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Phase Behavior and Densities of Propylene + Hexane Binary Mixtures to 585 K and 70 MPa
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Citations
18
References
2016
Year
EngineeringMixture Density DataExperimental ThermodynamicsChemistryTwo-phase FlowThermodynamic ModellingChemical EngineeringFluid PropertiesMolecular ThermodynamicsNumerical SimulationTransport PhenomenaThermodynamicsPhase SeparationEquilibrium Thermodynamic PropertyPolymer ChemistryMaterials ScienceChemical ThermodynamicsPolymer BlendPhase BehaviorPhysical ChemistryMultiphase FlowMsl EosPhase EquilibriumPolymer ScienceChemical Kinetics
In this study, we report phase behavior data for propylene + hexane mixtures at temperatures of 295 to 468 K and pressures to 5.5 MPa and high-pressure mixture density data at temperatures of 295 to 584 K and pressures to 70 MPa. Both the phase behavior and density data are simultaneously determined using a variable volume, high-pressure view cell that is coupled with a linear variable differential transformer. The phase behavior and mixture density data are modeled with the Soave–Redlich–Kwong (SRK), Peng–Robinson (PR), modified Sanchez–Lacombe (MSL), and perturbed-chain statistical associating fluid theory (PC-SAFT) equations of state (EoS). The PC-SAFT and MSL EoS provide the best fit of the phase behavior data with a nonzero value of 0.028 for kij. Likewise, the PC-SAFT EoS provides the best fit of the high-pressure mixture density data, though the PC-SAFT equation slightly overpredicts the solution density and the calculated densities are relatively insensitive to changes in kij from zero to 0.028.
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