{\cdot }\boldsymbol{u}/2$, averaged over the computational domain: (a) case D5; (b) case D11. As shown by Chouippe & Uhlmann (2015) the evolution equation reads as follows: $0=-\text{d}\langle E_{k}\rangle _{\unicode[STIX]{x1D6FA}}/\text{d}t-\unicode[STIX]{x1D700}_{\unicode[STIX]{x1D6FA}}+\unicode[STIX]{x1D6F9}^{(t)}+\unicode[STIX]{x1D6F9}^{(p)}$, where $\langle \cdot \rangle _{\unicode[STIX]{x1D6FA}}$ indicates averaging over the spatial domain, $\unicode[STIX]{x1D700}_{\unicode[STIX]{x1D6FA}}$ is the box-averaged instantaneous dissipation rate (- - -, red), $\unicode[STIX]{x1D6F9}^{(t)}$ the power input due to turbulence forcing (——, black), and $\unicode[STIX]{x1D6F9}^{(p)}$ the two-way coupling term (——, red); the time-rate-of-change term is plotted in blue (——, blue).

Figure 4

Figure 2.Normalized difference between the variance of the fluid velocity and that of the particle velocity. The symbols correspond to: ♢, Homann & Bec (2010); ♦, Cisse (2015); ($\times$, red), density-matched particles (cases ‘N1’, ‘N2’) of Yeo et al. (2010); ($\times$, black), particles with density ratio $\unicode[STIX]{x1D70C}_{p}/\unicode[STIX]{x1D70C}_{f}=1.4$ (cases ‘S1’, ‘S2’) of Yeo et al. (2010); ●, present simulations; ○, case ‘A-G0’ from Chouippe & Uhlmann (2015). The dashed line (- - -) indicates a power law proportional to $(D/\unicode[STIX]{x1D702})^{2/3}$.

Figure 5

Figure 3.Normalized p.d.f. of the particle Reynolds number computed from the sphere-averaged relative velocity $\boldsymbol{u}_{pr}$ as defined in the text. Line styles correspond to: (, black), case D5; (, red), case D11. The blue dashed line indicates a gamma distribution with shape parameter $k=3$ which for a quantity $x$ with variance unity reads: $f(x)=(3^{3/2}/2)x^{2}\exp (-x\sqrt{3})$. Mean and standard deviations of the particle Reynolds number are listed next to the graph.

Figure 6

Figure 4.Normalized p.d.f.s of the linear particle acceleration. Samples corresponding to particles in contact with other particles have been eliminated. Line styles correspond to: (——, black), case D5; (——, red), case D11; (- - -, blue), fit of experimental data proposed by Qureshi et al. (2007).

Figure 7

Figure 5.Variance of the single-component particle acceleration normalized by the variance of fluid particles, plotted as function of the particle diameter. The present data are represented by the filled circular symbols (●); additionally, numerical values are listed next to the graph. The open circle (○) indicates the case ‘A-G0’ from Chouippe & Uhlmann (2015). The dark green triangles (▾) mark the experimental results of Voth et al. (2002) which were obtained in a von Kármán flow at different Reynolds numbers ($Re_{\unicode[STIX]{x1D706}}=140,\ldots ,970$). The orange triangles (▸) indicate the more recent measurements in the same flow, carried out at Reynolds numbers $Re_{\unicode[STIX]{x1D706}}=400,\ldots ,800$, as reported by Brown et al. (2009). The blue squares (▪) correspond to the wind-tunnel data of Qureshi et al. (2007) for neutrally buoyant particles at $Re_{\unicode[STIX]{x1D706}}=160$. The magenta triangles (▴) are experimental measurements in a von Kármán flow by Volk et al. (2011), performed at different Reynolds numbers ($Re_{\unicode[STIX]{x1D706}}=590,\ldots ,1050$). Red diamonds represent the simulation data of Homann & Bec (2010) (♢) and those of Cisse (2015) (♦). The numerical data for density-matched particles (cases ‘N1’, ‘N2’) of Yeo et al. (2010) are indicated by the symbol ($\times$) in red and their particles with density ratio $\unicode[STIX]{x1D70C}_{p}/\unicode[STIX]{x1D70C}_{f}=1.4$ (cases ‘S1’, ‘S2’) are shown as ($\times$) in black. The guiding lines are proportional to $(D/\unicode[STIX]{x1D702})^{-2/3}$ (- - -, black) and to $(D/\unicode[STIX]{x1D702})^{-4/3}$ (- - -, red).

Figure 8

Figure 6.(a) Lagrangian auto-correlation coefficient of one-component, linear particle acceleration, normalized with the large-eddy turnover time $T$. The correlations have been computed during collision-free intervals only. The inset shows the same data for smaller separation times $\unicode[STIX]{x1D70F}$, and normalized in Kolmogorov time units $\unicode[STIX]{x1D70F}_{\unicode[STIX]{x1D702}}$. Line styles correspond to: (——, black), case D5; (——, red), case D11, (b) The integral scale $\unicode[STIX]{x1D70F}_{int}$ of the auto-correlation (from integration up to the first zero crossing) shown in (a), plotted as a function of the particle size. The present data is indicated by solid circles (●); the black open circle (○) indicates the data of case ‘A-G0’ from Chouippe & Uhlmann (2015). The magenta triangles (▴) correspond to data from the von Kármán flow experiments of Volk et al. (2011); the red diamonds (♢) represent the simulation data of Homann & Bec (2010). The dashed line (- - -) indicates a linear increase $\unicode[STIX]{x1D70F}_{int}/\unicode[STIX]{x1D70F}_{\unicode[STIX]{x1D702}}=1+0.08(D/\unicode[STIX]{x1D702})$.

Figure 9

Figure 7.(a) Time evolution of the standard deviation of the normalized volume of the cells of the three-dimensional Voronoï tessellation with the particle centres as ‘sites’. Line styles correspond to: (, black), case D5; (, red), case D11, The dashed lines indicate the average value for a sequence of random distributions of non-overlapping spheres computed for the same number of particles and domain sizes as in the respective DNS. (b) The time average of the standard deviation of the Voronoï cell volumes (normalized by the corresponding value for a random particle arrangement), plotted as a function of the particle diameter (normalized by the Kolmogorov length scale). The DNS data are indicated by circular symbols (●, black, case D5; ●, red, case D11), with the error bars corresponding to the standard deviation in time. The error bars attached to the random data (open circles) indicate the standard deviation over the respective random sequence. Note that the red open circle has been shifted slightly in the horizontal direction for clarity.

Figure 10

Figure 8.(a) Normalized radial-distribution function $g(r)$ of particle positions in case D5 (——, black) and D11 (——, red) in the statistically stationary regime. (b) The same data as in (a), but showing the excess value $g(r)-1$ in double-logarithmic scaling. The blue dashed line (- - -) corresponds to a $-1$ power law.

Figure 11

Figure 9.P.d.f. of the Voronoï cell volumes, sampled over the entire statistically stationary interval in case D5 (——), as compared with the distribution obtained from a random Poisson process (- - -), sampled over a large ensemble. The cross-over points between the two curves are marked with solid circles (●).

Figure 12

Figure 10.(a) P.d.f. of the size distribution of particle clusters expressed in terms of the number of member cells per cluster. The black solid line (——) corresponds to case D5; the dashed line (- - -, black) shows the distribution for a corresponding random particle arrangement. (b) P.d.f. of the distribution of the volume of particle clusters. The dashed line (- - -, blue) corresponds to a $-16/9$ power-law.

Figure 13

Figure 11.The seven largest clusters in some snapshots of case D5, with the Voronoï cell faces coloured uniformly per cluster. The colour code is in descending order (the number of member cells is given in parenthesis): black (90), blue (80), red (77), magenta (76), green (64), cyan (59) and yellow (56). The particles inside those cells are coloured in black, while all remaining particles have been omitted from the figure. Graphs (a) and (b) show the same data from two different perspectives.

Figure 14

Figure 12.Snapshot of the flow field and the particle positions in cases (a) D5; (b) D11. Intense vortical structures are educed with the $q$-criterion of Hunt, Wray & Moin (1988), and locations with a value of $1.5$ times the standard deviation of $q$ are shown as blue coloured surfaces. Only a slice with thickness equal to one-eighth of the domain size (equivalent to approximately $90$ Kolmogorov units) is shown for clarity; in the other two directions the entire domain is shown.

Figure 15

Figure 13.The same data as in figure 12, but showing a close up with side length equal to $180\unicode[STIX]{x1D702}$ and a reduced depth of $45\unicode[STIX]{x1D702}$.

Figure 16

Figure 14.The p.d.f. of the volume of the vortical structures, educed with the criterion of Hunt et al. (1988) (using a threshold equal to $1.5$ times the standard deviation) and normalized in Kolmogorov length scales. Line styles correspond to: (, black) case D5; (, red) case D11; ——, single-phase data. The vertical lines indicate the particle volume of cases D5 and D11. Note that the different lower ends of the three curves correspond to the specific values of $\unicode[STIX]{x0394}x^{3}$ in each case.

Figure 17

Figure 15.P.d.f. of the distance from the particles to the nearest point on any vortical structure (as educed with the criterion of Hunt et al.1988). Note that the distance $d_{CS}^{(i)}$ (defined in the text) is measured from the particle surface. Line styles correspond to: , case D5; ——, black, case D5 and removing coherent structures with a volume inferior to $V_{p}$; ——, blue, distance from randomly chosen points to the coherent structures in case D5.

Figure 18

Figure 16.Instantaneous location of particles (red spheres) and the points of the fluid velocity field (grey dots) which satisfy the criteria of (3.1). The data are shown in a slice of thickness equal to $15\unicode[STIX]{x1D702}$ (direction into the page), the length in the other two directions being $380\unicode[STIX]{x1D702}$: (a) case D5; (b) case D11.

Figure 19

Figure 17.Radial-distribution function of ‘sticky points’ as defined in (3.1). The number density $n_{S}(r)$ is normalized with the global value $n_{SG}$. The lines correspond to: ——, red, case D11; ——, blue, single-phase flow.

Figure 20

Figure 18.Particle-conditioned, relative number density of ‘sticky points’ (as defined in (3.1)). The number density $n_{PS}(r)$ is normalized with the global value $n_{PSG}$. In (a) the distance is scaled with the Kolmogorov length scale $\unicode[STIX]{x1D702}$, in (b) it is scaled with the particle diameter $D$. Line styles: ——, black, case D5; ——, red, case D11.

Figure 21

Figure 19.(a) Comparison of the particle-conditioned radial-distribution function in case D5 according to different criteria: ——, black, criterion (3.1); , zero-acceleration points. (b) Particle-conditioned, relative number density of ‘sticky points’ (as in figure 18), showing the full set of samples versus only those samples corresponding to clustering particles (having Voronoï cell volumes smaller than the lower cross-over point in figure 9). Line styles: ——, black, case D5; ——, blue, only clustering particles of case D5.

Figure 22

Figure 20.P.d.f. of the largest eigenvalue $\unicode[STIX]{x1D706}_{1}$ of the symmetric part of the fluid acceleration gradient tensor, $\unicode[STIX]{x1D735}\boldsymbol{a}_{f}+(\unicode[STIX]{x1D735}\boldsymbol{a}_{f})^{\text{T}}$, in single-phase turbulence case S5.