Hostname: page-component-8448b6f56d-gtxcr Total loading time: 0 Render date: 2024-04-19T17:03:03.068Z Has data issue: false hasContentIssue false

Spiral instabilities in the flow of highly elastic fluids between rotating parallel disks

Published online by Cambridge University Press:  26 April 2006

Jeffrey A. Byars
Affiliation:
Department of Chemical Engineering, Massachusetts Institute of Technology, Cambridge, MA 02139, USA
Alparslan Öztekin
Affiliation:
Department of Chemical Engineering, Massachusetts Institute of Technology, Cambridge, MA 02139, USA
Robert A. Brown
Affiliation:
Department of Chemical Engineering, Massachusetts Institute of Technology, Cambridge, MA 02139, USA
Gareth H. Mckinley
Affiliation:
Division of Applied Sciences, Harvard University, Cambridge, MA 02138, USA

Abstract

Experimental observations and linear stability calculations are presented for the stability of torsional flows of viscoelastic fluids between two parallel coaxial disks, one of which is held stationary while the other is rotated at a constant angular velocity. Beyond a critical value of the dimensionless rotation rate, or Deborah number, the purely circumferential, viscometric base flow becomes unstable with respect to a nonaxisymmetric, time-dependent motion consisting of spiral vortices which travel radially outwards across the disks. Video-imaging measurements in two highly elastic polyisobutylene solutions are used to determine the radial wavelength, wavespeed and azimuthal structure of the spiral disturbance. The spatial characteristics of this purely elastic instability scale with the rotation rate and axial separation between the disks; however, the observed spiral structure of the secondary motion is a sensitive function of the fluid rheology and the aspect ratio of the finite disks.

Very near the centre of the disk the flow remains stable at all rotation rates, and the unsteady secondary motion is only observed in an annular region beyond a critical radius, denoted R*1. The spiral vortices initially increase in intensity as they propagate radially outwards across the disk; however, at larger radii they are damped and the spiral structure disappears beyond a second critical radius, R*2. This restabilization of the base viscometric flow is described quantitatively by considering a viscoelastic constitutive equation that captures the nonlinear rheology of the polymeric test fluids in steady shearing flows. A radially localized, linear stability analysis of torsional motions between infinite parallel coaxial disks for this model predicts an instability to non-axisymmetric disturbances for a finite range of radii, which depends on the Deborah number and on the rheological parameters in the model. The most dangerous instability mode varies with the Deborah number; however, at low rotation rates the steady viscometric flow is stable to all localized disturbances, at any radial position.

Experimental values for the wavespeed, wavelength and azimuthal structure of this flow instability are described well by the analysis; however, the critical radii calculated for growth of infinitesimal disturbances are smaller than the values obtained from experimental observations of secondary motions. Calculation of the time rate of change in the additional viscous energy created or dissipated by the disturbance shows that the mechanism of instability for both axisymmetric and non-axisymmetric perturbations is the same, and arises from a coupling between the kinematics of the steady curvilinear base flow and the polymeric stresses in the disturbance flow. For finitely extensible dumb-bells, the magnitude of this coupling is reduced and an additional dissipative contribution to the mechanical energy balance arises, so that the disturbance is damped at large radial positions where the mean shear rate is large.

Hysteresis experiments demonstrate that the instability is subcritical in the rotation rate, and, at long times, the initially well-defined spiral flow develops into a more complex three-dimensional aperiodic motion. Experimental observations indicate that this nonlinear evolution proceeds via a rapid splitting of the spiral vortices into vortices of approximately half the initial radial wavelength, and ultimately results in a state consisting of both inwardly and outwardly travelling spiral vortices with a range of radial wavenumbers.

Type
Research Article
Copyright
© 1994 Cambridge University Press

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

Avgousti, M. & Beris, A. N. 1993 Nonaxisymmetric modes in viscoelastic Taylor–Couette flow. J. Non-Newtonian Fluid Mech. 50, 225251.Google Scholar
Bird, R. B., Armstrong, R. C. & Hassager, O. 1987 a Dynamics of Polymeric Liquids. Volume 1: Fluids Mechanics, 2nd edn. Wiley Interscience.
Bird, R. B., Curtiss, C. F., Armstrong, R. C. & Hassager, O. 1987b Dynamics of Polymeric Liquids. Volume 2: Kinetic Theory, 2nd edn. Wiley Interscience.
Boger, D. V. 1977/ 78 A highly elastic constant-viscosity fluid. J. Non-Newtonian Fluid Mech. 3, 8791.Google Scholar
Chiao, S.-M. F. & Chang, H.-C. 1990 Instability of a Criminale–Ericksen–Filbey fluid in a disk-and-cylinder system. J. Non-Newtonian Fluid Mech. 36, 361394.Google Scholar
Chilcott, M. D. & Rallison, J. M. 1988 Creeping flow of dilute polymer solutions past cylinders and spheres. J. Non-Newtonian Fluid Mech. 29, 381432.Google Scholar
Coates, P. J., Armstrong, R. C. & Brown, R. A. 1992 Calculation of steady state viscoelastic flow through axisymmetric contractions with the EEME formulation. J. Non-Newtonian Fluid Mech. 42, 141188.Google Scholar
Crewther, I., Huilgol, R. R. & Jozsa, R. 1991 Axisymmetric and nonaxisymmetric flows of a non-Newtonian fluid between coaxial rotating disks. Phil. Trans. R. Soc. Lond. A 337, 467495.Google Scholar
Davis, P. J. 1993 Spirals: From Theodorus to Chaos. A. K. Peters. Wellesley, MA.
Ferry, J. D. 1980 Viscoelastic Properties of Polymers, 3rd edn. Wiley Interscience.
Flory, P. J. 1953 Principles of Polymer Chemistry. Cornell University Press.
Giesekus, H. 1965 Sekundärsrömungenin Viskoelastischen Flüssigkeiten bei Stationärer und Periodischer Bewegung. Rheol. Acta 4, 85101.Google Scholar
Göuttlieb, D. & Orszag, S. A. 1977 Numerical Analysis of Spectral Methods: Theory and Applications. Society for Industrial and Applied Mathematics, Bristol, UK.
Goussis, D. A. & Pearlstein, A. J. 1989 Removal of infinite eigenvalues in the generalized matrix eigenvalue problem. J. Comput. Phys. 84, 242246.Google Scholar
Griffiths, D. F., Jones, D. T. & Walters, K. 1969 A flow reversal due to edge effects. J. Fluid Mech. 36, 161175.Google Scholar
Hill, C. T. 1972 Nearly viscometric flow in the disk and cylinder system. II: Experimental. Trans. Soc. Rheol. 16(2), 213245.Google Scholar
Hutton, J. F. 1969 Fracture and secondary flow of elastic liquids. Rheol. Acta 8(1), 5459.Google Scholar
Jackson, J. P., Walters, K. & Williams, R. W. 1984 A rheometrical study of Boger fluids. J. Non-Newtonian Fluid Mech. 14, 173188.Google Scholar
Ji, Z., Rajagopal, K. R. & Szeri, A. Z. 1990 Multiplicity of solutions in von Kármán flows of viscoelastic fluids. J. Non-Newtonian Fluid Mech. 36, 125.Google Scholar
Joo, Y. L. & Shaqfeh, E. S. G. 1991 Viscoelastic Poiseuille flow through a curved channel: a new elastic instability. Phys. Fluids A 3(7), 16911694.Google Scholar
Joo, Y. L. & Shaqfeh, E. S. G. 1992 A purely elastic instability in Dean and Taylor–Dean flow. Phys. Fluids A 4(3), 524543.Google Scholar
Joo, Y. L. & Shaqfeh, E. S. G. 1994 Observations of purely elastic instabilities in the Taylor–Dean flow of a Boger fluid. J. Fluid Mech. 262, 2773.Google Scholar
Kobayashi, R., Kohama, Y. & Takamadate, C. 1980 Spiral vortices in boundary layer transition regime on a rotating disk. Acta Mech 35, 7182.Google Scholar
Larson, R. G. 1992 Instabilities in viscoelastic flows. Rheol. Acta 31, 213263.Google Scholar
Larson, R. G., Muller, S. J. & Shaqfeh, E. S. G. 1994 The effect of fluid rheology on the elastic Taylor–Couette flow instability. J. Non-Newtonian Fluid Mech. 51, 195225.Google Scholar
Larson, R. G., Shaqfeh, E. S. G. & Muller, S. J. 1990 A purely elastic instability in Taylor–Couette flow. J. Fluid Mech. 218, 573600.Google Scholar
Lee, C. S., Tripp, B. C. & Magda, J. J. 1992 Does N1 or N2 control the onset of edge fracture. Rheol. Acta 31, 306398.Google Scholar
McKinley, G. H., Armstrong, R. C. & Brown, R. A. 1993 The wake instability in viscoelastic flow past confined cylinders. Phil. Trans. R. Soc. Lond. 344, 265304.Google Scholar
McKinley, G. H., Byars, J. A., Brown, R. A. & Armstrong, R. C. 1991a Observations on the elastic instability in cone-and-plate and parallel-plate flows of a polyisobutylene Boger fluid. J. Non-Newtonian Fluid Mech. 40, 201229.Google Scholar
McKinley, G. H., Raiford, W. P., Brown, R. A. & Armstrong, R. C. 1991b Nonlinear dynamics of viscoelastic flow in axisymmetric abrupt contractions. J. Fluid Mech. 223, 411456.Google Scholar
Magda, J. J. & Larson, R. G. 1988 A transition occurring in ideal elastic liquids during shear flow. J. Non-Newtonian Fluid Mech. 30, 119.Google Scholar
Magda, J. J., Lou, J., Baek, S.-G. & DeVries, K. L. 1991 Second normal stress difference of a Boger fluid. Polymer 32(11), 20002009.Google Scholar
Malik, M. R. 1986 The neutral curve for stationary disturbances in rotating-disk flow. J. Fluid Mech. 164, 275287.Google Scholar
Merzkirch, W. 1987 Flow Visualization, 2nd edn. Academic.
Muller, S. J., Shaqfeh, E. S. G. & Larson, R. G. 1993 Experimental studies of the onset of oscillatory instability in viscoelastic Taylor–Couette flow. J. Non-Newtonian Fluid Mech. 46, 315330.Google Scholar
Olagunju, D. O. 1994 Effect of free surface and inertia on viscoelastic parallel plate flow. J. Rheol. 38 (1), 151168.Google Scholar
Öztekin, A. & Brown, R. A. 1993 Instability of a visoelastic fluid between rotating parallel disks: analysis for the Oldroyd-B fluid. J. Fluid Mech. 255, 473502.Google Scholar
Phan-Thien, N. 1983 Coaxial-disk flow of an Oldroyd-B fluid: exact solution and stability. J. Non-Newtonian Fluid Mech. 13, 325340.Google Scholar
Phan-Thien, N. 1985 Cone and plate flow of the Oldroyd-B fluids is unstable. J. Non-Newtonian Fluid Mech. 17, 3744.Google Scholar
Prilutski, G., Gupta, R. K., Sridhar, T. & Ryan, M. E. 1983 Model viscoelastic liquids. J. Non-Newtonian Fluid Mech. 12, 233241.Google Scholar
Quinzani, L. M., McKinley, G. H., Brown, R. A. & Armstrong, R. C. 1990 Modeling the Rheology of Polyisobutylene Solutions. J. Rheol. 34(5), 705748.Google Scholar
Russ, J. C. 1992 The Image Processing Handbook. CRC Press, Boca Raton.
Shaqfeh, E. S. G., Muller, S. J. & Larson, R. G. 1992 The effects of gap width and dilute solution properties on the viscoelastic Taylor–Couette instability. J. Fluid Mech. 235, 285317.Google Scholar
Steiert, P. & Wolff, C. 1990 Rheological properties of a polyisobutylene in a kerosene/ polybutene mixture in simple shear flow. J. Non-Newtonian Fluid Mech. 35, 189196.Google Scholar
Tanner, R. I. & Keentok, M. 1983 Shear fracture in cone-plate rheometry. J. Rheol. 27(1), 4757.Google Scholar
Walsh, W. P. 1987 On the flow of a non-Newtonian fluid between rotating co-axial disks. Z. angew. Math. Phys. 38, 495511.Google Scholar
Zandbergen, P. J. & Dijkstra, D. 1987 Von Kármán swirling flows. Ann. Rev. Fluid Mech. 19, 465491.Google Scholar
Zebib, A. 1987 Removal of spurious modes encountered in solving stability problems by spectral methods. J. Comput. Phys. 70, 521525.Google Scholar