Fluid phase equilibrium studies on model substances for supercritical fluid extraction with CO2 up to 100 MPa

Abstract

Multicomponent fluid phase equilibrium data are of increasing interest for applications in Supercritical Fluid Extraction (SFE) where compressed supercritical gases are used for the extraction of low-volatile substances (e.g. caffeine from coffee and tea, hops etc.). Sometimes so-called moderator substances have to be added in order to increase solvent power and/or selectivity. Systematic measurements on a four-component system of the type CO₂ + fatty alcohol (e.g. 1-do-decanol) + alkane (e.g. hexadecane) as a function of the amount of moderator added were performed at 393 K and at pressures from 10 to 100 MPa in an analytical high-pressure cell. Separation factors calculated from the p,T,w/,w, “data are presented and discussed.