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Experimental study of inertial particles clustering and settling in homogeneous turbulence

Published online by Cambridge University Press:  14 February 2019

Alec J. Petersen*
Affiliation:
Department of Aerospace Engineering and Mechanics, University of Minnesota, Minneapolis, MN 55414, USASt. Anthony Falls Laboratory, University of Minnesota, Minneapolis, MN 55414, USA
Lucia Baker
Affiliation:
Department of Aerospace Engineering and Mechanics, University of Minnesota, Minneapolis, MN 55414, USASt. Anthony Falls Laboratory, University of Minnesota, Minneapolis, MN 55414, USA
Filippo Coletti
Affiliation:
Department of Aerospace Engineering and Mechanics, University of Minnesota, Minneapolis, MN 55414, USASt. Anthony Falls Laboratory, University of Minnesota, Minneapolis, MN 55414, USA
*
†Email address for correspondence: pet00105@umn.edu

Abstract

We study experimentally the spatial distribution, settling and interaction of sub-Kolmogorov inertial particles with homogeneous turbulence. Utilizing a zero-mean-flow air turbulence chamber, we drop size-selected solid particles and study their dynamics with particle imaging and tracking velocimetry at multiple resolutions. The carrier flow is simultaneously measured by particle image velocimetry of suspended tracers, allowing the characterization of the interplay between both the dispersed and continuous phases. The turbulence Reynolds number based on the Taylor microscale ranges from $Re_{\unicode[STIX]{x1D706}}\approx 200{-}500$, while the particle Stokes number based on the Kolmogorov scale varies between $St_{\unicode[STIX]{x1D702}}=O(1)$ and $O(10)$. Clustering is confirmed to be most intense for $St_{\unicode[STIX]{x1D702}}\approx 1$, but it extends over larger scales for heavier particles. Individual clusters form a hierarchy of self-similar, fractal-like objects, preferentially aligned with gravity and with sizes that can reach the integral scale of the turbulence. Remarkably, the settling velocity of $St_{\unicode[STIX]{x1D702}}\approx 1$ particles can be several times larger than the still-air terminal velocity, and the clusters can fall even faster. This is caused by downward fluid fluctuations preferentially sweeping the particles, and we propose that this mechanism is influenced by both large and small scales of the turbulence. The particle–fluid slip velocities show large variance, and both the instantaneous particle Reynolds number and drag coefficient can greatly differ from their nominal values. Finally, for sufficient loadings, the particles generally augment the small-scale fluid velocity fluctuations, which however may account for a limited fraction of the turbulent kinetic energy.

Information

Type
JFM Papers
Copyright
© Cambridge University Press 2019. This is a work of the U.S. Government and is not subject to copyright protection in the United States. 
Figure 0

Table 1.Unladen turbulence statistics for the configurations in this study. The r.m.s. velocity $u^{\prime }$ and the longitudinal integral scale $L$ are based on a weighted average between the $x$ and $z$ directions. The Kolmogorov length scale $\unicode[STIX]{x1D702}=(\unicode[STIX]{x1D708}^{3}/\unicode[STIX]{x1D700})^{1/4}$ and time scale $\unicode[STIX]{x1D70F}_{\unicode[STIX]{x1D702}}=(\unicode[STIX]{x1D708}/\unicode[STIX]{x1D700})^{1/2}$ are based on estimates of the dissipation rate $\unicode[STIX]{x1D700}$ from the second-order transverse structure functions. For further details see Carter et al. (2016).

Figure 1

Table 2.Particle properties. The diameters $d_{p}$ are listed in mean $\pm$ standard deviation.

Figure 2

Table 3.Imaging parameters obtained with the CCD camera (2048 by 2048 pixels, $7.4~\unicode[STIX]{x03BC}\text{m}$ pixel size) when mounting the different lenses. The large FOV with the 50 mm lens is not used for PIV.

Figure 3

Figure 1.Image processing procedure for PIV/PTV measurements of tracer and particle motion: (a) raw image, (b) inset of raw image, (c) particle-only image, (d) tracer-only image, (e) resulting fluctuating fluid and particle velocity vectors.

Figure 4

Figure 2.Particle counts for example FOVs.

Figure 5

Figure 3.(a) Example Voronoï tessellation with connected sets of Voronoï cells below the area threshold coloured. (b) Example Voronoï area PDF shows clear departure from random Poisson distribution indicating the presence of clusters and voids for a case with $St_{\unicode[STIX]{x1D702}}=3.2$. (c) All PDFs of log($A$), centred at the mean and normalized by the standard deviation. The black dotted line shows a normal distribution with variance $=$ 1. (d) PDF of a sample case, with (purple circles) and without (black dashes) the neighbouring cell condition. (e) Scatter plot of cluster perimeter and square root of its area (same case as in d).

Figure 6

Table 4.Main experimental parameters for all considered cases, ordered in decreasing particle Stokers number $St_{\unicode[STIX]{x1D702}}$.

Figure 7

Figure 4.(a) Example RDFs where symbols represent the calculated RDFs and dashed lines their fits according to (3.2). Panels (b,c) show the fitted values versus $St_{\unicode[STIX]{x1D702}}$, and (d) shows the value of the correlation dimension.

Figure 8

Figure 5.(a) Example RDFs where symbols represent the calculated RDFs and dashed lines their fits according to (3.3). Panels (b–d) show the fitted coefficients versus $St_{\unicode[STIX]{x1D702}}$.

Figure 9

Figure 6.Two qualifications of clustering intensity using the Voronoï tessellation method: (a) $\unicode[STIX]{x1D70E}_{A}/\unicode[STIX]{x1D70E}_{RPP}$ representing departure from a random particle distribution versus Stokes number. (b) Fraction of inertial particles belonging to coherent clusters as a function of normalized $\unicode[STIX]{x1D70E}_{A}/\unicode[STIX]{x1D70E}_{RPP}$.

Figure 10

Figure 7.Example clusters for the cases $St_{\unicode[STIX]{x1D702}}=1.6$ and 4.6 imaged in the large FOV, highlighting the wide variety of sizes and shapes.

Figure 11

Figure 8.PDFs of cluster area normalized by $\unicode[STIX]{x1D702}$ and separated by FOV size. Largest FOV ($30\times 30~\text{cm}^{2}$) is shown in (a), medium field ($14.5\times 14.5~\text{cm}^{2}$) in (b) and smallest field in (c) ($4.5\times 4.5~\text{cm}^{2}$).

Figure 12

Figure 9.PDFs of cluster area for experiments with $St_{\unicode[STIX]{x1D702}}$ between 1 and 2.5 ($30~\unicode[STIX]{x03BC}\text{m}$ glass spheres) in the medium FOV showing how increasing volume fraction shifts PDFs to smaller scales.

Figure 13

Figure 10.Mean cluster area versus particle inertia. Marker size is proportional to $Re_{\unicode[STIX]{x1D706}}$ of the underlying turbulent flow.

Figure 14

Figure 11.$N_{B}(r)$ for three cases with $St_{\unicode[STIX]{x1D702}}=4.6$ in (a), 3.6 in (b) and 2.0 in (c), normalized by the respective maximum. The box-counting dimension of 1.6 is consistent for all cases.

Figure 15

Figure 12.(a) A single coherent cluster, with primary and secondary axes as computed through SVD. The length of each arrow is proportional to the corresponding singular value. (b) PDFs of the aspect ratios of clusters for each case.

Figure 16

Figure 13.(a) PDFs of the cosine of the angle between clusters’ primary axis and the vertical. (b) Joint PDF of angle from vertical and size of cluster.

Figure 17

Figure 14.(a,b) Scatter plots of cluster area (normalized by the Kolmogorov scale) versus the number of particles in each cluster (normalized by the total number of particles in the domain) for two sample cases. (c) Average particle concentration in the clusters, normalized by the global concentration, plotted versus $St_{\unicode[STIX]{x1D702}}$ and coloured by overall solid-volume fraction.

Figure 18

Figure 15.(a) Measured settling velocity normalized by the still-fluid Stokes value versus $St_{\unicode[STIX]{x1D702}}$ and coloured by solid-volume fraction. (b) Measured settling velocity variation from the still-fluid Stokes value normalized by the fluid r.m.s. fluctuations.

Figure 19

Figure 16.(a) Settling increase plotted as a function of both $St_{\unicode[STIX]{x1D702}}$ and $Sv_{\unicode[STIX]{x1D702}}$. (b) Settling increase as a function of the mixed scale, $St_{\unicode[STIX]{x1D702}}Sv_{L}$.

Figure 20

Figure 17.Average settling velocity of all clusters as a function of cluster size. Error bars indicate $\pm$ the standard deviation.

Figure 21

Figure 18.Normalized vertical particle velocity conditioned on the local particle concentration.

Figure 22

Figure 19.Fraction of particles in rotation-dominated regions. Black circles represent all particles in the field, while the purple diamonds represent only particles in coherent clusters.

Figure 23

Figure 20.Example case of the relative particle concentration conditioned on the vertical fluid velocity (normalized by the still-air settling velocity.) Black circles indicate the full particle set, while purple diamonds represent only particles in clusters.

Figure 24

Figure 21.Vertical fluid velocity at particle location, normalized by the fluid r.m.s. velocity, plotted versus particle Stokes number.

Figure 25

Figure 22.Prediction of settling velocity based on (5.1) normalized by the measured settling velocities, versus particle Stokes number.

Figure 26

Figure 23.Ratio of vertical particle to fluid r.m.s. velocity versus ratio of the same horizontal velocities.

Figure 27

Figure 24.Probability density functions of slip velocity magnitude normalized by fluid r.m.s. velocity (a), and vertical slip velocity (b) normalized by the still-fluid settling. (c,d) Plots of horizontal and vertical r.m.s. particle slip velocity, respectively, normalized by the fluid r.m.s. fluctuations along the corresponding direction.

Figure 28

Figure 25.PDFs of instantaneous particle Reynolds number. Vertical lines represent average Reynolds particle number based on the Stokes still-fluid settling velocity for each respective grouping of experiments. Panel (b) shows the ratios between drag coefficients (5.2) and (5.3), showing reduced drag when the ‘effective drag’ model is used.

Figure 29

Figure 26.PDF of the cosine of the angle between the particle velocity and the fluid velocity at the particle location (a). (b) Three example cases showing the probability distribution of the slip velocity orientation and magnitude.

Figure 30

Figure 27.Horizontal (a,b,d) and vertical (c,e) longitudinal structure functions for laden (colour coded by volume fraction) and unladen (black) multiphase flows. The shaded regions represent 95 % bootstrap confidence bounds.