Abstract
Liquid–liquid equilibrium (LLE) data for ternary systems at both low and high pressures were well reproduced by the PRSV equation of state (EOS) with two Gibbs free energy-based equation of state (EOS-G E) mixing rules, called modified Huron–Vidal first order (MHV1) and Wong–Sandler (WS) mixing rules. The binary parameters, which were previously determined from only the Gibbs free energy models at each temperature and pressure in the literature, are utilized for the rules. Good predictions were obtained for the water + methanol + alkyl ether systems at low pressure and the water + alcohol + 1,1-difluoroethane (DFE) systems at high pressures.
Sign-in/Register to access full text options 
Talk to us
Join us for a 30 min session where you can share your feedback and ask us any queries you have
Schedule a callDisclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.
