TY - JOUR
T1 - Anisotropy parameter restrictions for the eXtended Pom-Pom model
AU - Baltussen, M.G.H.M.
AU - Verbeeten, W.M.H.
AU - Bogaerds, A.C.B
AU - Hulsen, M.A.
AU - Peters, G.W.M.
PY - 2010
Y1 - 2010
N2 - A significant step forward in modelling polymer melt rheology has been the introduction of the Pom-Pom constitutive model of McLeish & Larson [J. Rheol., 42(1):81¡§C110, 1998]. Various modifications of the Pom-Pom model have been published over the years in order to overcome several inconveniences of the original model. Amongst those modified models, the eXtended Pom-Pom (XPP) model of Verbeeten et. al. [J. Rheol., 45(4):823-843, 2001] has received quite some attention. However, the XPP model has been criticized for the generation of multiple and unphysical solutions. This paper deals with two issues. First, in the XPP model, anisotropy is implemented in a Giesekus-like manner which is known to result in unphysical solutions for non-linear parameter values ¦Á ¡Ý 0.5. Hence, we put forward the conjecture that a similar limitation holds for the XPP model. In the present paper, the limits for the anisotropy parameter are elaborated on and result to be most restraining at high deformation rates where the backbone tube is oriented and the backbone tube stretch approaches the number of arms q. By restricting the anisotropy parameter to a maximum critical value the XPP model produces only one solution, which is the correct physical rheology. In the second part we show that, contrary to the results published by Inkson and Phillips [J. Non-Newton Fluid, 145(2-3):92-101, 2007], for the special case where the anisotropy parameter equals zero, only one physically relevant solution exists in unaxial extensional. In addition to this physically relevant solution, also solutions exist in the physically unattainable part of the conformation space. However, the existence of these physically unattainable solutions is not a unique feature of the XPP model but rather general for non-linear differential type rheological equations.
AB - A significant step forward in modelling polymer melt rheology has been the introduction of the Pom-Pom constitutive model of McLeish & Larson [J. Rheol., 42(1):81¡§C110, 1998]. Various modifications of the Pom-Pom model have been published over the years in order to overcome several inconveniences of the original model. Amongst those modified models, the eXtended Pom-Pom (XPP) model of Verbeeten et. al. [J. Rheol., 45(4):823-843, 2001] has received quite some attention. However, the XPP model has been criticized for the generation of multiple and unphysical solutions. This paper deals with two issues. First, in the XPP model, anisotropy is implemented in a Giesekus-like manner which is known to result in unphysical solutions for non-linear parameter values ¦Á ¡Ý 0.5. Hence, we put forward the conjecture that a similar limitation holds for the XPP model. In the present paper, the limits for the anisotropy parameter are elaborated on and result to be most restraining at high deformation rates where the backbone tube is oriented and the backbone tube stretch approaches the number of arms q. By restricting the anisotropy parameter to a maximum critical value the XPP model produces only one solution, which is the correct physical rheology. In the second part we show that, contrary to the results published by Inkson and Phillips [J. Non-Newton Fluid, 145(2-3):92-101, 2007], for the special case where the anisotropy parameter equals zero, only one physically relevant solution exists in unaxial extensional. In addition to this physically relevant solution, also solutions exist in the physically unattainable part of the conformation space. However, the existence of these physically unattainable solutions is not a unique feature of the XPP model but rather general for non-linear differential type rheological equations.
U2 - 10.1016/j.jnnfm.2010.05.002
DO - 10.1016/j.jnnfm.2010.05.002
M3 - Article
SN - 0377-0257
VL - 165
SP - 1047
EP - 1054
JO - Journal of Non-Newtonian Fluid Mechanics
JF - Journal of Non-Newtonian Fluid Mechanics
IS - 19-20
ER -