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Investigating the parametric dependence of the impact of two-way coupling on inertial particle settling in turbulence

Published online by Cambridge University Press:  16 May 2024

Soumak Bhattacharjee
Affiliation:
Department of Civil and Environmental Engineering, Duke University, Durham, NC 27708, USA
Josin Tom
Affiliation:
Department of Civil and Environmental Engineering, Duke University, Durham, NC 27708, USA
Maurizio Carbone
Affiliation:
Theoretical Physics I, University of Bayreuth, Universitätsstrasse 30, 95447 Bayreuth, GermanyMax Planck Institute for Dynamics and Self-Organization, Am Faßberg 17, 37077 Göttingen, Germany
Andrew D. Bragg*
Affiliation:
Department of Civil and Environmental Engineering, Duke University, Durham, NC 27708, USA
*
†Email address for correspondence: andrew.bragg@duke.edu

Abstract

Tom et al. (J. Fluid Mech., vol. 947, 2022, p. A7) investigated the impact of two-way coupling (2WC) on particle settling velocities in turbulence. For the limited parameter choices explored, it was found that (i) 2WC substantially enhances particle settling compared with the one-way coupled case, even at low mass loading $\varPhi _m$ and (ii) preferential sweeping remains the mechanism responsible for the particles settling faster than the Stokes settling velocity in 2WC flows. However, significant alterations to the flow structure that can occur at higher mass loadings mean that the conclusions from Tom et al. (J. Fluid Mech., vol. 947, 2022, p. A7) may not generalise. Indeed, even under very low mass loadings, the influence of 2WC on particle settling might persist, challenging the conventional assumption. We therefore explore a much broader portion of the parameter space, with simulations covering cases where the impact of 2WC on the global fluid statistics ranges from negligible to strong. We find that, even for $\varPhi _m=7.5\times 10^{-3}$, 2WC can noticeably increase the settling for some choices of the Stokes and Froude numbers. When $\varPhi _m$ is large enough for the global fluid statistics to be strongly affected, we show that preferential sweeping continues to be the mechanism that enhances particle settling rates. Finally, we compare our results with previous numerical and experimental studies. While in some cases there is reasonable agreement, discrepancies exist even between different numerical studies and between different experiments. Future studies must seek to understand this before the discrepancies between numerical and experimental results can be adequately addressed.

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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 (http://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), 2024. Published by Cambridge University Press.
Figure 0

Table 1.Flow parameters in DNS for the unladen flow. Here, $Re_{\lambda } \equiv u'\lambda /\nu = 2k/\sqrt {5/3\nu \langle \epsilon \rangle }$ is the Taylor microscale Reynolds number, $\lambda$ is the Taylor microscale, $\mathcal {L}$ is the domain length, $N$ is the number of grid points in each direction, $\nu$ is the fluid kinematic viscosity, $\langle \epsilon \rangle$ is the mean turbulent kinetic energy dissipation rate, $L$ is the integral length scale, $\eta \equiv (\nu ^{3}/\langle \epsilon \rangle )^{1/4}$ is the Kolmogorov length scale, $u' \equiv \sqrt {2\mathcal {K}/3}$ is the r.m.s. of the fluctuating fluid velocity, $\mathcal {K}$ is the turbulent kinetic energy, $u_{\eta }$ is the Kolmogorov velocity scale, $\tau _L \equiv L/u'$ is the large-eddy turnover time, $\tau _{\eta }$ is the Kolmogorov time scale, $k_{max} = \sqrt {2N/3}$ is the maximum resolved wavenumber and $dt$ is the time step. The small-scale resolution, $k_{max}\eta$ and the total flow kinetic energy measured by $u'$ are approximately constant between the different simulations. These flow statistics are constructed by averaging over the spatial domain and averaging over a time period of $10\tau _L$.

Figure 1

Figure 1.Plot of the Eulerian PDF $\mathcal {P}(\mathcal {Q})$ for 2WC simulations with (a) fixed $St_4=1$, $Fr=0.3$ and varying $\varPhi$, and (b) fixed $\varPhi _4=7\times 10^{-5}$ and $Fr=0.3$ and varying $St$. Black solid lines show $\mathcal {P}(\mathcal {Q})$ for the 1WC simulations, which is the same as for the unladen flow (see text). Here, $\mathcal {Q}$ is normalised by $\epsilon /(2\nu )$ from the unladen flow.

Figure 2

Figure 2.Turbulent kinetic energy spectrum $E(k)$ vs the wavenumber $k$ for 2WC simulations with $St=1$ particles, for different volume fractions for fixed $Fr$ numbers; (a) $Fr=0.3$, (c) $Fr=3.0$. Ratio of the turbulent kinetic energy spectrum $E(k)$ to the spectrum of the vertical component of the turbulent kinetic energy $E_{33}(k)$ vs the wavenumber $k$ for 2WC simulations with $St=1$ particles for different volume fractions for fixed $Fr$ numbers; (b) $Fr=0.3$, (d) $Fr=3.0$.

Figure 3

Figure 3.Plots showing the turbulent kinetic energy (TKE) dissipation rate $\epsilon$, normalised by corresponding values from the 1WC runs, for 1WC and 2WC simulations for different volume fractions $\varPhi$, and for particles with different $St$. Lines in blue, red, green, yellow and purple correspond to particles with $St_1=0.3$, $St_2=0.5$, $St_3=0.7$, $St_4=1$ and $St_5=2$, respectively. Panels (a–c) correspond to simulations with $Fr=0.3$, $Fr=1$ and $Fr=3$, respectively.

Figure 4

Figure 4.Normalised settling velocity enhancement for the 1WC (dashed) and 2WC (solid) cases for $\varPhi =1.5\times 10^{-6}$ (a) and $\varPhi =7\times 10^{-5}$ (b), vs $St$. See figure 14 for trends corresponding to other volume fractions.

Figure 5

Figure 5.Normalised settling velocity enhancement vs volume fraction $\varPhi$, for the 1WC (dashed) and 2WC (solid) cases, for fixed $Fr$: (a) $Fr=0.3$, (b) $Fr=3$. See figure 15 for simulations with $Fr=1$.

Figure 6

Figure 6.Results for the Lagrangian PDF $\mathscr {P}(\mathcal {Q})$ in 1WC and 2WC simulations, along particle trajectories (a) for ${St}_1=1$, $Fr=0.3$ showing $\varPhi$ dependence, and (b) at a constant volume fraction $\varPhi _4=7\times 10^{-5}$, and $Fr=0.3$ showing $St$ dependence. Dashed and solid lines mark the trends for 1WC and 2WC simulations, respectively. The black, solid line corresponds to Eulerian PDF of $\mathcal {P}(\mathcal {Q})$ of the unladen flow. Here, $\mathcal {Q}$ is normalised by $\epsilon /(2\nu )$ from the unladen flow.

Figure 7

Figure 7.Plots of $\varphi$ (4.2) vs volume fraction $\varPhi$ for simulations with (a) $Fr=0.3$, (b) $Fr=1$ and (c) $Fr=3$. When $\varphi > 1$, this indicates that the inertial particles exhibit a preference to move in strain-dominated regions of the flow.

Figure 8

Figure 8.Plots of $A$ (4.3), in blue, and $B$ (4.4), in red, for 1WC (dashed) and 2WC (solid) flows for $St=1$ particles as a function of $\varPhi$ with (a) $Fr=0.3$, (b) $Fr=1$ and (c) $Fr=3$. Plots of $A$ (blue) and $B$ (red) at a fixed volume fraction $\varPhi _4=7\times 10^{-5}$ for 1WC (dashed) and 2WC (solid) simulations, with (e) $Fr=0.3$, (f) $Fr=1$, (g) $Fr=3$ showing the $St$ dependence. See figures 18 and 19 for $\varPhi$-, $St$-dependence for other simulations.

Figure 9

Figure 9.Plots of the ratio $B/A$ (4.3), (4.4) for 2WC flows vs $\varPhi$ with (a) $Fr=0.3$, (b) $Fr=1$ and (c) $Fr=3$.

Figure 10

Table 2.Details of previous experiments (denoted by E) and numerical simulations (denoted by S). Here, ${\rm AL}\,{\rm E1}$ and ${\rm AL}\,{\rm E2}$ denote the measurements of Aliseda et al. (2002) in isotropic, decaying grid turbulence (squares and circles, respectively, in figure 14(a) of ${\rm AL}$); ${\rm YS}$ indicates the measurements of Yang & Shy (2005) in stationary, homogeneous, isotropic turbulence generated by a pair of counter-rotating fans (refer to figure 16(a) for data); ${\rm BM}\,{\rm S1}\unicode{x2013}{\rm S3}$ denote the results of DNS from Bosse et al. (2006) using a stochastic forcing scheme and a computational particle approach (in the Eulerian–Lagrangian framework); see table II (${\rm BM}\,{\rm S1}$) and table V, figure 14 (diamond for ${\rm BM}\,{\rm S2}$ and triangle for ${\rm BM}\,{\rm S3}$); ${\rm GW}$ indicates the studies presented in Good et al. (2014): ${\rm GW}\,{\rm E1}$ denotes the experiment of particle settling in soccer-ball apparatus with 32 loudspeaker jets (labelled E1 in ${\rm GW}$ table 1), whereas ${\rm GW}\,{\rm S1}$ marks the results obtained from DNS using a deterministic forcing scheme (simulation labelled S2 in ${\rm GW}$ table 1 interpolated to the same $Fr$ as ${\rm GW}\,{\rm E1}$); see figure 3(a) in ${\rm GW}$ for data; ${\rm MD}$ refers to the numerical studies presented in Monchaux & Dejoan (2017) using DNS. The simulations ${\rm S1}$ and ${\rm S2}$ correspond to simulations, for Rouse number $R=\tau _pg/u^\prime =0.25$, with $St=0.36$ and $St=1$, respectively; see table II for additional details; ${\rm BC}\,{\rm E1},2$ indicate the results from the experiments in a turbulence chamber (Berk & Coletti 2021) with facing jet arrays at two different $Re_\lambda$ (see table 2 and figure 8 in ${\rm BC}$ for data); ${\rm HC}\,{\rm E1},2$ denote the experiments in a similar set-up as ${\rm BC}$, but with the jet arrays activated in a randomised sequence (Hassaini & Coletti 2022); refer to table 1 and figure 3 in ${\rm HC}$ for data.

Figure 11

Figure 10.Ratio of the (a) horizontal to vertical turbulence intensities $u^\prime _1/u^\prime _3$, $u^\prime _2/u^\prime _3$ and (b) horizontal turbulence intensities for 2WC in unladen simulations $u^\prime _1/u^\prime _{1,\varPhi =0}$, $u^\prime _2/u^\prime _{2,\varPhi =0}$ for DNS (coloured symbols) and data from previous work (in black). Experimental results from Hassaini & Coletti (2022) figure 3(a) are shown in black circles ($St=0.3$) and black diamonds ($St=2.6$), denoted by ${\rm HC}\,{\rm E1}$ and ${\rm HC}\,{\rm E2}$, respectively. Results from Bosse et al. (2006) table II, denoted by ${\rm BM}\,{\rm S1}$, are given by black squares. Solid and dashed lines for the current and previous numerical results simply correspond to data along to two different horizontal directions. Details of the previous works are given in table 2.

Figure 12

Figure 11.Comparison of the TKE dissipation rate (normalised by 1WC values) for the current simulations (red circles) and Bosse et al. (2006) table II (black diamonds), denoted by ${\rm BM}\,{\rm S1}$, vs volume fraction $\varPhi$.

Figure 13

Figure 12.Comparison of the current DNS results for normalised Lagrangian PDFs $\mathscr {P}(\mathcal {Q})$ (symbols) in 1WC and 2WC simulations and the experiments of Berk & Coletti (2021), hereafter ${\rm BC}$. Black solid line corresponding to the 1WC simulations, which is the same as for the unladen flow, and the black dashed line corresponds to the red line from figure 8 of ${\rm BC}$ (corresponding to the unladen fluid statistics), are shown for reference. Black circles and diamonds correspond to measurements along Lagrangian particle trajectories in ${\rm BC}\,{\rm E1}$ and ${\rm BC}\,{\rm E2}$, respectively, for $\varPhi \approx 10^{-7}$. See table 2 for the details of these experiments. Here, $\sigma _{\mathcal {Q}}$ denotes the standard deviation of $Q$.

Figure 14

Figure 13.Comparison of 1WC (dashed lines) and 2WC (solid lines) DNS results for settling velocity enhancement (normalised by $u^{\prime }$), as a function of (a,b) $St$ for different $\varPhi$ and $Fr$, (c) $\varPhi$ for a constant $St$ and $Fr$, with previous studies. See table 2 for details of experiments and numerical simulations. Experimental and numerical results from previous studies are shown by dotted lines and open symbols, respectively.

Figure 15

Table 3.Flow parameters in DNS of 2WC simulations for different volume fraction Φ, Stokes number St and Froude number Fr. The Stokes number and Froude number are defined with respect to the unladen DNS statistics.

Figure 16

Figure 14.Normalised settling velocity enhancement for the 1WC (dashed) and 2WC (solid) cases for (a) $\varPhi _2=7\times 10^{-6}$, (b) $\varPhi _3=1.5\times 10^{-5}$ and (c) $\varPhi _5=1.5\times 10^{-4}$, vs $St$. Figure 4 in the text shows the results for other volume fractions.

Figure 17

Figure 15.Normalised settling velocity enhancement vs volume fraction $\varPhi$, for the 1WC (dashed) and 2WC (solid) cases for $Fr=1$. Figure 5 in the text shows the results for $Fr=0.3$ and $Fr=3$.

Figure 18

Figure 16.Plots showing $\mathbb {P}(\mathcal {Q}>0)-\mathbb {P}(\mathcal {Q}<0)$ vs volume fraction $\varPhi$ for particles with different Stokes number $St$, for simulations with (a) $Fr=0.3$, (b) $Fr=1$ and (c) $Fr=3$. The corresponding values for the 1WC simulations are also shown for reference.

Figure 19

Figure 17.Plots showing $[\mathbb {P}(\mathcal {Q}>0)-\mathbb {P}(\mathcal {Q}<0)]\vert _{St=0}$ vs volume fraction $\varPhi$ for simulations with (a) $Fr=0.3$, (b) $Fr=1$ and (c) $Fr=3$. The corresponding values for the 1WC simulations are also shown for reference.

Figure 20

Figure 18.Plots of $A$ (blue) and $B$ (red) vs volume fraction $\varPhi$, for 1WC (dashed) and 2WC (solid) flows for particles with (a–c) ${St}_1=0.3$, (d–f) ${St}_2=0.5$, (g–i) ${St}_3=0.7$ and (j–l) ${St}_5=2$. Panels (a,d,g,j) correspond to simulations with $Fr=0.3$; panels (b,e,h,k) correspond to simulations with $Fr=1$; panels (c,f,i,l) correspond to simulations with $Fr=3$. See figure 8 for the volume fraction dependence in simulations with ${St}_4$ particles.

Figure 21

Figure 19.Plots of $A$ (blue) and $B$ (red) vs Stokes number $St$, for 1WC (dashed) and 2WC (solid) flows for volume fractions (a–c) $\varPhi _1$, (d–f) for $\varPhi _2$, (g–i) $\varPhi _3$ and (j–l) $\varPhi _5$. Panels (a,d,g,j) correspond to simulations with $Fr=0.3$; panels (b,e,h,k) correspond to simulations with $Fr=1$; and panels (c,f,i,l) correspond to simulations with $Fr=3$. See figure 8 for the $St$-dependence in simulations with volume fraction $\varPhi _4$.