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- [22] Measurements of Isothermal Vapor-Liquid Equilibrium and Critical Point-Based Perturbed-Chain Statistical Association Fluid Theory Phase Behavior Modeling of the Propane plus Phenol and Tetracosane plus Propane/n-Butane Mixtures JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2022, 68 (01): : 138 - 150
- [23] New Design of the High-Pressure Optical Cell for Vapor-Liquid Equilibrium Measurements. Supercritical Binary Mixture (Propane/n-Butane) plus Acetophenone JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2020, 65 (07): : 3306 - 3317
- [25] Three-Phase Vapor-Liquid-Liquid Equilibria for Methane plus n-Octane plus Monoethylene Glycol plus Water at Pressures from (3.1 to 15.0) MPa and Temperatures from (281 to 363) K JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2009, 54 (05): : 1613 - 1618
- [28] Densities, speeds of sound, refractive indices, viscosities and their related thermodynamic properties for n-hexadecane plus two aromatic hydrocarbons binary mixtures at temperatures from 298.15 K to 318.15 K JOURNAL OF CHEMICAL THERMODYNAMICS, 2019, 128 : 383 - 393
- [29] Isothermal (vapour plus liquid) equilibrium measurements and correlation for the {n-butane (R600)+1,1,1,3,3-pentafluoropropane (R245fa)} system at temperatures from (303.150 to 373.150) K JOURNAL OF CHEMICAL THERMODYNAMICS, 2016, 95 : 49 - 53
- [30] Measurement of the (pressure, density, temperature) relation of two (methane plus nitrogen) gas mixtures at temperatures between 240 and 400 K and pressures up to 20 MPa using an accurate single-sinker densimeter JOURNAL OF CHEMICAL THERMODYNAMICS, 2006, 38 (07): : 916 - 922