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Model for the dynamics of micro-bubbles in high-Reynolds-number flows

Published online by Cambridge University Press:  01 October 2019

Zhentong Zhang
Affiliation:
Institut de Mécanique des Fluides de Toulouse (IMFT), Université de Toulouse, CNRS, INPT, UPS, Toulouse, France
Dominique Legendre
Affiliation:
Institut de Mécanique des Fluides de Toulouse (IMFT), Université de Toulouse, CNRS, INPT, UPS, Toulouse, France
Rémi Zamansky*
Affiliation:
Institut de Mécanique des Fluides de Toulouse (IMFT), Université de Toulouse, CNRS, INPT, UPS, Toulouse, France
*
†Email address for correspondence: remi.zamansky@imft.fr

Abstract

We propose a model for the acceleration of micro-bubbles (smaller than the dissipative scale of the flow) subjected to the drag and fluid inertia forces in a homogeneous and isotropic turbulent flow. This model, that depends on the Stokes number, Reynolds number and the density ratio, reproduces the evolution of the acceleration variance as well as the relative importance and alignment of the two forces as observed from direct numerical simulations (DNS). We also report that the bubble acceleration statistics conditioned on the local kinetic energy dissipation rate are invariant with the Stokes number and the dissipation rate. Based on this observation, we propose a stochastic model for the instantaneous bubble acceleration vector accounting for the small-scale intermittency of the turbulent flows. The norm of the bubble acceleration is obtained by modelling the dissipation rate along the bubble trajectory from a log-normal stochastic process, whereas its orientation is given by two coupled random walks on a unit sphere in order to model the evolution of the joint orientation of the drag and inertia forces acting on the bubble. Furthermore, the proposed stochastic model for the bubble acceleration is used in the context of large eddy simulations (LES) of turbulent flows laden with small bubbles. To account for the turbulent motion at scales smaller than the mesh resolution, we decompose the instantaneous bubble acceleration in its resolved and residual parts. The first part is given by the drag and fluid inertia forces computed from the resolved velocity field, and the second term refers to the random contribution of small unresolved turbulent scales and is estimated with the stochastic model proposed in the paper. Comparisons with DNS and standard LES, show that the proposed model improves significantly the statistics of the bubbly phase.

Information

Type
JFM Papers
Copyright
© 2019 Cambridge University Press 
Figure 0

Table 1.The numerical parameters of the DNS and LES. The number of grid points in each direction is given by $N$. The size of numerical domain is $H=2\unicode[STIX]{x03C0}$, $\unicode[STIX]{x1D70F}_{L}=(2/3K)/\unicode[STIX]{x1D700}$ is the eddy turnover time, $L=(2/3K)^{3/2}/\unicode[STIX]{x1D700}$ is the scale of the large eddies, $K$ is the average turbulent kinetic energy and $\unicode[STIX]{x1D700}$ is the average dissipation rate. The Reynolds number based on the large scale of the flow is given by $Re_{H}$, $Re_{\unicode[STIX]{x1D706}}$ is Reynolds number based on the Taylor length scale, $\unicode[STIX]{x1D702}$ and $\unicode[STIX]{x1D70F}_{\unicode[STIX]{x1D702}}$ are the Kolmogorov length and time scale and $\unicode[STIX]{x1D70F}_{\unicode[STIX]{x1D6E5}}=\unicode[STIX]{x1D6E5}^{2}/\unicode[STIX]{x1D708}_{\unicode[STIX]{x1D6E5}}$.

Figure 1

Table 2.The Stokes numbers and non-dimensional diameters of the bubbles used for the DNS and LES, and the bubble Reynolds numbers computed from the DNS.

Figure 2

Figure 1.Acceleration variance normalized by the fluid tracer acceleration variance from our DNS for bubbles (● and continuous line), the DNS data of Bec et al. (2010) and Lanotte (2011) for heavy inertial particles $\unicode[STIX]{x1D6FD}=0$, $Re_{\unicode[STIX]{x1D706}}=400$ (▴ and continuous line), the DNS from Calzavarini et al. (2009) for $\unicode[STIX]{x1D6FD}=2.5$ and $Re_{\unicode[STIX]{x1D706}}=180$, with and without the Faxén correction ($+$ with dotted and dot-dashed lines, respectively), and $\unicode[STIX]{x1D6FD}=0.14$ ($+$ with continuous line), the experimental measurements from Prakash (2013) for $Re_{\unicode[STIX]{x1D706}}=145-230$ and $\unicode[STIX]{x1D6FD}\approx 3$ ($\times$ with dashed lines). Comparison with the relation (3.4), $\langle \boldsymbol{a}_{b}^{2}\rangle (St,\unicode[STIX]{x1D6FD},Re_{0})/\langle \boldsymbol{a}_{b}^{2}\rangle (0,1,Re_{0})$ with $c_{1}=2.8$ and $Re_{0}^{1/2}=0.08Re_{\unicode[STIX]{x1D706}}=16$ for $\unicode[STIX]{x1D6FD}=0$, 0.14, 0.5, 1, 1.5, 2, 2.5 and 3 from black to orange, in dashed lines, and with $c_{1}=2.8$ and $Re_{0}^{1/2}=0.08Re_{\unicode[STIX]{x1D706}}=32$, $\unicode[STIX]{x1D6FD}=0$ in black dotted line. The inset is the response function (3.1) as a function of $\unicode[STIX]{x1D714}\unicode[STIX]{x1D70F}_{b}$ for $\unicode[STIX]{x1D6FD}=0$, 0.5, 1, 2 and 3 from black to orange, respectively.

Figure 3

Figure 2.(a) Lagrangian fluid velocity spectra along the bubble trajectory from the DNS for $St=0.02$, 0.074, 0.20, 0.45, 1.01, 1.55 and 2.07 (from black to red, respectively). Comparison with the power law $\unicode[STIX]{x1D714}^{-2}$ and the relation (3.3), $k_{0}/((\unicode[STIX]{x1D714}/\unicode[STIX]{x1D714}_{\unicode[STIX]{x1D702}})^{2}+(\unicode[STIX]{x1D714}_{0}/\unicode[STIX]{x1D714}_{\unicode[STIX]{x1D702}})^{2})$ with $k_{0}=1$ and $\unicode[STIX]{x1D714}_{0}/\unicode[STIX]{x1D714}_{\unicode[STIX]{x1D702}}=0.0092$ in grey dot-dashed and dashed lines, respectively. (b) Evolution with the Stokes number of the variance of the material derivative of fluid velocity at the bubble position (black circles) and of the Lagrangian time derivative along the bubble trajectories of the fluid velocity (red crosses). Both quantities are normalized by the global variance of the fluid tracer acceleration. The inset is the variance of the difference between these two quantities in logarithmic scales normalized by the Kolmogorov acceleration and comparison with the $St$ and $St^{1/2}$ power laws.

Figure 4

Figure 3.(a) The p.d.f.s of the bubble acceleration normalized by its root-mean-square value in black for $St=0.02$, 0.074, 0.20, 0.45, 1.01, 1.55 and 2.07 (shifted upward by two decades from each other for clarity, respectively) and comparison with the p.d.f.s of the acceleration of fluid tracers in red. (b) Flatness of the bubble acceleration (●) and of the fluid acceleration at the bubble position ($+$) against $St$ from our DNS.

Figure 5

Figure 4.(a) Evolution with the Stokes number of the variance of the drag force (circle) and inertia force (crosses) relative to the bubble acceleration variance according to our DNS and comparison with (3.6) and (3.7) normalized by (3.4) with $c_{1}=2.8$ and $Re_{0}^{1/2}=16$ in dashed and dot-dashed lines, respectively. (b) The p.d.f. of the fluid inertia forces (black) and of the drag force (red) normalized by their root-mean-square value for $St=0.02$, 0.074, 0.20, 0.45, 1.01, 1.55 and 2.07 (shifted upward by one decade from each other for clarity, respectively).

Figure 6

Figure 5.(a) Evolution with $St$ of the coefficient of correlation between the drag and inertia forces (dots) and of $\langle \cos \unicode[STIX]{x1D703}\rangle$ ($\unicode[STIX]{x1D703}$ being the relative orientation of the forces) (crosses) from the DNS and comparison with relation (3.8) normalized by (3.6) and (3.7) with $c_{1}=2.8$ and $Re_{0}^{1/2}=16$ in blue lines. (b) The p.d.f.s of the cosine of the angle $\unicode[STIX]{x1D703}$ between the two forces, for $St=0.02$, 0.074, 0.20, 0.45, 1.01, 1.55 and 2.07 (from black to red, respectively).

Figure 7

Figure 6.(a) Autocorrelation coefficient of the bubble acceleration, drag force and fluid inertia terms (shifted upward by one unit from each other, respectively, for clarity) from our DNS. (b) Cross-correlation between the drag force and the fluid inertia term as given by our DNS. The inset is the evolution of the time lag (defined as the time of the peak of cross-correlation) with $St$, and comparison with the $\unicode[STIX]{x1D70F}_{lag}/\unicode[STIX]{x1D70F}_{\unicode[STIX]{x1D702}}=St$ and $\unicode[STIX]{x1D70F}_{lag}/\unicode[STIX]{x1D70F}_{\unicode[STIX]{x1D702}}=(\unicode[STIX]{x1D6FD}-1)^{-1}\tan ^{-1}((\unicode[STIX]{x1D6FD}-1)St)$. For both figures $St=0.02$, 0.074, 0.20, 0.45, 1.01, 1.55 and 2.07 (from black to red, respectively).

Figure 8

Figure 7.(a) Variance of the bubble acceleration conditioned on the local value of the dissipation rate $\unicode[STIX]{x1D700}$ for the various Stokes number $St=0.02$, 0.074, 0.20, 0.45, 1.01, 1.55 and 2.07 (from black to red, respectively) normalized by unconditional bubble acceleration variance, and comparison with the relation $\langle \boldsymbol{a}_{b}^{2}|\unicode[STIX]{x1D700}\rangle /\langle \boldsymbol{a}_{b}^{2}\rangle =(\unicode[STIX]{x1D700}/\langle \unicode[STIX]{x1D700}\rangle )^{3/2}$ with a dashed line. (b) The p.d.f.s of acceleration conditioned on the dissipation rate for $St=1$. Eight values of $\unicode[STIX]{x1D700}$ are reported, $\unicode[STIX]{x1D700}/\langle \unicode[STIX]{x1D700}\rangle =0.17$, $0.28$, $0.46$, $0.77$, $1.3$, $2.1$, $3.5$ and $5.8$ (shifted upward by two decades from each other, respectively) and comparison with unconditioned bubble acceleration p.d.f. with dashed lines.

Figure 9

Figure 8.(a) The p.d.f.s of $\boldsymbol{e}_{I}^{\ast }\boldsymbol{\cdot }\boldsymbol{e}_{D}^{\ast }$ for $St=0.02$, 0.074, 0.20, 0.45, 1.01, 1.55 and 2.07 (from black to red, respectively) as obtained from model (4.8)–(4.11). The inset is the evolution of $\langle \boldsymbol{e}_{D}^{\ast }\boldsymbol{\cdot }\boldsymbol{e}_{I}^{\ast }\rangle$ with $St$ as given by the stochastic model, and comparison with the relation (3.8). (b) Cross-correlation between $\boldsymbol{e}_{D}^{\ast }$ and $\boldsymbol{e}_{I}^{\ast }$ obtained from the model (4.8)–(4.11). The inset is the evolution of the time lag between $\boldsymbol{e}_{D}^{\ast }$ and $\boldsymbol{e}_{I}^{\ast }$ against $St$, and comparison with $\unicode[STIX]{x1D70F}_{\unicode[STIX]{x1D702}}(\unicode[STIX]{x1D6FD}-1)^{-1}\tan ^{-1}((\unicode[STIX]{x1D6FD}-1)St)$.

Figure 10

Figure 9.(a) Bubble acceleration variance normalized by the Kolmogorov acceleration ($a_{\unicode[STIX]{x1D702}}^{2}$) versus Stokes number in logarithm scale. Open symbols are LES with the proposed model; filled symbols are LES without model; for the three meshes we have $32^{3}$ (circles), $48^{3}$ (triangles) and $64^{3}$ (diamonds). Comparison with our DNS blue stars. (b) The p.d.f. of the bubble acceleration normalized by its variance for $St=0.02$, 0.074, 0.20, 0.45, 1.01, 1.55 and 2.07 (shifted upward by one decade each other, respectively). The DNS is a dashed black line, LES with the proposed model for $64^{3}$ is a solid red line and LES without model for $64^{3}$ is a blue dashed line.

Figure 11

Figure 10.Autocorrelation of the bubble acceleration for $St=0.07$. The DNS is a solid black line, LES with model for $64^{3}$ is a dashed red line and LES without model for $64^{3}$ is a dot-dashed black line. The inset is the evolution of the corresponding integral time scale normalized by the Kolmogorov time with the Stokes number. The DNS are circles, LES with the proposed model are stars, LES without model are crosses. The mesh size for the LES is $64^{3}$.

Figure 12

Figure 11.(a) Evolution of the second-order Lagrangian structure function with the time lag. (b) Evolution of the flatness of the Lagrangian velocity increments with the time lag. Comparison between the DNS (solid blue line), the Standard LES (black dot-dashed lines) and LES with the proposed model (dashed red lines). For both figures, for $St=0.02$, the mesh size for the LES is $64^{3}$.

Figure 13

Figure 12.Variance of the total bubble acceleration $\boldsymbol{a}_{b}=\overline{\boldsymbol{a}}_{b}+\boldsymbol{a}_{\ast }$ conditioned on the stochastic value of the dissipation rate $\unicode[STIX]{x1D700}_{\ast }$ obtained from the LES with the stochastic model (black line) and comparison with the bubble acceleration variance conditioned on the local dissipation rate obtained from the DNS (red line), with $St=0.02$ and a mesh size of $48^{3}$ for the LES.