Use of lubricated skin/core flow of a polymer melt and a hyperbolic sh
aped converging die are shown to result in essentially pure elongation
al flow at a constant elongational strain rate. This behavior is demon
strated first by modeling a series of skin/core layered flows: power-l
aw rectangular channel shearing flow; Newtonian fluid converging chann
el elongational flow; and power-law fluid converging channel elongatio
nal flow. Experimental measurements using tracer particles and an imag
e analysis system confirm the predicted behavior and demonstrate the a
bility to achieve a constant elongational strain rate in the core laye
r. The constant value is controlled by the volumetric flow rate and di
e geometry in this confined flow. The viscosity ratio of the core poly
mer must be at least 100 times that of the core and the converging flo
w channel must have a specific hyperbolic shape. A Dowex low-density p
olyethylene skin and a Marlex polypropylene core were used for the exp
erimental measurements and for the rheological parameters used in the
modeling.