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Phase Equilibria in Hydrocarbon Systems
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Experimental Determination of Critical Points of Pure Components and Binary Mixtures Using a Flow Apparatus
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Correlation and prediction of VLE data for n-alkane mixtures
inferred← citeshttps://doi.org/10.1016/0378-3812(92)85104-gopenalex-snapshot
Modification of the Kumar-Starling five-parameter cubic equation of state and extension to mixtures
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Critical properties of the N2 +, CH4 +, and C2H6 + n-alkane mixtures
inferred← citeshttps://doi.org/10.1016/b978-0-08-002973-3.50019-5openalex-snapshot
REFERENCES FOR PARTS I AND II
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REFERENCES FOR PART III
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Isothermal phase equilibrium of binary mixtures containing supercritical CO2 and C3H8. Experiment and modeling
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Extended corresponding states model for fluids and fluid mixtures
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Helmholtz energy, extended corresponding states and local composition model for fluid mixtures
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An improved Helmholtz energy model for non-polar fluids and their mixtures. Part 2: Application to mixtures of non-polar fluids
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Critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures. II. Maximum temperatures of coexistence of liquid and gas phase in alkane binary mixtures
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Calculation of critical points for natural gas mixtures with the GERG-2008 equation of state
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Compressed liquid densities of binary mixtures of n -decane + n -dodecane at temperatures from 283 K to 363 K and pressures up to 100 MPa
inferred← citeshttps://doi.org/10.1016/j.fluid.2018.01.022openalex-snapshot
Plotting of phase (vapor-liquid) transition surface near the critical point out of data from isochoric experiment. Experimental procedure
inferred← citeshttps://doi.org/10.1016/j.fluid.2020.112502openalex-snapshot
Measurements and modeling of the VLE properties of n-hexadecane in supercritical binary propane+n-butane solvent
inferred← citeshttps://doi.org/10.1016/j.fluid.2020.112884openalex-snapshot
Density Modeling of High-Pressure Mixtures using Cubic and Non-Cubic EoS and an Excess Volume Method
inferred← citeshttps://doi.org/10.1016/j.fluid.2022.113659openalex-snapshot
Extension of a square-well equation of state for chain-like molecules using perturbed hard chain theory
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High-pressure phase equilibria in methane + pentadecane system: Experimental measurement and modeling with PengRobinson equation of state
inferred← citeshttps://doi.org/10.1016/j.fluid.2026.114791openalex-snapshot
Isothermal phase equilibria with supercritical component: The system (Ethane + Phenol). Experimental and modeling
inferred← citeshttps://doi.org/10.1016/j.supflu.2010.10.022openalex-snapshot
Determination of critical properties of pure and multi-component mixtures using a “dynamic–synthetic” apparatus
inferred← citeshttps://doi.org/10.1016/j.supflu.2019.104628openalex-snapshot
Solubility of naphthaline in supercritical binary solvent propane + n-butane mixture
inferred← citeshttps://doi.org/10.1016/j.supflu.2025.106707openalex-snapshot
Experimental study of phase-equilibrium properties of binary mixtures of supercritical solvents with the main component of asphaltene -resin- paraffin deposits for the preventing and removing inside oil wells
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Thermodynamic properties for the alternative refrigerants
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Remarks on computing the density of dense fluids by Aalto–Keskinen model
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Critical temperatures, pressures, and densities for the mixtures CO2–C3H8, CO2–nC4H10, C2H6–C3H8, and C3H8–nC4H10
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Application of Renormalization Corrections to SAFT-VR Mie
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Experimental Study and Modeling of the Isothermal VLE Properties of the Supercritical C3H8 + Aniline Mixture at High Temperatures and High Pressures
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Vapor−Liquid Equilibrium (VLE) Properties for the Binary Systems Propane (1) + n -Butane (2) and Propane (1) + Isobutane (3)
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Liquid-Phase Thermodynamic Properties for the Binary and Ternary Systems of Propane (1), n-Butane (2), and Isobutane (3)
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Validation of a New Apparatus Using the Dynamic Method for Determining the Critical Properties of Binary Gas/Gas Mixtures
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Predicting Mixture Phase Equilibria and Critical Behavior Using the SAFT-VRX Approach
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Helmholtz-Type Equations of State for Hydrocarbon Refrigerant Mixtures of Propane/n-Butane, Propane/Isobutane, n-Butane/Isobutane, and Propane/n-Butane/Isobutane
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Assessing Energy Efficiency of Compression Heat Pumps in Drying Processes when Zeotropic Hydrocarbon Mixtures are Used as Working Agents
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On the Thermodynamics of Solutions. VII. Critical Properties of Mixtures
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Selection of the Evaporation Mode and the Possibility of Saving Electrical Energy when Operating Liquified Petroleum Gas Regasification Systems
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Measurement of Vapor-liquid Equilibria (VLE) for the Ternary, Propane + Dimethyl Ether + Butane, and the Three Constituent Binaries, and Predicted Values by the Benedict-Webb-Rubin (BWR) Equation of State: Measurement and Prediction of Thermophysical Properties for Dimethyl Ether with Liquefied…
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Determination of Compressed Liquid Densities for CO2 + n-Decane Using a Vibrating Tube Densimeter
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