2026-04-28T17:55:44Zhttps://riubu.ubu.es/oai/request

oai:riubu.ubu.es:10259/45662022-04-29T12:02:46Zcom_10259_4244com_10259_5086com_10259_2604col_10259_4245

00925njm 22002777a 4500 dc Melgosa Gómez, Rodrigo author Sanz Díez, Mª Teresa author García Solaesa, Ángela author Beltrán Calvo, Sagrario author 2017-12 This work provides experimental fluid phase equilibrium data of the pseudo-ternary mixture CO2 + ethanol + fish oil, a system of interest in pharmaceutical and food-industry applications such as the production of omega-3-enriched lipid derivatives at mild, non-oxidative conditions. Experimental tie-lines were obtained by means of an analytical isothermal method with recirculation of the vapour phase. Measurements were carried out in the temperature range 323.15 K–343.15 K and at pressures from 10 MPa to 30 MPa. The Peng-Robinson equation of state coupled with the conventional van der Waals mixing rules with two adjustable parameters was used for experimental data correlation. 0021-9614 http://hdl.handle.net/10259/4566 10.1016/j.jct.2017.07.032 Phase equilibrium Supercritical carbon dioxide Ethanol Fish oilThermodynamic modelling Peng-Robinson equation of state Phase behaviour of the pseudo-ternary system carbon dioxide + ethanol + fish oil at high pressures