Modeling of the thermodynamic properties of the mixtures: Prediction of the position of azeotropes for binary mixtures
Author:
Publisher
Elsevier BV
Subject
Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering
Reference21 articles.
1. Measurement of vapor–liquid equilibria for the binary systems of propane+1,1,1,2-tetrafluoroethane and 1,1,1-trifluoroethane+propane at various temperatures
2. Vapor−Liquid Equilibrium Data for the Azeotropic Difluoromethane + Propane System at Temperatures from 294.83 to 343.26 K and Pressures up to 5.4 MPa
3. Vapor–liquid equilibrium data for the difluoromethane (R32)–dimethyl ether (RE170) system at temperatures from 283.03 to 363.21K and pressures up to 5.5MPa
4. Vapor–liquid equilibrium data for the hexafluoroethane+carbon dioxide system at temperatures from 253 to 297K and pressures up to 6.5MPa
5. Isothermal Vapor−Liquid Equilibrium Data for the Hexafluoroethane (R116) + Propane System at Temperatures from (263 to 323) K
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2. Calculation of azeotropic properties for binary mixtures with the PC-SAFT equation of state;Fluid Phase Equilibria;2023-02
3. Prediction of thermodynamic properties of the ternary azeotropic mixtures;Fluid Phase Equilibria;2020-08
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