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Rheological measurements and transition to turbulence for moderate Reynolds number inertial suspensions

Published online by Cambridge University Press:  31 May 2024

Yichuan Song
Affiliation:
Division of Engineering and Applied Science, California Institute of Technology, Pasadena, CA 91125, USA
Melany L. Hunt*
Affiliation:
Division of Engineering and Applied Science, California Institute of Technology, Pasadena, CA 91125, USA
*
Email address for correspondence: [email protected]

Abstract

Particulate flows at moderate particle Reynolds numbers are important in critical engineering and geological applications. This experimental study explores neutrally buoyant suspensions in an outer-rotating coaxial rheometer for solid fractions, $\phi$, from 0.1 to 0.5, and particle Reynolds number, $Re$, from 0.5 to 800, covering laminar, transitional and turbulent regimes; $Re$ is defined in terms of the square of the particle diameter and the shear rate. For $0.1 < \phi < 0.4$ and $0.5 < Re <10$, the direct torque measurements normalised by the laminar flow torque, $M/M_{lam}$, are independent of $Re$, but depend on $\phi$. For the same range of $\phi$ and for $10< Re<100$, the normalised torques depend on both $\phi$ and $Re$, and show an increasing dependence on $Re$. As $Re$ increases, the flow transitions to turbulence. Small particles delay the turbulent transition for $\phi \leqslant 0.3$, while large particles augment the transition. A modified Reynolds number, $Re^\prime$, that depends linearly on the particle diameter and the maximum velocity, $U_{o}$, is introduced for both laminar and turbulent flows and shows a better correlation of the results as compared with $Re$. For $\phi = 50\,\%$, the normalised torque minus the torque at zero rotational speed is nearly independent of $Re^\prime$. Rheological models based on $Re^\prime$ and the Krieger–Dougherty relative viscosity are proposed in the laminar regime for $10< Re^\prime <500$; in the turbulent regime, a correlation is proposed in terms of $Re^\prime$ and $\phi$ for $1000< Re^\prime < 6000$.

Type
JFM Papers
Copyright
© The Author(s), 2024. Published by Cambridge University Press

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References

Acrivos, A., Fan, X. & Mauri, R. 1994 On the measurements of the relative viscosity of suspensions. J. Rheol. 38 (5), 12851296.CrossRefGoogle Scholar
Agrawal, N., Choueiri, G.H. & Hof, B. 2019 Transition to turbulence in particle laden flows. Phys. Rev. Lett. 122, 114502.CrossRefGoogle ScholarPubMed
Bagnold, R.A. 1954 Experiments on gravity-free dispersion of large solid spheres in a Newtonian fluid under shear. Proc. R. Soc. Lond. A 225, 4963.Google Scholar
Balachandar, S. & Eaton, J.K. 2010 Turbulent dispersed multiphase flow. Annu. Rev. Fluid Mech. 42 (1), 111133.CrossRefGoogle Scholar
Barnes, H.A. 1995 A review of the slip (wall depletion) of polymer solutions, emulsions and particle suspensions in viscometers: its cause, character, and cure. J. Non-Newtonian Fluid Mech. 56 (3), 221251.CrossRefGoogle Scholar
Batchelor, G.K. 1970 The stress system in a suspension of force-free particles. J. Fluid Mech. 41, 545570.CrossRefGoogle Scholar
Boyer, F., Guazzelli, E. & Pouliquen, O. 2011 Unifying suspension and granular rheology. Phys. Rev. Lett. 107, 188301–5.CrossRefGoogle ScholarPubMed
Brandt, L. & Coletti, F. 2022 Particle-laden turbulence: progress and perspectives. Annu. Rev. Fluid Mech. 54 (1), 159189.Google Scholar
Cartellier, A. & Riviere, N. 2001 Effect of particle size on modulating turbulent intensity. Phys. Fluids 13, 21652181.CrossRefGoogle Scholar
Cheng, N. 2008 Formula for the viscosity of a glycerol–water mixture. Ind. Engng Chem. Res. 47, 32853288.CrossRefGoogle Scholar
Coles, D. 1965 Transition in circular Couette flow. J. Fluid Mech. 21, 385424.CrossRefGoogle Scholar
Coles, D. & VanAtta, C. 1966 Measured distortion of a laminar circular Couette flow by end effects. J. Fluid Mech. 25, 513521.Google Scholar
Dash, A., Anantharaman, A. & Poelma, C. 2020 Particle-laden Taylor–Couette flows: higher order transitions and evidence for azimuthally localized wavy vortices. J. Fluid Mech. 903, A20.Google Scholar
Ellenberger, J. & Fortuin, J.M.H. 1985 A criterion for purely tangential laminar flow in the cone-and-plate rheometer and the parallel-plate rheometer. Chem. Engng Sci. 40, 111116.CrossRefGoogle Scholar
Ernst, R.C., Watkins, C.H. & Ruwe, H.H. 1936 The physical properties of the ternary system ethyl alcohol-glycerin-water. J. Phys. Chem. A 40, 5.Google Scholar
Gallier, S., Lemaire, E., Lobry, L. & Peters, F. 2016 Effect of confinement in wall-bounded non-colloidal suspensions. J. Fluid Mech. 799, 100127.CrossRefGoogle Scholar
Gore, R.A. & Crowe, C.T. 1989 Effect of particle size on modulating turbulent intensity. Intl J. Multiphase Flow 15, 279285.CrossRefGoogle Scholar
Haddadi, H. & Morris, J.F. 2014 Microstructure and rheology of finite inertia neutrally buoyant suspensions. J. Fluid Mech. 749, 431459.CrossRefGoogle Scholar
Hunt, M.L. & Zenit, R. 2024 Beyond Bagnold: rheological measurements of inertial suspensions. Intl J. Multiphase Flow (submitted).Google Scholar
Hunt, M.L., Zenit, R., Campbell, C.S. & Brennen, C.E. 2002 Revisiting the 1954 suspension experiments of R.A. Bagnold. J. Fluid Mech. 452, 124.CrossRefGoogle Scholar
Iverson, R.M. 2012 Elementary theory of bed-sediment entrainment by debris flows and avalanches. J. Geophys. Res. 117 (F03006), 117.CrossRefGoogle Scholar
Koos, E., Linares-Guerrero, E., Hunt, M.L. & Brennen, C.E. 2012 Rheological measurements of large particles in high shear rate flows. Phys. Fluids 24, 013302.CrossRefGoogle Scholar
Kulkarni, P.M. & Morris, J.F. 2008 Suspension properties at finite Reynolds number from simulated shear flow. Phys. Fluids 20, 40602.CrossRefGoogle Scholar
Larson, R.G. 1999 The Structure and Rheology of Complex Fluids. Oxford University Press.Google Scholar
Lashgari, I., Picano, F., Breugem, W. & Brandt, L. 2014 Laminar, turbulent, and inertial shear-thickening regimes in channel flow of neutrally buoyant particle suspensions. Phys. Rev. Lett. 113, 254502.Google ScholarPubMed
Leskovec, M., Lundell, F. & Innings, F. 2020 Pipe flow with large particles and their impact on the transition to turbulence. Phys. Rev. Fluids 5, 112301.CrossRefGoogle Scholar
Linares, E., Hunt, M. & Zenit, R. 2017 Effects of inertia and turbulence on rheological measurements of neutrally buoyant suspensions. J. Fluid Mech. 811, 525543.CrossRefGoogle Scholar
Majji, M.V. & Morris, J.F. 2018 Inertial migration of particles in Taylor–Couette flows. Phys. Fluids 30, 033303.CrossRefGoogle Scholar
Matas, J.P., Morris, J.F. & Guazzelli, E. 2003 Transition to turbulence in particulate pipe flow. Phys. Rev. Lett. 90 (1), 014501.CrossRefGoogle ScholarPubMed
Mendez-Diaz, S., Serrano-Garcia, J.C., Zenit, R. & Hernandez-Cordero, J.A. 2013 Power spectral distributions of pseudo-turbulent bubbly flows. Phys. Fluids 25, 043303.CrossRefGoogle Scholar
Moazzen, M., Lacassagne, T., Thomy, V. & Bahrani, S.A. 2022 Torque scaling at primary and secondary bifurcations in a Taylor–Couette flow of suspensions. J. Fluid Mech. 937, A2.CrossRefGoogle Scholar
Osiptsov, A.A. 2017 Fluid mechanics of hydraulic fracturing: a review. J. Petrol. Sci. Engng 156, 513535.CrossRefGoogle Scholar
Picano, F., Breugem, W.P., Mitra, D. & Brandt, L. 2013 Shear thickening in non-Newtonian suspensions: an excluded volume effect. Phys. Rev. Lett. 111, 98302.CrossRefGoogle Scholar
Rahmani, M., Hammouti, A. & Wachs, A. 2018 Momentum balance and stresses in a suspension of spherical particles in a plane Couette flow. Phys. Fluids 30, 043301.CrossRefGoogle Scholar
Ramesh, P., Bharadwaj, S. & Alam, M. 2019 Suspension Taylor–Couette flow: co-existence of stationary and travelling waves, and the characteristics of Taylor vortices and spirals. J. Fluid Mech. 870, 901940.CrossRefGoogle Scholar
Ravelet, F., Delfos, R. & Westerweel, J. 2010 Influence of global rotation and Reynolds number on the large-scale features of a turbulent Taylor–Couette flow. Phys. Fluids 22, 055103.CrossRefGoogle Scholar
Savage, S.B. & McKeown, S. 1983 Shear stresses developed during rapid shear of concentrated suspensions of large spherical particles between concentric cylinders. J. Fluid Mech. 127, 453472.CrossRefGoogle Scholar
Schlichting, H. 1951 Boundary Layer Theory, 7th edn. McGraw Hill.Google Scholar
Song, Y. 2022 Rheological measurements in moderate Reynolds number liquid–solid flows. PhD thesis, California Institute of Technology.Google Scholar
Stickel, J.J., Knutsen, J.R., Liberatore, M.W., Luu, W., Bousfield, D.W., Klingenberg, D.R., Scott, C.T., Root, T.W., Ehrhardt, M.R. & Monz, T.O. 2009 Rheology measurements in a biomass slurry: an inter-labotory study. Rheol. Acta 48, 10051015.CrossRefGoogle Scholar
Stickel, J.J. & Powell, R.L. 2005 Fluid mechanics and rheology of dense suspensions. Annu. Rev. Fluid Mech. 37 (1), 129149.CrossRefGoogle Scholar
Tapia, F., Ichihara, M., Pouliquen, O. & Guazzelli, E. 2022 Viscous to inertial transition in dense granular suspension. Phys. Rev. Lett. 129, 078001.Google ScholarPubMed
Taylor, G.I. 1936 a Fluid friction between rotating cylinders, I. Torque measurements. Proc. R. Soc. Lond. A 157 (892), 546564.Google Scholar
Taylor, G.I. 1936 b Fluid friction between rotating cylinders, II. Distribution of velocity between concentric cylinders when outer one is rotating and inner one is at rest. Proc. R. Soc. Lond. A 157 (892), 565578.Google Scholar
VanAtta, C. 1966 Exploratory measurements in spiral turbulence. J. Fluid Mech. 25, 495512.Google Scholar
Yang, F.L. & Hunt, M.L. 2006 Dynamics of particle-particle collisions in a viscous liquid. Phys. Fluids 18, 121506.CrossRefGoogle Scholar
Yeo, K. & Maxey, M.R. 2013 Dynamics and rheology of concentrated, finite-Reynolds-number suspensions in a homogeneous shear flow. Phys. Fluids 25, 533303.CrossRefGoogle Scholar
Young, A.B., Shetty, A. & Hunt, M.L. 2024 Flow transitions and effective properties in multiphase Taylor–Couette flow. J. Fluid Mech. 983, A14.CrossRefGoogle Scholar
Yousefi, A., Costa, P., Picano, F. & Brandt, L. 2023 On the role of inertia in channel flows of finite-size neutrally-buoyant particles. J. Fluid Mech. 955, A30.CrossRefGoogle Scholar
Yu, Z., Wu, T., Shao, X. & Lin, J. 2013 Numerical studies of the effects of large neutrally buoyant particles on the flow instability and transition to turbulence in pipe flow. Phys. Fluids 25, 043305.CrossRefGoogle Scholar
Zhou, G. & Prosperetti, A. 2020 Inertial effects in a shear flow of fluid particle mixture: resolved simulations. Phys. Rev. Fluids 5, 0803401.CrossRefGoogle Scholar