A. Luciani et al., INTERFACIAL-TENSION COEFFICIENT FROM THE RETRACTION OF ELLIPSOIDAL DROPS, Journal of polymer science. Part B, Polymer physics, 35(9), 1997, pp. 1393-1403
A new method for the determination of the interfacial tension coeffici
ent between two immiscible fluids is proposed. The method is particula
rly useful for the binary polymer blends. The deformed drop retraction
method, DDRM, makes it possible to determine the dynamic interfacial
tension coefficient, nu, from the time evolution of a distorted fluid
drop toward its equilibrium form. Analysis of this interfacial tension
-driven process led to a theoretical relation between the shape retrac
tion rate and the system's geometrical and rheological characteristics
. Measurements of either low viscosity model systems or high viscosity
industrial polymer mixtures led to a good agreement with values obtai
ned from the widely used breaking thread method. DDRM enables to measu
re nu in polymeric blends of commercial interest-the high viscosity sy
stems that would be very difficult to characterize by other techniques
. Furthermore, for the first time it is possible to follow the time de
pendence of the interfacial tension coefficient, thus unambiguously de
termine the dynamic and equilibrium values of nu(12). For example, in
low density polyethylene blends with polystyrene, LDPE/PS, nu decrease
d with the polymer-polymer contact time, t(c), from nu = 6.9 mN/m at t
(c) = 12 min, to nu = 5.2 mN/m at t(c) greater than or equal to 75 min
-the latter may represent the true thermodynamic equilibrium value, nu
(12). However, it is not clear whether such a reduction is exclusively
due to the thermodynamically driven migration of chain-ends, low mole
cular weight fractions and additives, or by the thermal degradation as
well. The contact time dependence of nu explained some of the differe
nces reported for the data obtained using different measurement techni
ques, viz. pendant drop, capillary breakup, or ellipsoid retraction te
chniques. (C) 1997 John Wiley & Sons, Inc.