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Attenuation of shear-layer instabilities in steady and pulsatile axisymmetric shear-thinning flows

Published online by Cambridge University Press:  24 January 2025

Moira Barnes
Affiliation:
Department of Mechanical and Materials Engineering, Queen's University, Kingston, Ontario KL7 3N6, Canada
Giuseppe A. Rosi*
Affiliation:
Institute of Fluid Mechanics, Technische Universität Braunschweig, Braunschweig, Niedersachsen 38108, Germany
David E. Rival
Affiliation:
Department of Mechanical and Materials Engineering, Queen's University, Kingston, Ontario KL7 3N6, Canada Institute of Fluid Mechanics, Technische Universität Braunschweig, Braunschweig, Niedersachsen 38108, Germany
*
Email address for correspondence: [email protected]

Abstract

The current study characterizes the attenuation of instabilities in steady and unsteady shear layers by investigating shear-thinning flows downstream of a confined axisymmetric sudden expansion. Flow fields were captured using particle image velocimetry. Tested fluids exhibited approximate power-law indices of 1, 0.81, 0.61 and 0.47 and measurements were performed at mean throat-based Reynolds numbers of ${Re_m} = 4800$ and 14 400. Unsteady flows were tested at a Strouhal number and amplitude-to-mean velocity ratio of $St = 0.15$ and $\lambda = 0.95$, respectively. For unsteady shear layers, shear-layer roll-up regardless of shear-thinning strength was evidenced by collapse of average circulation over time. For steady shear layers, consistent shear-layer behaviour regardless of shear-thinning strength was evidenced by similar shear-layer trajectories and by growth rates in vorticity thickness. However, vorticity fields of the unsteady and steady shear layers, standard deviations of shear-layer trajectory, thickness of steady shear layers and Reynolds shear-stress spectra of the steady shear layers reveal an attenuation of shear-layer instabilities not captured by Reynolds number. Specifically, shear-layer instabilities exhibit increased diffusion with increasing shear-thinning strength and, in the case of steady shear layers, shear-thinning strength is shown to promote shear-layer stabilization. Also, evidenced by vorticity fields and through Reynolds shear-stress spectra, instabilities frequently coalesce into large rollers, a result that would suggest the presence of an inverse eddy cascade. The behaviour of shear-thinning fluids is shown to stabilize shear layers through attenuating shear-layer instabilities, complementing observations from previous studies showing how shear-thinning fluids promote turbulence in the dominant flow direction.

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

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References

Back, L.H. & Roschke, E.J. 1972 Shear-layer flow regimes and wave instabilities and reattachment lengths downstream of an abrupt circular channel expansion. J. Appl. Mech. 39, 677–681.CrossRefGoogle Scholar
Bentata, O., Anne-Archard, D. & Brancher, P. 2018 Experimental study of low inertia vortex rings in shear-thinning fluids. Phys. Fluids 30, 113103.CrossRefGoogle Scholar
Brown, G.L. & Roshko, A. 1974 On density effects and large structure in turbulent mixing layers. J. Fluid Mech. 64 (4), 775816.CrossRefGoogle Scholar
Castro, O.S. & Pinho, F.T. 1995 Turbulent expansion flow of low molecular weight shear-thinning solutions. Exp. Fluids 20, 42–55.CrossRefGoogle Scholar
Dabiri, J.O. 2009 Optimal vortex formation as a unifying principle in biological propulsion. Annu. Rev. Fluid Mech. 41, 17–33.CrossRefGoogle Scholar
Escudier, M.P., Nickson, A.K. & Poole, R.J. 2009 Turbulent flow of viscoelastic shear-thinning liquids through a rectangular duct: quantification of turbulence anisotropy. J. Non-Newtonian Fluid Mech. 160, 2–10.CrossRefGoogle Scholar
Escudier, M.P. & Smith, S. 1999 Turbulent flow of Newtonian and shear-thinning liquids through a sudden axisymmetric expansion. Exp. Fluids 27, 427434.CrossRefGoogle Scholar
Gharib, M., Rambod, E. & Shariff, K. 1998 A universal time scale for vortex ring formation. J. Fluid Mech. 360, 121140.CrossRefGoogle Scholar
Glezer, A. 1988 The formation of vortex rings. Phys. Fluids 31, 35323542.CrossRefGoogle Scholar
Green, M. 1995 Fluid Vorticies. Kluwer Academic.CrossRefGoogle Scholar
Hussain, A.K.M.F. 1986 Coherent structures and turbulence. J. Fluid Mech. 173, 303356.CrossRefGoogle Scholar
Jeronimo, M. & Rival, D. 2021 On the lifespan of recirculating suspensions with pulsatile flow. J. Fluid Mech. 928, A2.CrossRefGoogle Scholar
Kelessidis, V., Dalamarinis, P. & Maglione, R. 2011 Experimental study and predictions of pressure losses of fluids modeled as Herschel–Bulkley in concentric and eccentric annuli in laminar, transitional and turbulent flows. J. Petrol. Sci. Engng 77 (3), 305312.CrossRefGoogle Scholar
Kheradvar, A., Houle, H., Pedrizzetti, G., Tonti, G., Belcik, T., Ashraf, M., Lindner, J.R., Gharib, M. & Sahn, D. 2010 Echocardiographic particle image velocimetry: a novel technique for quantification of left ventricular blood vorticity pattern. J. Am. Soc. Echocardiogr. 23 (1), 8694.CrossRefGoogle ScholarPubMed
Kumar, S. & Homsy, G. 1999 Direct numerical simulation of hydrodynamic instabilities in two- and three-dimensional viscoelastic free shear layers. J. Non-Newtonian Fluid Mech. 83 (1), 249276.CrossRefGoogle Scholar
Lin, L., Walker, A. & Rival, D.E. 2014 The characterization of a non-Newtonian blood analog in natural- and shear-layer-induced transitional flow. Biorheology 51, 275–291.Google Scholar
Ma, X. & Schröder, A. 2017 Analysis of flapping motion of reattaching shear layer behind a two-dimensional backward-facing step. Phys. Fluids 29 (11), 115104.CrossRefGoogle Scholar
Mrokowska, M.M. & Krzton-Maziopa, A. 2019 Viscoelastic and shear-thinning effects of aqueous exopolymer solution on disk and sphere settling. Sci. Rep. 9, 7897.CrossRefGoogle ScholarPubMed
Nikbakht, A., Madani, A., Olson, J.A. & Martinez, D.M. 2014 Fibre suspensions in Hagen–Poiseuille flow: transition from laminar plug flow to turbulence. J. Non-Newtonian Fluid Mech. 212, 2835.CrossRefGoogle Scholar
Palacios-Morales, C. & Zenit, R. 2013 The formation of vortex rings in shear-thinning liquids. J. Non-Newtonian Fluid Mech. 194, 113.CrossRefGoogle Scholar
Pereira, A. & Pinho, F. 2000 Turbulent characteristics of shear-thinning fluids in recirculating flows. Exp. Fluids 28, 266278.CrossRefGoogle Scholar
Poole, R.J. & Escudier, M.P. 2004 Turbulent flow of viscoelastic liquids through an axisymmetric sudden expansion. J. Non-Newtonian Fluid Mech. 117, 2546.CrossRefGoogle Scholar
Poole, R.J., Escudier, M.P. & Oliveira, P.J. 2005 Laminar flow of a viscoelastic shear-thinning liquid through a plane sudden expansion preceded by a gradual contraction. Proc.: Math. Phys. Engng Sci. 461, 3827–3845.Google Scholar
Raffel, M., Willert, C.E., Scarano, F., Kähler, C.J., Wereley, S.T. & Kompenhans, J. 2018 Particle Image Velocimetry: A Practical Guide. Springer.CrossRefGoogle Scholar
Rahgozar, S. & Rival, D.E. 2017 On turbulence decay of a shear-thinning fluid. Phys. Fluids 29 (12), 123101.CrossRefGoogle Scholar
Rudman, M., Blackburn, H., Graham, L. & Pullum, L. 2004 Turbulent pipe flow of shear-thinning fluids. J. Non-Newtonian Fluid Mech. 118 (1), 3348.CrossRefGoogle Scholar
Stalder, A.F., Frydrychowicz, A., Russe, M.F., Korvink, J.G., Hennig, J., Li, K. & Markl, M. 2011 Assessment of flow instabilities in the healthy aorta using flow-sensitive MRI. J. Magn. Reson. Imag. 33 (4), 839846.CrossRefGoogle ScholarPubMed
Sundin, J., Bustamante, M., Ebbers, T., Dyverfeldt, P. & Carlhäll, C.-J. 2022 Turbulent intensity of blood flow in the healthy aorta increases with dobutamine stress and is related to cardiac output. Front. Physiol. 13 (1), 11.CrossRefGoogle ScholarPubMed
Terrapon, V., Dubief, Y., Moin, P., Shaqfeh, E. & Lele, S. 2004 Simulated polymer stretch in a turbulent flow using Brownian dynamics. J. Fluid Mech. 504, 6171.CrossRefGoogle Scholar
Warholic, M.D., Heist, D.K., Katcher, M. & Hanratty, T.J. 2001 A study with particle-image velocimetry of the influence of drag-reducing polymers on the structure of turbulence. Exp. Fluids 31, 474–483.CrossRefGoogle Scholar
White, C. & Mungal, M. 2008 Mechanics and prediction of turbulent drag reduction with polymer additives. Annu. Rev. Fluid Mech. 40, 556.CrossRefGoogle Scholar
Supplementary material: File

Barnes et al. supplementary movie 1

Shear-layer roll-up occurs downstream of the sudden expansion when unsteady pulsatile boundary conditions are imposed. Representative instantaneous normalized vorticity and velocity vectors are animated for t/T = 0 to 1. In figures(a, c, e, & g): cases at Rem = 4800 are shown, and in figures(b, d, f, & h): cases at Rem = 14400 are shown. Shear-layer roll-up for pure-water cases is shown in figures(a & b), 35PPM in figures(c & d), 450PPM in figures(e & f), and 900PPM in figures(g & h). All cases were prescribed a frequency of St = 0.15. Every third velocity vector is plotted for clarity. With increasing shear-thinning strength, the number of instabilities generally reduce but shear-layer roll-up persists.
Download Barnes et al. supplementary movie 1(File)
File 7.9 MB
Supplementary material: File

Barnes et al. supplementary movie 2

Shear-layer instabilities develop and convect downstream of the sudden expansion when steady boundary conditions are imposed. Representative instantaneous normalized vorticity and velocity vectors are animated to show shear-layer instability formation and evolution. In figures(a, c, e, &g): cases at Rem = 4800 are shown, and in figures(b, d, f, &h): cases at Rem = 14400 are shown. Shear-layer instability formation and evolution for pure-water cases is shown in figures(a & b), 35PPM in figures(c & d), 450PPM in figures(e & f), and 900PPM in figures(g & h). Every third velocity vector is plotted for clarity.
Download Barnes et al. supplementary movie 2(File)
File 9.6 MB