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Fluid dynamics and passive scalar transport driven by non-uniform tumbling of a prolate spheroid in simple shear flow

Published online by Cambridge University Press:  14 October 2025

Yanxing Wang*
Affiliation:
Department of Mechanical and Aerospace Engineering, New Mexico State University, Las Cruces, NM 88003, USA
Hui Wan
Affiliation:
Department of Mechanical and Aerospace Engineering, University of Colorado, Colorado Springs, CO 80918, USA
Tie Wei
Affiliation:
Department of Mechanical Engineering, New Mexico Institute of Mining and Technology, Socorro, NM 87801, USA
Fangjun Shu
Affiliation:
Department of Mechanical and Aerospace Engineering, New Mexico State University, Las Cruces, NM 88003, USA
*
Corresponding author: Yanxing Wang, yxwang@nmsu.edu

Abstract

Using high-fidelity numerical simulations based on a lattice Boltzmann framework, the advection-enhanced transport of a passive scalar from a prolate spheroid in simple shear flow has been thoroughly investigated across various parameters, including the spheroid’s aspect ratio, particle-to-fluid density ratio, Reynolds number (defined as ${\textit{Re}}=\textit{GR}^{2}/\nu$, where $G$ is the flow shear rate, $R$ is the radius of a sphere of the same volume as the spheroid and $\nu$ is the kinematic viscosity of the fluid) and Schmidt number (defined as $\textit{Sc}=\nu /D$, where $D$ is the diffusivity of passive scalar transport). The Reynolds number is constrained to the range of 0 ≤ Re ≤ 1, where the prolate spheroid tumbles around its minor axis, aligned with the vorticity axis, in an equilibrium state. Several key findings have emerged: (i) particle inertia significantly influences the uniformity of the spheroid’s tumbling, affecting flow patterns around the spheroid and, consequently, the modes of scalar transport; (ii) both uniform and non-uniform tumbling generate a scalar line in the fluid with elevated scalar concentration, which sweeps through the wake region and merges with clusters of previously formed scalar lines; (iii) fluid passing over the spheroid carries the passive scalar downstream along these scalar lines; (iv) variations in the uniformity of spheroid tumbling result in distinct flow patterns and scalar transport modes, leading to different transport rates; (v) within the studied parameter ranges, increased particle inertia enhances the scalar transport rate; (vi) when particle inertia is minimal, the dimensionless scalar transport rate for different aspect ratios converges to a common dependence on the Péclet number. These phenomena are analysed in detail.

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Type
JFM Papers
Copyright
© The Author(s), 2025. Published by Cambridge University Press

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References

Acrivos, A. 1971 Heat transfer at high Peclet number from a small sphere freely rotating in a simple shear field. J. Fluid Mech. 46, 233240.CrossRefGoogle Scholar
Aidun, C.K., Lu, Y. & Ding, E.J. 1998 Direct analysis of particulate suspensions with inertia using the discrete Boltzmann equation. J. Fluid Mech. 373, 287311.10.1017/S0022112098002493CrossRefGoogle Scholar
Badgujar, K.C. & Bhanage, B.M. 2015 Factors governing dissolution process of lignocellulosic biomass in ionic liquid: current status, overview and challenges. Bioresour. Technol. 178, 218.10.1016/j.biortech.2014.09.138CrossRefGoogle ScholarPubMed
Batchelor, G.K. 1979 Mass transfer from a particle suspended in fluid with a steady linear ambient velocity distribution. J. Fluid Mech. 95, 369400.10.1017/S0022112079001518CrossRefGoogle Scholar
Bhatnagar, P.L., Gross, E.P. & Krook, M. 1954 A model for collision processes in gases. I: small amplitude processes in charged and neutral one-component system. Phys. Rev. 94, 511525.10.1103/PhysRev.94.511CrossRefGoogle Scholar
Binder, R.C. 1939 The motion of cylindrical particles in viscous flow. J. Appl. Phys. 10, 711713.10.1063/1.1707254CrossRefGoogle Scholar
Bouzidi, M., Firdaouss, M. & Lallemand, P. 2001 Momentum transfer of a Boltzmann-lattice fluid with boundaries. Phys. Fluids 13, 34523459.CrossRefGoogle Scholar
Chamolly, A. & Lauga, E. 2019 Stochastic dynamics of dissolving active particles. Eur. Phys. J. E 42, 115.10.1140/epje/i2019-11854-3CrossRefGoogle ScholarPubMed
Chen, S. & Doolen, G.D. 1998 Lattice Boltzmann method for fluid flows. Annu. Rev. Fluid Mech. 30, 329364.10.1146/annurev.fluid.30.1.329CrossRefGoogle Scholar
Costa, P. & Lobo, J.M.S. 2001 Modeling and comparison of dissolution profiles. Eur. J. Pharm. Sci. 13, 123133.10.1016/S0928-0987(01)00095-1CrossRefGoogle ScholarPubMed
Dabade, V., Marath, N.K. & Subramanian, G. 2016 The effect of inertia on the orientation dynamics of anisotropic particles in simple shear flow. J. Fluid Mech. 791, 631703.10.1017/jfm.2016.14CrossRefGoogle Scholar
Decuzzi, P., Pasqualini, R., Arap, W. & Ferrari, M. 2009 Intravascular delivery of particulate systems: does geometry really matter? Pharmaceut. Res. 26, 235243.10.1007/s11095-008-9697-xCrossRefGoogle ScholarPubMed
Ding, E.J. & Aidun, C.K. 2000 The dynamics and scaling law for particles suspended in shear flow with inertia. J. Fluid Mech. 423, 317344.10.1017/S0022112000001932CrossRefGoogle Scholar
Frankel, N.A. & Acrivos, A. 1968 Heat and mass transfer from small spheres and cylinders freely suspended in shear flow. Phys. Fluids 11, 19131918.10.1063/1.1692218CrossRefGoogle Scholar
Frenkel, D. & Ernst, M.H. 1989 Simulation of diffusion in a two-dimesional lattice-gas cellular automation: a set of mode-coupling theory. Phys. Rev. Lett. 56, 21652168.CrossRefGoogle Scholar
Huang, H., Wu, Y. & Lu, X. 2012 Shear viscosity of dilute suspensions of ellipsoidal particles with a lattice Boltzmann method. Phys. Rev. E 86, 046305.CrossRefGoogle ScholarPubMed
Huang, H., Yang, X., Krafczyk, M. & Lu, X.Y. 2012 Rotation of spheroidal particles in Couette flows. J. Fluid Mech. 692, 369394.10.1017/jfm.2011.519CrossRefGoogle Scholar
Jeffery, G.B. 1922 The motion of ellipsoidal particles immersed in a viscous fluid. Proc. R. Lond. A 102, 161179.Google Scholar
Karnis, A., Goldsmith, H.L. & Mason, S.G. 1963 Axial migration of particles in Poiseuille flow. Nature 200, 159160.10.1038/200159a0CrossRefGoogle Scholar
Laadhari, A., Saramito, P. & Misbah, C. 2012 Vesicle tumbling inhibited by inertia. Phys. Fluids 24, 031901.CrossRefGoogle Scholar
Ladd, A.J.C. 1994 Numerical simulations of particulate suspensions via a discretized Boltzmann equation. Part 1. Theoretical foundation. J. Fluid Mech. 271, 285309.10.1017/S0022112094001771CrossRefGoogle Scholar
Lallemand, P. & Luo, L. 2003 Lattice Boltzmann method for moving boundaries. J. Comput. Phys. 184, 406421.10.1016/S0021-9991(02)00022-0CrossRefGoogle Scholar
Lane, D.A. 1993 Visualization of time-dependent flow fields. In Proc. Visual. 93. IEEE.Google Scholar
Lowe, C.P. & Frenkel, D. 1995 The super long-time decay of velocity fluctuations in a two dimensional fluid. Physica A 220, 251260.10.1016/0378-4371(95)00208-OCrossRefGoogle Scholar
Lundell, F. & Carlsson, A. 2010 Heavy ellipsoids in creeping shear flow: transitions of the particle rotation rate and orbit shape. Phys. Rev. E 81, 016323.CrossRefGoogle ScholarPubMed
Masaeli, M., Sollier, E., Amini, H., Mao, W., Camacho, K., Doshi, N., Mitragotri, S., Alexeev, A. & Carlo, D.D. 2012 Continuous inertial focusing and separation of particles by shape. Phys. Rev. X 2, 031017.Google Scholar
Mao, W. & Alexeev, A. 2014 Motion of spheroid particles in shear flow with inertia. J. Fluid Mech. 749, 145166.CrossRefGoogle Scholar
Marath, N.K. & Subramanian, G. 2017 The effect of inertia on the time period of rotation of an anisotropic particle in simple shear flow. J. Fluid Mech. 830, 165210.10.1017/jfm.2017.534CrossRefGoogle Scholar
Marath, N.K. & Subramanian, G. 2018 The inertial orientation dynamics of anisotropic particles in planar linear flows. J. Fluid Mech. 844, 357402.10.1017/jfm.2018.184CrossRefGoogle Scholar
Merks, R.M.H., Hoekstra, A.G. & Sloot, P.M.A. 2002 The momentum propagation method for advection-diffusion in the lattice Boltzmann method: validation and Peclet number limit. J. Comput. Phys. 183, 563576.10.1006/jcph.2002.7209CrossRefGoogle Scholar
Nilsen, C. & Andersson, H.I. 2013 Chaotic rotation of inertial spheroids in oscillating shear flow. Phys. Fluids 25, 013303.CrossRefGoogle Scholar
Petersen, J. 2016 Heap leaching as a key technology for recovery of values from low-grade ores – a brief review. Hydrometallurgy 165, 206212.10.1016/j.hydromet.2015.09.001CrossRefGoogle Scholar
Polyanin, A.D. & Dil’man, V.V. 1985 New methods of the mass and heat transfer theory—II. The methods of asymptotic interpolation and extrapolation. Intl J. Heat Mass Transfer 28, 4558.10.1016/0017-9310(85)90007-9CrossRefGoogle Scholar
Qi, D. & Luo, L.S. 2003 Rotational and orientational behavior of three-dimensional spheroidal particles in Couette flows. J. Fluid Mech. 477, 201213.10.1017/S0022112002003191CrossRefGoogle Scholar
Qian, Y., d’humieres, D. & Lallemand, P. 1992 Lattice BGK models for Navier–Stokes equation. Europhys. Lett. 17, 479484.CrossRefGoogle Scholar
Rosén, T., Lundell, F. & Aidun, C.K. 2014 Effect of fluid inertia on the dynamics and scaling of neutrally buoyant particles in shear flow. J. Fluid Mech. 738, 563590.10.1017/jfm.2013.599CrossRefGoogle Scholar
Rosén, T., Do-Quang, M., Aidun, C.K. & Lundell, F. 2015 Effect of fluid and particle inertia on the rotation of an oblate spheroidal particle suspended in linear shear flow. Phys. Rev. E. 91, 053017.10.1103/PhysRevE.91.053017CrossRefGoogle ScholarPubMed
Rosén, T., Do-Quang, M., Aidun, C.K. & Lundell, F. 2015 The dynamical states of a prolate spheroidal particle suspended in shear flow as a consequence of particle and fluid inertia. J. Fluid Mech. 771, 115158.10.1017/jfm.2015.127CrossRefGoogle Scholar
Saffman, P.G. 1956 On the motion of small spheroidal particles in a viscous liquid. J. Fluid Mech. 1, 540553.10.1017/S0022112056000354CrossRefGoogle Scholar
Salehi, N., Ai-Gousous, J., Mudie, D.M., Amidon, G.L., Ziff, R.M. & Amidon, G.E. 2020 Hierarchical mass transfer analysis of drug particle dissolution, highlighting the hydrodynamics, pH, particle size, and buffer effects for the dissolution of ionizable and nonionizable drugs in a compendial dissolution vessel. Mol. Pharm. 17, 38703884.CrossRefGoogle Scholar
Stover, C.A. & Cohen, C. 1990 The motion of rodlike particles in the pressure-driven flow between two flat plates. Rheol. Acta 29, 192203.10.1007/BF01331355CrossRefGoogle Scholar
Subramanian, G. & Koch, D.L. 2005 Inertial effects on fibre motion in simple shear flow. J. Fluid Mech. 535, 383414.10.1017/S0022112005004829CrossRefGoogle Scholar
Subramanian, G. & Koch, D.L. 2006 a Centrifugal forces alter streamline topology and greatly enhance the rate of heat and mass transfer from neutrally buoyant particles to a shear flow. Phys. Rev. Lett. 96, 134503.10.1103/PhysRevLett.96.134503CrossRefGoogle ScholarPubMed
Subramanian, G. & Koch, D.L. 2006 b Inertial effects on the transfer of heat or mass from neutrally buoyant spheres in a steady linear velocity field. Phys. Fluids 18, 073302.10.1063/1.2215370CrossRefGoogle Scholar
Taylor, G.L. 1923 The motion of ellipsoidal particles in a viscous fluid. Proc. R. Soc. Lond. A 102, 5861.Google Scholar
Wang, Y., Brasseur, J.G., Banco, G.G., Webb, A.G., Ailiani, A.C. & Neuberger, T. 2010 Development of a lattice-Boltzmann method for multiscale transport and absorption with application to intestinal function. In Computational Modeling in Biomechanics (ed. S. De, F. Guilak & R.K.M. Mofrad).Springer.Google Scholar
Wang, Y., Abrahammson, B., Lindfors, L. & Brasseur, J.G. 2012 Comparison and analysis of theoretical models for diffusion-controlled dissolution. Mol. Pharm. 9, 10521066.10.1021/mp2002818CrossRefGoogle ScholarPubMed
Wang, Y., Abrahamsson, B., Lindfors, L. & Brasseur, J.G. 2015 Analysis of diffusion-controlled dissolution from polydisperse collections of drug particles with an assessed mathematical model. J. Pharm. Sci. 104, 29983017.10.1002/jps.24472CrossRefGoogle ScholarPubMed
Wang, Y. & Brasseur, J.G. 2019 Enhancement of mass transfer from particles by local shear-rate and correlations with application to drug dissolution. AIChE J. 65, e16617.10.1002/aic.16617CrossRefGoogle Scholar
Wang, Y., Wan, H., Wei, T., Nevares, D. & Shu, F. 2022 Quasi-steady-state modeling and characterization of diffusion-controlled dissolution from monodisperse prolate and oblate spheroidal particles. Proc. R. Soc. A 478, 20220283.10.1098/rspa.2022.0283CrossRefGoogle Scholar
Wang, Y., Wan, H., Gonzalez Pizarro, R., Lim, S. & Shu, F. 2023 Heat and mass transport from neutrally suspended oblate spheroid in simple shear flow. Phys. Fluids 35, 033319.10.1063/5.0140778CrossRefGoogle Scholar
Yu, Z., Phan-Thien, N. & Tanner, R.I. 2007 Rotation of a spheroid in a Couette flow at moderate Reynolds numbers. Phys. Rev. E 76, 026310.10.1103/PhysRevE.76.026310CrossRefGoogle Scholar
Zettner, C.M. & Yoda, M. 2001 Moderate-aspect-ratio elliptical cylinders in simple shear with inertia. J. Fluid Mech. 442, 241266.CrossRefGoogle Scholar
Zhong, W., Yu, A., Zhou, G., Xie, J. & Zhang, H. 2016 a CFD simulation of dense particulate reaction system: approaches, recent advances and applications. Chem. Engng Sci. 140, 1643.Google Scholar
Zhong, W., Yu, A., Liu, X., Tong, Z. & Zhang, H. 2016 b DEM/CFD-DEM modelling of non-spherical particulate systems: theoretical developments and applications. Powder Technol. 302, 108152.Google Scholar
Supplementary material: File

Wang et al. supplementary movie 1

Evolution of typical streaklines of microtracers released at various locations around a prolate spheroid with $rc/R=3$ and ε=0.4 at $Re=1$ , along with the evolution of scalar concentration on the central x-z plane for $Sc = 100$ .
Download Wang et al. supplementary movie 1(File)
File 6 MB
Supplementary material: File

Wang et al. supplementary movie 2

Evolution of streaklines of microtracers released on the central x-z plane, upstream of a prolate spheroid with $rc/R=3$ and ε=0.4 at $Re=1$ , along with the evolution of scalar concentration on the same plane for $Sc = 100$ .
Download Wang et al. supplementary movie 2(File)
File 3.1 MB
Supplementary material: File

Wang et al. supplementary movie 3

Evolution of typical streaklines of microtracers released at various locations around a prolate spheroid with $rc/R=3$ and ε=40 at $Re=1$ , along with the evolution of scalar concentration on the central x-z plane for $Sc = 100$ .
Download Wang et al. supplementary movie 3(File)
File 8.5 MB
Supplementary material: File

Wang et al. supplementary movie 4

Evolution of streaklines of microtracers released on the central x-z plane, upstream of a prolate spheroid with $rc/R=3$ and ε=40 at $Re=1$ , along with the evolution of scalar concentration on the same plane for $Sc = 100$ .
Download Wang et al. supplementary movie 4(File)
File 4.3 MB