A phenomenological viscosity model for steady-state flows of non-Newto
nian polymeric fluids has been proposed based on the assumption of uni
queness of viscosity. The separable dependences of viscosity on the se
cond and third invariants of the rate of deformation tensor represent
the key ingredient of the model, i.e. eta = eta(SH)(II(d))Tr(III(d)).
The model fits experimental data of shear and extensional viscosities
of various polymer melts and solutions. These data show shear-thinning
, extension-thinning, extension-thickening, and extension-thickening w
ith a maximum (and a minimum). The application of the viscosity model
in numerical simulation of contraction flow predicts non-monotonically
increasing vortex enhancement, which is in agreement with experiments
. The third invariant dependence of viscosity which, in the current wo
rk, is not introduced merely to give a large Trouton ratio, is discuss
ed. It is found that the third invariant can vary significantly betwee
n an unadulterated extensional flow and an adulterated one, a fact whi
ch can affect viscosity dramatically.