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On the (de)stabilization of draw resonance due to cooling

Published online by Cambridge University Press:  25 September 2009

BENOIT SCHEID*
Affiliation:
School of Engineering and Applied Sciences, Harvard University, Cambridge, MA 02138, USA
SARA QUILIGOTTI
Affiliation:
Saint-Gobain Recherche, 39 Quai Lucien Lefranc, B.P. 135, 93303 Aubervilliers Cedex, France
BINH TRAN
Affiliation:
Saint-Gobain Recherche, 39 Quai Lucien Lefranc, B.P. 135, 93303 Aubervilliers Cedex, France
RENÉ GY
Affiliation:
Saint-Gobain Recherche, 39 Quai Lucien Lefranc, B.P. 135, 93303 Aubervilliers Cedex, France
HOWARD A. STONE
Affiliation:
School of Engineering and Applied Sciences, Harvard University, Cambridge, MA 02138, USA
*
Email address for correspondence: [email protected]

Abstract

We study the drawing of a Newtonian viscous sheet under the influence of cooling with temperature dependence of the viscosity. Classically this problem has an instability called draw resonance, when the draw ratio Dr, which is the ratio of the outlet velocity relative to the inlet velocity, is beyond a critical value Drc. The heat transfer from the surface compared to the bulk energy advection is conveniently measured by the Stanton number St. Usual descriptions of the problem are one-dimensional and rigorously apply for St ≤ 1. The model presented here accounts for variations of the temperature across the sheet and has therefore no restriction on St. Stability analysis of the model shows two different cooling regimes: the ‘advection-dominated’ cooling for St ≪ 1 and the ‘transfer-dominated’ cooling for St ≫ 1. The transition between those two regimes occurs at St = O(1) where the stabilizing effect due to cooling is most efficient, and for which we propose a mechanism for stabilization, based on phase shifts between the tension and axial-averaged flow quantities. Away from this transition, the sheet is always shown to be unstable at smaller draw ratios. Additionally, in the limit of St → ∞, the heat exchange is such that the temperature of the fluid obtains the far-field temperature, which hence corresponds to a ‘prescribed temperature’ regime. This dynamical situation is comparable to the isothermal regime in the sense that the temperature perturbation has no effect on the stability properties. Nevertheless, in this regime, the critical draw ratio for draw resonance can be below the classical value of Drc = 20.218 obtained in isothermal conditions.

Type
Papers
Copyright
Copyright © Cambridge University Press 2009

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References

REFERENCES

Barot, G. & Rao, I. J. 2004 Modeling the film casting process using a continuum model for crystallization in polymers. Intl J. Nonlinear Mech. 40, 939955.CrossRefGoogle Scholar
Buckmaster, J. D., Nachman, A. & Ting, L. 1975 The buckling and stretching of a viscida. J. Fluid Mech. 69, 120.CrossRefGoogle Scholar
Cao, F., Khayat, R. E. & Puskas, J. E. 2005 Effect of inertia and gravity on the draw resonance in high-speed film casting of Newtonian fluids. Intl J. Solids Struct. 42, 57345757.CrossRefGoogle Scholar
Dewynne, J. N., Ockendon, J. R. & Wilmott, P. 1992 A systematic derivation of the leading-order equations for extensional flows in slender geometries. J. Fluid Mech. 244, 323338.CrossRefGoogle Scholar
Doedel, E. J., Champneys, A., Fairfrieve, T., Kuznetsov, Y., Sandstede, B. & Wang, X. 1997 Auto97 continuation and bifurcation software for ordinary differential equations. Montreal Concordia University. Auto software is freely distributed on http://indy.cs.concordia.ca/auto/.Google Scholar
Fisher, R. J. & Denn, M. M. 1977 Mechanics of nonisothermal polymer melt spinning. AIChE 23, 2328.CrossRefGoogle Scholar
Forest, M. G., Zhou, H. & Wang, Q. 2000 Thermotropic liquid crystalline polymer fibres. SIAM J. Appl. Math. 60, 11771204.Google Scholar
Gelder, D. 1971 The stability of fibre drawing processing. Ind. Engng Chem. Fundam. 10, 534535.CrossRefGoogle Scholar
Geyling, F. T. & Homsy, G. M. 1980 Extensional instabilities of glass fibre drawing process. Glass Tech. 21, 95102.Google Scholar
Gupta, G. K., Schultz, W. W., Arruda, E. M. & Lu, X. 1996 Nonisothermal model of glass fibre drawing stability. Rheol. Acta 35, 584596.CrossRefGoogle Scholar
Howell, P. D. 1996 Models for thin viscous sheets. Euro. J. Appl. Math. 7, 321343.CrossRefGoogle Scholar
Hyun, J. C. 1978 Theory of draw resonance. AIChE 24, 418422.CrossRefGoogle Scholar
Hyun, J. C. 1999 Draw resonance in polymer processing: a short chronology and a new approach. Korean–Australia Rheol. J. 11, 279285.Google Scholar
Jung, H. W., Choi, S. M. & Hyun, J. C. 1999 Approximate method for determining the stability of the film-casting process. AIChE 45, 11571160.CrossRefGoogle Scholar
Jung, H. W., Song, H.-S. & Hyun, J. C. 2000 Draw resonance and kinematic waves in viscoelastic isothermal spinning. AIChE 46, 21062111.CrossRefGoogle Scholar
Kase, S., Matsuo, T. & Yoshimoto, Y. 1966 Theoretical analysis of melt spinning. Part 2. Surging phenomena in extrusion casting of plastic films. Seni Kikai Gakkai Shi 19, T63.Google Scholar
Kim, B. M., Hyun, J. C., Oh, J. S. & Lee, S. J 1996 Kinematic waves in the isothermal melt spinning of Newtonian fluids. AIChE 42, 31643169.CrossRefGoogle Scholar
Lee, J. S., Jung, H. W. & Hyun, J. C. 2005 Simple indicator of draw resonance instability in melt spinning processes. AIChE 51, 28692874.CrossRefGoogle Scholar
Minoshima, W. & White, J. L. 1983 Stability of continuous film extrusion processes. Polym. Engng Rev. 2, 211226.Google Scholar
Pearson, J. R. A. 1985 Mechanics of Polymer Processing. Elsevier Applied Science Publishers.Google Scholar
Pearson, J. R. A. & Matovich, M. A. 1969 Spinning a molten threadline – Stability. Ind. Engng Chem. Fundam. 8, 605609.CrossRefGoogle Scholar
Renardy, M. 2006 Draw resonance revisited. SIAM J. Appl. Math. 66, 12611269.CrossRefGoogle Scholar
Shah, Y. T. & Pearson, J. R. A. 1972 a On the stability of nonisothermal fibre spinning. Ind. Engng Chem. Fundam. 11, 145149.CrossRefGoogle Scholar
Shah, Y. T. & Pearson, J. R. A. 1972 b On the stability of nonisothermal fibre spinning – General case. Ind. Engng Chem. Fundam. 11, 150153.CrossRefGoogle Scholar
Shin, D. M., Lee, J. S., Kim, J. M., Jung, H. W. & Hyun, J. C. 2007 Transient and steady-state solutions of 2d viscoelastic nonisothermal simulation model of film casting process via finite element method. J. Rheol. 51, 393407.CrossRefGoogle Scholar
Silagy, D., Demay, Y. & Agassant, J.-F. 1996 Study of the stability of the film casting process. Polym. Engng Sci. 36, 26142625.CrossRefGoogle Scholar
Smith, S. & Stolle, D. 2000 Nonisothermal two-dimensional film casting of a viscous polymer. Polym. Engng Sc. 40, 18701877.CrossRefGoogle Scholar
Smith, S. & Stolle, D. 2003 Numerical simulation of film casting using an updated Lagrangian finite element algorithm. Polym. Engng Sc. 43, 11051122.CrossRefGoogle Scholar
Sollogoub, C., Demay, Y. & Agassant, J.-F. 2006 Non-isothermal viscoelastic numerical model of the cast-film process. J. Non-Newtonian Fluid Mech. 138, 7686.CrossRefGoogle Scholar
Willien, J.-L., Demay, Y. & Agassant, J.-F. 1988 Stretching stability analysis of a Newtonian fluid: application to polymer spinning and glass drawing. J. Theor. Appl. Mech. 7, 719739.Google Scholar
Wylie, J. J., Huang, H. & Miura, R. M. 2007 Thermal instability in drawing viscous threads. J. Fluid Mech. 570, 116.CrossRefGoogle Scholar
Yeow, Y. L. 1974 On the stability of extending films: a model for the film casting process. J. Fluid Mech. 66, 613622.CrossRefGoogle Scholar
Zheng, H., Yu, W., Zhou, C. & Zhang, H. 2006 Three-dimensional simulation of the non-isothermal cast film process of polymer melts. J. Polym. Res. 13, 433440.CrossRefGoogle Scholar