We report new evidence of secondary flow during plane Couette shearing
of entangled polystyrene solutions and an entangled polyisobutylene m
elt. The secondary how is shown to be driven by normal stress imbalanc
es at the free edges of the materials, and is accompanied by spatial v
ariations in birefringence. In the polymer solutions, the secondary fl
ow, though unmistakable, is weak and is only apparent from tracer part
icle visualization experiments using a video microscopy technique. In
the polymer melt, however, secondary flow is much stronger and causes
gross shape changes in sheared samples that are easily visualized with
the naked eye. We also show that several details of the plane Couette
secondary flow are correctly predicted by a simple differential const
itutive equation in the narrow gap approximation. Our findings suggest
that the secondary flow's effect on sliding plate rheological measure
ments could be minimized by (a) using large plates with narrow gaps, i
.e., small sample aspect ratios; (b) performing measurements at low We
issenberg numbers (Wi = tau(L) gamma); and (c) employing measuring tec
hniques such as laser birefringence that permit stresses to be determi
ned close to the center of the shearing surfaces of the plane Couette
cell. In addition to secondary flow, we find significant levels of sli
p during steady shearing of entangled polystyrene solutions. The slip,
though qualitatively similar to the entangled slip predictions of Bro
chard and deGennes [Langmuir 8, 3033-3037(1992)], is unusual because a
t low slip velocities V-s the slip lengths b = V-s/gamma are of the or
der of 150 mu m, which is much larger than expected for entangled slip
. Furthermore, slip in the solutions is shown to be nonisotropic with
the slip velocity manifesting a similar shear rate dependence to the b
irefringence. These findings suggest that the slip law for entangled p
olymers may be more complex than previously thought. (C) 1996 Society
of Rheology.