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Collision rate of bidisperse, hydrodynamically interacting spheres settling in a turbulent flow

Published online by Cambridge University Press:  04 February 2021

Johnson Dhanasekaran
Affiliation:
Sibley School of Mechanical and Aerospace Engineering, Cornell University, Ithaca, NY 14853, USA
Anubhab Roy
Affiliation:
Department of Applied Mechanics, Indian Institute of Technology Madras, Chennai, Tamil Nadu 600036, India
Donald L. Koch*
Affiliation:
Smith School of Chemical and Biomolecular Engineering, Cornell University, Ithaca, NY 14853, USA
*
†Email address for correspondence: dlk15@cornell.edu

Abstract

The collisions in a dilute polydisperse suspension of sub-Kolmogorov spheres with negligible inertia settling in a turbulent flow and interacting through hydrodynamics including continuum breakdown on close approach are studied. A statistically significant decrease in ideal collision rate without gravity is resolved via a Lagrangian stochastic velocity-gradient model at Taylor microscale Reynolds number larger than those accessible by current direct numerical simulation capabilities. This arises from the difference between the mean inward velocity and the root-mean-square particle relative velocity. Differential sedimentation, comparable to the turbulent shear relative velocity, but minimally influencing the sampling of the velocity gradient, diminishes the Reynolds number dependence and enhances the ideal collision rate i.e. the rate without interactions. The collision rate is retarded by hydrodynamic interactions between sphere pairs and is governed by non-continuum lubrication as well as full continuum hydrodynamic interactions at larger separations. The collision efficiency (ratio of actual to ideal collision rate) depends on the relative strength of differential sedimentation and turbulent shear, the size ratio of the interacting spheres and the Knudsen number (defined as the ratio of the mean-free path of the gas to the mean radius of the interacting spheres). We develop an analytical approximation to concisely report computed results across the parameter space. This accurate closed form expression could be a critical component in computing the evolution of the size distribution in applications such as water droplets in clouds or commercially valuable products in industrial aggregators.

Information

Type
JFM Papers
Copyright
© The Author(s), 2021. Published by Cambridge University Press
Figure 0

Table 1. Droplet pairs at the lower end of the ‘size gap’ whose collisions are weakly influenced by particle inertia. The radius $a_1$ and Stokes number $St$ for turbulent shear are listed for the larger drop. For $St<0.2$ the effect of the inertial response to turbulence on the collision rate can be captured by multiplying an inertialess local collision rate by an enhanced pair distribution function obtained from studies of inertial clustering. The critical size ratio $\kappa$ above which the gravitational Stokes number $St_{g}<1.9$, corresponding to a deviation of less than $10\,\%$ from the inertialess case, and the corresponding $Q$ values are also shown. All these values justify a local collision rate calculation performed without inertia and gravitational sampling. Consistent with conditions typical in a cloud we take $\epsilon =10^{-2}\ \textrm {m}^2\ \textrm {s}^{-3}$.

Figure 1

Figure 1. Case ‘I’ is the ideal collision rate $K^{0}_{12}$ given as a function of ${Re}_{\lambda }$ for $Q=0$, i.e. no gravitational effects. The variation of the inward velocity on the collision sphere with Taylor microscale Reynolds number is given by ‘II’. Calculations performed with a frozen velocity gradient during any given satellite sphere evolution are denoted by ‘III’. Case ‘IV’ is the model of Saffman & Turner (1956), which is independent of ${Re}_{\lambda }$. A portion of the decreased inward velocity can be attributed to changes in $\langle \varPhi ^{1/2} \rangle$ as the log normal pseudo-dissipation distribution becomes broader with increasing Taylor microscale Reynolds number. This quantity is continuously decreasing with ${Re}_{\lambda }$ and is given as ‘$V$’ after multiplying with $\int _{(r=2)\& (n_i\varGamma _{ij}n_j<0)} \, \textrm {d} A n_i\varGamma _{ij}n_j/\varPhi ^{1/2} \approx 1.4$. The predictions of the ideal collision rate fit, given in (3.2), are plotted as ‘VI’.

Figure 2

Figure 2. The ideal collision rate $K^0_{12}$ is given as a function of $Q$ at ${Re}_{\lambda }=90$ and $2500$. The symbols correspond to the numerically calculated collision rate and the solid lines to the fit. The higher ${Re}_{\lambda }$ corresponds to lower collision rate. For reference, the ideal collision rate predicted by Smoluchowski (1918) for spheres settling in a quiescent fluid is given by the dashed line.

Figure 3

Figure 3. The decrease of the collision efficiency $\beta$ with decreasing $Kn$ is shown for $\kappa =0.7$ and ${Re}_{\lambda }=2500$. Panel (a) is in the pure turbulence limit ($Q=0$) and (b) is for the differential-sedimentation limit ($Q \to \infty$).

Figure 4

Figure 4. The collision efficiency is shown as a function of $\kappa$ for $Kn=10^{-3}$ and ${Re}_{\lambda }=2500$. Panel (a) is in the absence of gravitational effects ($Q=0$) and (b) is in a purely gravity driven flow ($Q \to \infty$).

Figure 5

Figure 5. The dependence of $\beta$ on ${Re}_{\lambda }$ is shown for $Kn=10^{-2}, \kappa =0.9$ at (a) $Q=0$, (b) $Q \approx 1$ and (c) $Q \approx 10$. The collision efficiency varies with ${Re}_{\lambda }$ for moderate $Q$.

Figure 6

Figure 6. The variation of the collision efficiency with $Q$ is shown for $Kn=10^{-3}$ and $\kappa =0.5$. The symbols correspond to the stochastic linear flow field with ${Re}_{\lambda }=2500$. The solid line is the frozen uniaxial compressional flow calculation, with the compression axis aligned with gravity.

Figure 7

Table 2. Values of the coefficients in the asymptotic forms of the continuum mobilities: $B_0,B_1,M_0,M_1,A_,L_1$ at various values of $\kappa$. These have been obtained from the work of Jeffrey & Onishi (1984), Jeffrey (1992) and Wang et al. (1994).

Figure 8

Figure 7. The collision efficiency is plotted as a function of $Kn$ for $\kappa =0.4$. Panel (a) is in the pure turbulence limit ($Q=0$) and (b) is for pure differential sedimentation ($Q \to \infty$). The symbols represent the results of the numerical calculation. The solid lines are the analytical approximation, given in (5.7), which provides a good prediction of the numerical results.

Figure 9

Table 3. Values of the fitting parameters $p_{1,\epsilon }, p_{2,\epsilon },p_{1,g}$ and $p_{2,g}$ at various values of $\kappa$.

Figure 10

Figure 8. The value of $\beta$ is shown as a function of $\kappa$ at $Kn=10^{-2}$. Panel (a) is in the absence of gravitational effects ($Q=0$) and (b) is in a purely gravity-driven flow ($Q \to \infty$). The symbols represent the results of the numerical calculation with errors bars of $\pm \sigma _e/N_r$. The solid line is from (5.7) and agrees well with the data for $\kappa \geq 0.3$.

Figure 11

Figure 9. The collision efficiency $\beta$ is plotted as a function of $Q$ for $Kn=10^{-1}$ and $\kappa =0.6$. The symbols represent the results of the numerical calculation. The solid line is from (5.7), with the fitting parameter forms given in (5.9) and values in table 3. The agreement is good across the parameter space.

Figure 12

Figure 10. The collision efficiency $\beta$ for differential-sedimentation-driven collisions with $a_1=10~\mathrm {\mu } \textrm {m}$. The analytical model results for van der Waals attractions and non-continuum hydrodynamic interactions (model: $vdW+NC$), non-continuum hydrodynamic interactions without van der Waals forces (model: $NC$) and van der Waals attractions in a continuum gas (model: $vdW$) are plotted as a function of the size ratio and compared to results of Davis's (1984) trajectory analysis with $vdW+NC$ and particle inertia. The composite model (model: $vdW+NC$) is in good agreement with the computational result. Our own trajectory analysis with $vdW+NC$ and without particle inertia is very close to the results of Davis (1984), indicating that particle inertia is negligible for this drop size.

Figure 13

Figure 11. Experimentally evaluated $b/n_i$ from Duru et al. (2007) is plotted against the initial mean particle size reported in experiments and compared against the theoretical predictions obtained using our $K_{12}$. In (a) we show results for a Kolmogorov shear rate of 88 s$^{-1}$. The ‘$\times$’ are the experimental results, the filled circles are $b/n_i$ computed using the ideal result and the open circles are $b/n_i$ evaluated with $K_{12}^{NC+vdW}$. In (b) we show results for the Kolmogorov shear rate of 88 s$^{-1}$ in green, 59 s$^{-1}$ in red and 25 s$^{-1}$ in blue. The ideal result is not shown here for the sake of conciseness.