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Velocity and spatial distribution of inertial particles in a turbulent channel flow

Published online by Cambridge University Press:  10 June 2019

Kee Onn Fong*
Affiliation:
Department of Aerospace Engineering and Mechanics, University of Minnesota, Minneapolis, MN 55455, USA St Anthony Falls Laboratory, University of Minnesota, Minneapolis, MN 55414, USA
Omid Amili
Affiliation:
Department of Aerospace Engineering and Mechanics, University of Minnesota, Minneapolis, MN 55455, USA
Filippo Coletti
Affiliation:
Department of Aerospace Engineering and Mechanics, University of Minnesota, Minneapolis, MN 55455, USA St Anthony Falls Laboratory, University of Minnesota, Minneapolis, MN 55414, USA
*
†Email address for correspondence: fongx065@umn.edu

Abstract

We present experimental observations of the velocity and spatial distribution of inertial particles dispersed in turbulent downward flow through a vertical channel at friction Reynolds numbers $\mathit{Re}_{\unicode[STIX]{x1D70F}}=235$ and 335. The working fluid is air laden with size-selected glass microspheres, having Stokes numbers $St=\mathit{O}(10)$ and $\mathit{O}(100)$ when based on the Kolmogorov and viscous time scales, respectively. Cases at solid volume fractions $\unicode[STIX]{x1D719}_{v}=3\times 10^{-6}$ and $5\times 10^{-5}$ are considered. In the more dilute regime, the particle concentration profile shows near-wall and centreline maxima compatible with a turbophoretic drift down the gradient of turbulence intensity; the particles travel at speed similar to that of the unladen flow except in the near-wall region; and their velocity fluctuations generally follow the unladen flow level over the channel core, exceeding it in the near-wall region. The denser regime presents substantial differences in all measured statistics: the near-wall concentration peak is much more pronounced, while the centreline maximum is absent; the mean particle velocity decreases over the logarithmic and buffer layers; and particle velocity fluctuations and deposition velocities are enhanced. An analysis of the spatial distributions of particle positions and velocities reveals different behaviours in the core and near-wall regions. In the channel core, dense clusters form which are somewhat elongated, tend to be preferentially aligned with the vertical/streamwise direction and travel faster than the less concentrated particles. In the near-wall region, the particles arrange in highly elongated streaks associated with negative streamwise velocity fluctuations, several channel heights in length and spaced by $\mathit{O}(100)$ wall units, supporting the view that these are coupled to fluid low-speed streaks typical of wall turbulence. The particle velocity fields contain a significant component of random uncorrelated motion, more prominent for higher $St$ and in the near-wall region.

Information

Type
JFM Papers
Copyright
© 2019 Cambridge University Press 
Figure 0

Table 1. A list of experimental studies addressing gas–solid wall-bounded flows. When not explicitly reported in the referenced papers, the parameters are calculated using information therein.

Figure 1

Figure 1. A schematic diagram of the particle–laden channel flow facility and its main elements.

Figure 2

Table 2. Fluid and particle parameters for the investigated cases. Parameter $\unicode[STIX]{x1D702}_{c}$ is calculated using the relation $\unicode[STIX]{x1D702}_{c}=\unicode[STIX]{x1D706}_{\unicode[STIX]{x1D708}}(\unicode[STIX]{x1D705}Re_{\unicode[STIX]{x1D70F}})^{1/4}$ (Pope 2000).

Figure 3

Table 3. Cases studied in this experiment and respective notation.

Figure 4

Figure 2. (a) Main imaging planes investigated in the present study. (b) Light intensity profile as measured by a photodiode to estimate the laser sheet thickness. The dashed lines mark the full width at half maximum.

Figure 5

Figure 3. The mean velocity profile shown in logarithmic scale for $Re_{\unicode[STIX]{x1D70F}}=235$ and 335. The dashed black line represents the expected fluid velocity profile in the viscous sublayer ($y^{+}<5$). The solid black line indicates the log-law slope ($K=0.41$, $B=5.2$, shifted up 1 unit in diagram for illustration) used to determine the friction Reynolds number from $y^{+}=30$ to 100.

Figure 6

Figure 4. Wall-normal profiles for the unladen flow at both considered Reynolds numbers, normalized in outer units: (a) mean velocity; (b) streamwise r.m.s. velocity fluctuation; (c) wall-normal r.m.s. velocity fluctuation; (d) Reynolds shear stress.

Figure 7

Figure 5. Mean particle concentration profiles normalized by the global concentration for (a) LoSt cases and (b) HiSt cases. Here and in the following plots, WP indicates data points from wall-parallel measurements, with the horizontal error bars indicating uncertainty on laser sheet position.

Figure 8

Figure 6. Profiles of mean streamwise particle velocity for (a,c) LoSt and (b,d) HiSt cases, normalized in outer units (a,b) and inner units (c,d). Unladen fluid profiles are plotted for comparison.

Figure 9

Figure 7. Profiles of mean wall-normal particle velocity for (a) LoSt and (b) HiSt cases. Unladen fluid profiles are plotted for comparison.

Figure 10

Figure 8. Profiles of r.m.s. streamwise particle velocity for (a) LoSt and (b) HiSt cases. Unladen fluid profiles are plotted for comparison.

Figure 11

Figure 9. Profiles of r.m.s. wall-normal particle velocity for (a) LoSt and (b) HiSt cases. Unladen fluid profiles are plotted for comparison.

Figure 12

Figure 10. Profiles of characteristic flux velocity $k^{+}$ based on fluxes towards and away from the wall, for (a) LoSt-LoVF and (b) LoSt-HiVF cases.

Figure 13

Figure 11. Profiles of particle Reynolds shear stress for (a) LoSt and (b) HiSt cases. Unladen fluid profiles are plotted for comparison.

Figure 14

Figure 12. Contribution of each quadrant of the ($u,v$) plane to the Reynolds shear stresses for (a) unladen fluid, and inertial particles for (b) the LoSt-LoVF case and (c) the LoSt-HiVF case.

Figure 15

Figure 13. Profile of r.m.s. spanwise particle velocity for LoSt-HiVF and HiSt-HiVF cases, obtained from the wall-parallel measurements expanded in § 3.2.

Figure 16

Figure 14. Profile of the skewness of the particle streamwise velocity fluctuations in the LoSt-LoVF and LoSt-HiVF cases. Unladen fluid profile is plotted for comparison. The vertical dashed lines demarcate the regions over which the particle–laden data are averaged.

Figure 17

Figure 15. Global and directional RDFs along the centreplane for (a) LoSt-HiVF and (b) HiSt-HiVF. The vertical dashed line indicates the laser sheet thickness.

Figure 18

Figure 16. Angular distribution functions along the centreplane for (a) LoSt-HiVF and (b) HiSt-HiVF.

Figure 19

Figure 17. Two-point correlation of streamwise velocity fluctuations with separations in streamwise and spanwise directions along the centreplane, for (a) LoSt-HiVF and (b) HiSt-HiVF. The vertical dashed line indicates the laser sheet thickness.

Figure 20

Figure 18. Polar map of streamwise velocity two-point correlation along the centreplane, for (a) LoSt-HiVF and (b) HiSt-HiVF.

Figure 21

Figure 19. (a) Global and directional RDFs and (b) ADF for the LoSt-HiVF case along the near-wall plane.

Figure 22

Figure 20. (a) Two-point correlation of streamwise velocity fluctuations with separations in the near-wall plane. (b) Spatial velocity correlation map for streamwise velocity fluctuations of inertial particles in the near-wall plane.

Figure 23

Figure 21. (a) Voronoi tessellation diagram in a sample centreplane realization, with (b) highlighted clusters (coherent clusters in cyan). (c) Probability distribution function of the Voronoi cell areas $A_{cell}$ along the centreplane (red circles), compared with a $\unicode[STIX]{x1D6E4}$ distribution (blue dashed line); the vertical dashed line indicates the threshold $A_{cell}^{\ast }$.

Figure 24

Figure 22. The p.d.f.s of the cluster areas for the LoSt-HiVF and HiSt-HiVF cases in the channel centreplane, normalized by (a) the Kolmogorov scale corresponding to the flow velocity and (b) the square of the channel half-height, $h^{2}$.

Figure 25

Figure 23. The p.d.f.s of (a) the SVD-based aspect ratio and (b) the angle between the primary axis and the vertical for the LoSt-HiVF and HiSt-HiVF cases.

Figure 26

Figure 24. The p.d.f.s of normalized in-cluster (red squares) and global (black circles) concentrations for (a) LoSt-HiVF and (b) HiSt-HiVF.

Figure 27

Figure 25. (a) The same instantaneous realization as in figure 21, with the Voronoi cell colour-coded by the local particle streamwise velocity. (b) Joint p.d.f. of streamwise velocity and concentration at the centreplane for the LoSt-HiVF case. The dashed lines indicate the velocity and concentration values averaged along the centreplane. The black contour line indicates the p.d.f. level at 0.005.

Figure 28

Figure 26. The p.d.f.s of normalized in-cluster (red squares) and global (black circles) velocities for (a) LoSt-HiVF and (b) HiSt-HiVF in the channel centreplane.

Figure 29

Figure 27. (a) The p.d.f. of the Voronoi cell areas $A_{cell}$ along the near-wall plane (red circles), compared with a $\unicode[STIX]{x1D6E4}$ distribution (blue dashed line). (b) The p.d.f. of particle concentration in square boxes of size $0.18h$ used to tessellate the near-wall plane (red circles) compared to a Poisson distribution (blue dashed line).

Figure 30

Figure 28. (a) Sample realization at the near-wall plane, tessellated by $0.18h\times 0.18h$ boxes and colour-coded by the mean local streamwise particle velocity within the boxes. (b) Joint p.d.f. of streamwise velocity and box-based concentration at the near-wall plane for the LoSt-HiVF case. The dashed lines indicate the velocity and concentration averaged along the near-wall plane. The black contour line indicates the p.d.f. level at 0.005.

Figure 31

Figure 29. Wall-normal profiles of mean concentration for recordings of different durations, using (a) standard acrylic and (b) electrostatic dissipative acrylic. Here $C_{0}=880~\text{particles}~\text{cm}^{-3}$, corresponding to $\unicode[STIX]{x1D719}_{v}=5\times 10^{-5}$ for both cases. Refer to table 2 for definitions on $y,h$.

Figure 32

Figure 30. Particle height and vertical velocity data used for determining the restitution coefficient for particle–wall collisions over five trials. Positive velocity indicates upward motion. Tracks for each trial are shown in markers of different shapes and colours.