Normal-stress difference

In simple shear, the first and second normal-stress differences are $N_1={\tau }_{xx}-{\tau }_{yy}$ and $N_2={\tau }_{yy}-{\tau }_{zz}$.

A polymeric extrudate can expand sideways after leaving a die as the normal-stress differences and stored deformation generated upstream relax. Axial elastic recovery contributes to transverse swelling in an incompressible flow. A Newtonian extrudate can also swell through rearrangement of its velocity profile, so observing swelling alone does not isolate the elastic contribution.

A rotating rod can draw a liquid with appreciable viscoelasticity inward and raise its free surface around the rod. Tensile normal stresses along curved flow lines produce an inward hoop force, competing with inertia and gravity. It is a manifestation of elastic normal-stress differences, rather than merely a changed scalar shear viscosity.