J. Non-Newtonian Fluid Mech., 75 (1998) 1–23
A finite element method for computing the flow of multi-mode
viscoelastic fluids: comparison with experiments
C. Be ´raudo
a
, A. Fortin
b
, T. Coupez
a
, Y. Demay
c
, B. Vergnes
a
, J.F. Agassant
a,
*
a
Centre de Mise en Forme des Mate ´riaux, URA CNRS 1374, E
´
cole des Mines de Paris,
BP 207 06904 Sophia Antipolis Cedex, France
b
De ´partement de Mathe ´matiques et de Ge ´nie Industriel, E
´
cole Polytechnique de Montre ´al, C.P. 6079,
Succursale Centre -Ville, H3C 3A7 Montre ´al, Canada
c
Institut Non Line ´aire de Nice, UMR CNRS 129, 1361, route des Lucioles, 06560 Valbonne, France
Received 3 February 1997; received in revised form 9 September 1997
Abstract
The numerical computation of viscoelastic fluid flows with differential constitutive equations presents various
difficulties. The first one lies in the numerical convergence of the complex numerical scheme solving the non-linear set
of equations. Due to the hybrid type of these equations (elliptic and hyperbolic), geometrical singularities such as
reentrant corner or die induce stress singularities and hence numerical problems. Another difficulty is the choice of
an appropriate constitutive equation and the determination of rheological constants. In this paper, a quasi-Newton
method is developed for a fluid obeying a multi-mode Phan-Thien and Tanner constitutive equation. A confined
convergent geometry followed by the extrudate swell has been considered. Numerical results obtained for two-dimen-
sional or axisymmetric flows are compared to experimental results (birefringence patterns or extrudate swell) for a
linear low density polyethylene (LLDPE) and a low density polyethylene (LDPE). © 1998 Elsevier Science B.V.
Keywords: Viscoelastic fluid flows; Geometrical singularities; Extrudate swell; Birefringence patterns
1. Introduction
The numerical simulation of polymer processing needs to take into account their complex
viscoelastic rheological behavior. A large number of constitutive equations have been proposed
and the selection of an adequate model is obviously a critical step in the simulation of
viscoelastic flows. Different criteria have to be considered but the constitutive equation should
at least give satisfactory predictions in simple rheometrical flows. Furthermore, a numerical
solution of the resulting governing set of equations must be possible. Generally speaking,
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