Ts. Creasy et Sg. Advani, A MODEL LONG-DISCONTINUOUS-FIBER FILLED THERMOPLASTIC MELT IN EXTENSIONAL FLOW, Journal of non-Newtonian fluid mechanics, 73(3), 1997, pp. 261-278
The shear cell model works for dilute fiber filled systems in extensio
nal flow. This research investigates the suitability of the idea for h
ighly aligned fibers in a concentrated suspension. A model fiber-fille
d polymer system made from nylon fibers in low-density polyethylene pr
ovided a means of controlling the material parameters. Two systems, wi
th fiber aspect ratios of 20 and 100, containing 50% 0.5 mm fibers by
volume are investigated. The thickness of the polymer layer, i.e. with
fibers this size, allows bulk viscosity data to be compared with the
data from the filled fluid. A weaving process created the discontinuou
s fiber/polyethylene preforms with high alignment of the fibers and wi
th control of the fiber to fiber overlap. Testing the polyethylene in
simple shear and extending the nylon/polyethylene provided the data ne
eded to check the micro mechanics. A cone and plate rheometer and a ca
pillary instrument produced the viscosity/strain rate data that charac
terized the specific polyethylene used in the composite. ir furnace in
set placed in an Instron hydraulic test machine allowed extension of t
he filled system at strain rates from 0.002 to 0.4 s(-1). The shear ex
periments show that the low-density polyethylene is a simple shear-thi
nning melt that provides a good model fluid. The extension of the fill
ed systems I;hows an increase of the apparent extensional viscosity fr
om that of neat polyethylene. Apparent viscosity rises two to three or
ders of magnitude for the systems investigated. The micromechanics all
owed the conversion of the extensional data from the two filled system
s to the shear viscosity of the polymer surrounding the fibers. The ca
lculated polyethylene viscosity compares well with the data from the s
tandard rheometers. The shear cell approach may be applied to highly a
ligned, high fiber-volume-fraction suspensions when the viscosity of t
he polymer is known at the scale of the Sim surrounding each fiber. (C
) 1997 Elsevier Science B.V.