Hostname: page-component-78c5997874-m6dg7 Total loading time: 0 Render date: 2024-11-08T05:32:40.122Z Has data issue: false hasContentIssue false

The effects of gap width and dilute solution properties on the viscoelastic Taylor-Couette instability

Published online by Cambridge University Press:  26 April 2006

Eric S. G. Shaqfeh
Affiliation:
Department of Chemical Engineering, Stanford University, Stanford, CA 94305-5025, USA
Susan J. Muller
Affiliation:
AT & T Bell Laboratories, 600 Mountain Avenue, Murray Hill, NJ 07974, USA
Ronald G. Larson
Affiliation:
AT & T Bell Laboratories, 600 Mountain Avenue, Murray Hill, NJ 07974, USA

Abstract

The effects of finite gap and various dilute solution properties on the previously studied purely elastic Taylor-Couette instability reported by Muller et al. (1989) and Larson et al. (1990) are investigated. The dilute solution properties which we consider are the ratio of the second to the first normal stress coefficient, ψ21, and the ratio of the solvent to the polymer contribution to the shear viscosity, S. Linear stability predictions for the flow of an Oldroyd-B fluid are presented over a wide range of Deborah number, De, gap ratio, ε, and S. In addition, the Oldroyd-B model is modified to include second normal stress differences, and new stability predictions are presented for small negative and small positive ψ21. Both the critical conditions and changes in the flow structure are presented. It is demonstrated that finite-gap effects are stabilizing even for relatively small gap ratios (0 < ε < 0.35). Furthermore, it is shown that there are two possible flow structures which can be chosen near the onset of instability: a standing wave structure (i.e. radially propagating vortices) or a travelling wave (i.e. vortices propagating up or down the coaxial cylinders). However, the strength and both the axial and radial dimensions of these vortices depend markedly on the gap, with both dimensions decreasing as the gap ratio increases. Thus, the number of vortices filling the gap increases with the gap ratio.

In a second study, we show that the instability is sensitive to the presence of second normal stress differences. Positive second normal stress differences are shown to be destabilizing, while negative differences are strongly stabilizing. Furthermore, when both finite-gap effects and small negative second normal stress differences are included, the predicted gap dependence of the critical De is in good agreement with previous measurements on the flow of a dilute polyisobutylene solution. Finally, we present new measurements of the critical values of the De for a series of dilute, viscous polystyrene solutions, for which ψ2 was found to be near zero. We find that as the polymer concentration increases (and therefore S decreases) the critical Deborah number decreases, in qualitative agreement with the theoretical predictions.

Type
Research Article
Copyright
© 1992 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

Berry, G. C. 1967 Thermodynamic and conformation properties of polystyrene. II. Intrinsic viscosity studies on dilute solutions of linear polystyrenes. J. Chem. Phys. 46, 13381352.Google Scholar
Boger, D. V. 1977/78 A highly elastic constant-viscosity fluid. J. Non-Newtonian Fluid Mech. 3, 8791.Google Scholar
Drazin, P. G. & Reid, W. H. 1981 Hydrodynamic Stability. Cambridge University Press.
Giesekus, H. 1966 Zur stabilitat von stromungen viskoelastischer Flussigkeiten. Rheol. Acta 5, 239252.Google Scholar
Giesekus, H. 1972 On instabilities in Poiseuille and Couette flows of viscoelastic fluids. Prog. Heat Mass Transfer 5, 187193.Google Scholar
Ginn, R. F. & Denn, M. M. 1969 Rotational stability in viscoelastic liqids. AIChE J. 15, 450454.Google Scholar
Huerre, P. & Monkewitz, P. A. 1985 Absolute and convective instabilities in free shear layers. J. Fluid Mech. 159, 151168.Google Scholar
Keentok, M., Georgescu, A. G., Sherwood, A. A. & Tanner, R. I. 1980 The measurement of the second normal stress difference for some polymer solutions. J. Non-Newtonian Fluid Mech. 6, 303324.Google Scholar
Larson, R. G. 1988 Constitutive Equations for Polymer Melts and Solutions, pp. 33, 120121, 136. Butterworths.
Larson, R. G., Muller, S. J. & Shaqfeh, E. S. G. 1991 The elastic Taylor-Couette instability for rheologically complex fluids. J. Non-Newtonian Fluid Mech. (to be submitted).Google Scholar
Larson, R. G., Shaqfeh, E. S. G. & Muller, S. J. 1990 A purely viscoelastic instability in Taylor-Couette flow. J. Fluid Mech. 218, 573600 (referred to herein as II).Google Scholar
Laun, H. M. & Hingmann, R. 1990 Rheological characterization of the fluid M1 and of its components. J. Non-Newtonian Fluid Mech. 35, 137157.Google Scholar
Lee, C. S., Magda, J. J., Muller, S. J. & Larson, R. G. 1991 Dependence of 2nd normal stress differences on polymer concentration. Natl AIChE Meeting, Session on Advances in Rheology (Abstract Submitted).
Magda, J. J., Lou, J., Back, S. G. & DeVries, K. L. 1991 The second normal stress difference of a Boger fluid. Polymer (to appear).Google Scholar
Muller, S. J., Larson, R. G. & Shaqfeh, E. S. G. 1989 A purely elastic transition in Taylor-Couette flow. Rheol. Acta, 28, 499503 (referred to herein as I).Google Scholar
Northey, P., Armstrong, R. C. & Brown, R. A. 1990 Finite-element calculation of purely elastic, nonlinear transitions in circular Couette flow. Paper 167j, Annual AIChE Meeting, November, 1990.
Northey, P., Brown, R. A. & Armstrong, R. C. 1989 Numerical calculation of time-dependent, two-dimensional inertial flows described by a multimode UCM model, Paper 166Adb, Annual AIChE Meeting, November, 1989.Google Scholar
Quinzani, L. M., McKinley, G. H., Brown, R. A. & Armstrong, R. C. 1991 Modeling the rheology of polyisobutylene solutions. J. Rheol. 34, 705748.Google Scholar
Taylor, G. I. 1923 Stability of a viscous liquid contained between two rotating cylinder. Phil. Trans. R. Soc. Lond. A 223, 289343.Google Scholar