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Isothermal vapor–liquid equilibrium data for the binary mixture of carbon dioxide (CO2) and 1,1,1,3,3-pentafluorobutane (R365mfc) were measured at six isotherms ranging from 283.16 to 337.16 K, at pressures ranging from 0.7 to 9.1 MPa, and are presented. The measurements were performed using a “static-analytic” apparatus, equipped with two capillary ROLSI samplers, with phase analysis performed via gas chromatography. The measured data were correlated using in-house thermodynamic software based on the Peng–Robinson equation of state with the Mathias–Copeman α function and the Wong–Sandler mixing rules incorporating the nonrandom two liquids model.

journal of chemical and engineering data

Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO<sub>2</sub>) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K

Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO2) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K

Vapor–Liquid Equilibrium Data for the Carbon Dioxide (CO₂) + 1,1,1,3,3-Pentafluorobutane (R365mfc) System at Temperatures from 283.15 to 337.15 K