The application of liquid-liquid separation as a means of polymer-solvent s
eparation was studied. Phase separation experiments were performed with eth
ene-propene-diene terpolymer (EPDM) solved in hexane, using propene as an a
ntisolvent. The results were interpreted using a thermodynamic model based
on the Sako-Wu-Prausnitz (SWP) equation of state. The description of homoge
neous polymers is unambiguous, but for heterogeneous polymers further devel
opment of the SWP theory is required. It was found that the model shows pro
mising results with respect to multicomponent polymer systems. However, the
description of the interaction between the components is still unsatisfact
ory. Therefore, an empirical model was developed to describe the experiment
al results. A flowsheet model was constructed to describe a novel EPDM proc
ess containing a liquid-liquid countercurrent extraction column. The effect
s of temperature, pressure, antisolvent concentration, and number of theore
tical equilibrium stages were studied. With respect to variable costs, liqu
id-liquid extraction is a cost-effective option in the purification of rubb
er polymer solutions.