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Dynamics of finite-size spheroids in turbulent flow: the roles of flow structures and particle boundary layers

Published online by Cambridge University Press:  30 March 2022

Linfeng Jiang
Affiliation:
Center for Combustion Energy, Key laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Energy and Power Engineering, Tsinghua University, Beijing 100084, PR China
Cheng Wang
Affiliation:
Center for Combustion Energy, Key laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Energy and Power Engineering, Tsinghua University, Beijing 100084, PR China
Shuang Liu
Affiliation:
Center for Combustion Energy, Key laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Energy and Power Engineering, Tsinghua University, Beijing 100084, PR China
Chao Sun*
Affiliation:
Center for Combustion Energy, Key laboratory for Thermal Science and Power Engineering of Ministry of Education, Department of Energy and Power Engineering, Tsinghua University, Beijing 100084, PR ChinaDepartment of Engineering Mechanics, School of Aerospace Engineering, Tsinghua University, Beijing 100084, PR China
Enrico Calzavarini*
Affiliation:
Univ. Lille, Unité de Mécanique de Lille – J. Boussinesq – ULR 7512, F-59000 Lille, France
*
†Email addresses for correspondence: chaosun@tsinghua.edu.cn, enrico.calzavarini@polytech-lille.fr
†Email addresses for correspondence: chaosun@tsinghua.edu.cn, enrico.calzavarini@polytech-lille.fr

Abstract

We study the translational and rotational dynamics of neutrally buoyant finite-size spheroids in hydrodynamic turbulence by means of fully resolved numerical simulations. We examine axisymmetric shapes, from oblate to prolate, and the particle volume dependences. We show that the accelerations and rotations experienced by non-spherical inertial-scale particles result from volume filtered fluid forces and torques, similar to spherical particles. However, the particle orientations carry signatures of preferential alignments with the surrounding flow structures, which are reflected in distinct axial and lateral fluctuations for accelerations and rotation rates. The randomization of orientations does not occur even for particles with volume-equivalent diameter size in the inertial range, here up to $60$ dissipative units ($\eta$) at Taylor-scale Reynolds number ${Re_{\lambda }=120}$. Additionally, we demonstrate that the role of fluid boundary layers around the particles cannot be neglected in reaching a quantitative understanding of particle statistical dynamics, as they affect the intensities of the angular velocities and the relative importance of tumbling with respect to spinning rotations. This study brings to the fore the importance of inertial-scale flow structures in homogeneous and isotropic turbulence and their impacts on the transport of neutrally buoyant bodies with sizes in the inertial range.

Information

Type
JFM Papers
Copyright
© The Author(s), 2022. Published by Cambridge University Press
Figure 0

Table 1.Parameters of the NSE numerical simulations and relevant turbulence scales. Here, $N^{3}$: number of spatial grid points, $\eta =(\nu ^{3}/\epsilon )^{1/4}$: Kolmogorov dissipation length scale in grid space units $\Delta x$, $\tau _\eta$: Kolmogorov time scale in time-step units $\Delta t$, $L=u'^{3}/\epsilon$: integral scale, $T_L=L/u'$: large-eddy turnover time, $\lambda = (15 \nu u' / \epsilon )^{1/2}$: Taylor micro-scale, $Re_\lambda$: Taylor–Reynolds number.

Figure 1

Figure 1.Parameter space of particle shapes and sizes in turbulent scale units at $Re_\lambda =120$. The symbols indicate the numerically simulated particle types. All particles are axisymmetric of diameter $d$ and length $l$, aspect ratio $\alpha =l/d$, with $\alpha = 1/2,1,2,4$, the volume-equivalent diameter is $D_v = (l d^{2})^{1/3}$. The lengths are here all expressed in terms of the dissipative scale $\eta$. The Taylor micro-scale $\lambda$ (dashed lines) and the integral scale $L$ (dashed-dotted lines) are also reported.

Figure 2

Table 2.Summary of the six numerical experiments with the corresponding involved dynamical equations: Navier–Stokes equation (NSE) (2.1)–(2.2), Newton–Euler equation (NEE) (2.3)–(2.4); Euler equation (EE) (2.4) only rotation for particles with fixed location; no-slip boundary conditions (i.e. two-way coupling) at particle–fluid interface implemented via the IBM; tracer equation (2.11), Jeffery equation (2.12)–(2.13).

Figure 3

Figure 2.Sketches of the six numerical experiments performed: (a) real particles RP, (b) real particles with fixed locations RPFL, (c) virtual particles VP, i.e. particles without solid–fluid boundaries, (d) virtual particles with fixed locations VPFL, (e) Jeffery fluid tracers JFT and (f) volume average of fluid tracers VA. The light blue region denotes the fluid. The black shaded areas in panels (a,b) represent the two-way coupling region. The points in panels (e,f) represent the Jeffery fluid tracers. The tracers marked in black in panel (f) are used to calculate the volume averages.

Figure 4

Figure 3.(a) Example of trajectory for a spheroid with an equivalent diameter $D_v\approx 25\eta$ and aspect ratio $\alpha =2$ at $Re_\lambda =120$. The slices show the local dissipation rate $\epsilon _{\boldsymbol {x},t}$, normalized by $\epsilon$, at the planes through the spheroid centre at times $t=0,8.7,17.4,26.1,39.1$ in $\tau _\eta$. (b) Azimuthally and temporally averaged dissipation rate $\overline \epsilon$, normalized by $\epsilon$, around the spheroid with a diameter $D_v\approx 25\eta$ and aspect ratio $\alpha =2$ at $Re_\lambda =120$. The black line denotes the contour line of ${\rm log}_{10}(\bar {\epsilon }/\epsilon )=0$. (c) Azimuthally and temporally averaged square of $\boldsymbol {u}-\boldsymbol {v}$, normalized by the mean square of $\boldsymbol {u}$, around the spheroid with diameter $D_v= 25\eta$ and aspect ratio $\alpha =2$ at $Re_\lambda =120$. The black line denotes the contour line of $\overline {(\boldsymbol {u}-\boldsymbol {v})^{2}}/\langle \boldsymbol {u}^{2}\rangle ^{v,t}=1$. Here, $x_p$ and $y_p$ represent the coordinates in the particle frame.

Figure 5

Figure 4.(a) Normalized single component acceleration variance as a function of the normalized particle size $D_v/\eta$ at $Re_\lambda =120$ for real particles (RP: solid symbols) and volume averages (VA: open symbols). The dashed lines are the fitting lines for spheres of RP (exponent $-1.0 \pm 0.1$). Inset in (a) shows the ratio of acceleration variance of VA to acceleration variance of RP, $\langle a_i^{2} \rangle ^{VA}/\langle a_i^{2} \rangle$, as a function of $D_v/\eta$. (b) Normalized componentwise acceleration variance as a function of the normalized particle size $D_v/\eta$ at $Re_\lambda =120$ for real particles (RP: solid symbols) and virtual particles (VP: open symbols). The dashed lines are the fitting lines for spheres of RP. Inset in (b) shows the ratio of acceleration variance of VP to acceleration variance of RP, $\langle a_i^{2} \rangle ^{VP}/\langle a_i^{2} \rangle$, as a function of $D_v/\eta$. (c) The ratio of axial variance $\langle (\boldsymbol {a}\boldsymbol {\cdot } \boldsymbol {p})^{2}\rangle$ to lateral variance $\langle |\boldsymbol {a}\times \boldsymbol {p}|^{2}\rangle$ of particle acceleration as a function of aspect ratio at $Re_\lambda =120$ for RP (triangles), VA (square) and VP (circles), respectively. The black dash-dot line denotes the results of Jeffery tracers. The colour represents the normalized particle size $D_v/\eta$ in logarithmic scale.

Figure 6

Figure 5.The p.d.f.s of $|\cos (\theta _{\boldsymbol {a},\boldsymbol {p}})|$ for RP spheroids with different aspect ratios: (a) $\alpha =0.5$, (b) $\alpha =1$, (c) $\alpha =2$ and (d) $\alpha =4$ and for Jeffery fluid tracers.

Figure 7

Figure 6.(a) Mean squared angular velocity, normalized by the results of Jeffery tracers with corresponding aspect ratio, as a function of $D_v/\eta$ at $Re_\lambda =120$. The open symbols denote the results of VA for spheres. The dashed line denotes the fitting line for spheres with scaling exponent $-4/3$. Inset shows the ratio of angular velocity variance of VA to that of RP, $\langle \varOmega _i\varOmega _i \rangle ^{VA}/\langle \varOmega _i\varOmega _i \rangle$, as a function of $D_v/\eta$ for spheres. (b) Mean squared angular velocity, normalized by the results of Jeffery tracers with corresponding aspect ratio, as a function of $D_v/\eta$ at $Re_\lambda =120$. The open symbols denote the results of VP. The dashed line denotes the fitting line for spheres with scaling exponent $-4/3$. Inset shows the ratio of angular velocity variance of VP to that of RP, $\langle \varOmega _i\varOmega _i \rangle ^{VP}/\langle \varOmega _i\varOmega _i \rangle$, as a function of $D_v/\eta$.

Figure 8

Figure 7.(a) The ratio of spinning rate squared to tumbling rate squared, $\langle \varOmega _i^{s}\varOmega _i^{s}\rangle /\langle \dot {p}_i\dot {p}_i\rangle$, as a function of aspect ratio $\alpha$ for RP. The colour bar represents the normalized particle size $D_v/\eta$ in the logarithmic scale. Spheres denote the results for Jeffery tracers. Leftward triangles denote the results at $Re_\lambda =32$ and rightward triangles denote the results at $Re_\lambda =120$. The arrows denote the direction in which the size of the particles increases. The dashed line shows the results of tracers at $Re_\lambda =433$ in Byron et al. (2015). (b) The ratio of mean spinning rate squared to mean tumbling rate squared, $\langle {\varOmega }_i^{s}{\varOmega }_i^{s}\rangle /\langle \dot {p}_i\dot {p}_i\rangle$, as a function of size $D_v/\eta$. (c) The cartoon illustrates that the weight of the tumbling rate in the angular velocity of prolate spheroids becomes larger as the particle size increases. (d) The ratio of spinning rate squared to tumbling rate squared, $\langle \varOmega _i^{s}\varOmega _i^{s}\rangle /\langle \dot {p}_i\dot {p}_i\rangle$, as a function of aspect ratio $\alpha$ for VA and VP. The colour bar represents the normalized particle size $D_v/\eta$ in logarithmic scale.

Figure 9

Figure 8.Mean squared angular velocity, normalized by the results of tracers with corresponding aspect ratio, as a function of $D_v/\eta$ for the numerical experiments of (a) RPFL and (b) VPFL, compared with the results of RP. Insets show the ratio of the mean squared angular velocity of the numerical experiments to the results of RP as a function of $D_v/\eta$. The ratio of the mean spinning rate squared to the mean tumbling rate squared, $\langle \varOmega _i^{s}\varOmega _i^{s}\rangle /\langle \dot {p}_i\dot {p}_i\rangle$, as a function of aspect ratio $\alpha$ for the numerical experiments of (c) RPFL and (d) VPFL, respectively. The colour bar represents the normalized particle size $D_v/\eta$ in logarithmic scale.

Figure 10

Figure 9.Field of the ratio $\tfrac {1}{4} \overline {\boldsymbol {\omega }^{2}} / \overline {\boldsymbol {S}:\boldsymbol {S}}$ at (a) $\alpha =1$, $D_v = 20$ (b) $\alpha =0.5$, $D_v = 25.1$ and (c) $\alpha =2$, $D_v =25.1$ at $Re_{\lambda } =120$. The colour bar indicates the value of $\tfrac {1}{4} \overline {\boldsymbol {\omega }^{2}} / \overline {\boldsymbol {S}:\boldsymbol {S}}$. (d) The ratio of $\langle \tfrac {1}{4} \overline {\boldsymbol {\omega }^{2}} \rangle |_{1.5D_v}$ to $\langle \overline {\boldsymbol {S}:\boldsymbol {S}} \rangle |_{1.5D_v}$ as a function of $D_v/\eta$.

Figure 11

Table 3.Parameter of the NSE numerical simulations and relevant turbulence scales. $N^{3}$: number of spatial grid points, $\eta =(\nu ^{3}/\epsilon )^{1/4}$: Kolmogorov dissipation length scale in grid space units $\Delta x$, $\tau _\eta$: Kolmogorov time scale in time-step units $\Delta t$, $L=u'^{3}/\epsilon$: integral scale, $T_L=L/u'$: large-eddy turnover time, $\lambda = (15 \nu u' / \epsilon )^{1/2}$: Taylor micro-scale, $Re_\lambda$: Taylor–Reynolds number.

Figure 12

Figure 10.Parameter space of particle shapes and sizes in turbulent scale units at $Re_\lambda =32$. The symbols indicate the numerically simulated particle types. All particles are axisymmetric of diameter $d$ and length $l$, aspect ratio $\alpha =l/d$, with $\alpha = 1/2,1,2,4$, the volume-equivalent diameter is $D_v = (l d^{2})^{1/3}$. The lengths are here all expressed in terms of the dissipative scale $\eta$. The Taylor micro-scale $\lambda$ (dashed lines) and the integral scale $L$ (dashed-dotted lines) are also reported.

Figure 13

Figure 11.(a) Normalized single Cartesian component of the acceleration variance $\langle a_i^{2}\rangle /\langle a_i^{2}\rangle ^{tracer}$ as a function of the normalized particle size $d/\eta$ at $Re_\lambda =32$. Squares denote the results in Homann & Bec (2010) at the same $Re_\lambda$. The dashed-dot line denotes the Faxén correction (Calzavarini et al.2012). The inset shows the p.d.f.s of acceleration for different sizes. (b) Normalized correlation time of acceleration, $T_I/\tau _\eta$, as a function of the normalized particle size $D_v/\eta$. Squares denote the correlation time in Homann & Bec (2010) at the same $Re_\lambda$. The inset shows the autocorrelation function of a single Cartesian acceleration component.

Figure 14

Figure 12.Ratio of spinning rate variance over tumbling rate variance: comparison of present DNS results at $Re_{\lambda }=120$ with the experimental measurements by Oehmke et al. (2021) at $Re_{\lambda } \in [90,630]$. (a) Particle rotation ratio as a function of aspect ratio, here the colour code maps the particle size in equivalent radius units. (b) Rotation ratio compensated by $\alpha ^{4/3}$ as a function of the particle length (i.e. the symmetry axis) $l$ normalized by the Taylor microscale $\lambda$ (same as figure 5(b) in Oehmke et al.2021).