Model liquids with nearly constant viscosity and adjustable elasticity
are needed to resolve the role of elasticity in coating and other fre
e-surface flows. Available Boger liquids are not well suited to free-s
urface flows, because they are solutions in organic solvents and their
viscosities exceeding 1 Pa.s fall on the high side. Aqueous liquids a
re preferred in laboratory studies partly due to environmental hazards
. Aqueous polymer solutions with constant shear viscosity and adjustab
le elasticity were prepared by adding small amounts of a high-molecula
r-weight polymer to a more concentrated aqueous solution of the same p
olymer but of a much lower molecular weight. Up to 0.2 wt. % of high-m
olecular weight poly(ethylene oxide) (PEO, M-w from 400,000 to 4 milli
on g/mol) was added to almost inelastic solutions of low-MW polyethyle
ne glycol (PEG, M-n= 8,000 g/mol). PEG concentrations in these solutio
ns varied between 16.7 and 42.9 wt. %. Shear viscosities of these solu
tions ranged from about 0.02 to 0.3 Pa.s and were constant lip to shea
r rates of 100 s(-1). The stress ratio is one measure of the elasticit
y of the liquid. Stress ratios up to 0.2 were estimated from small-amp
litude oscillatory measurements. Terminal behavior (elastic modulus ri
sing with the square of the frequency) was not observed even at 10(-2)
rad/s. Viscosity and elasticity of the liquids can be manipulated ove
r a wide range by varying the amounts and molecular weights of PEG and
PEO within the unentangled and dilute regions of the concentration-mo
lecular weight diagram, respectively. Fits of experimental data to can
didate differential and integral constitutive equations are also discu
ssed.