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Phase Equilibria of Chlorofluorocarbon Alternative Refrigerant Mixtures

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Outgoing claims: the papers this work cites, builds on, or argues with.

inferredcites →https://doi.org/10.1007/bf02081285openalex-snapshot

Vapor-liquid equilibrium, coexistence curve, and critical locus for binary HFC-32/HFC-134a mixture

inferredcites →https://doi.org/10.1016/0140-7007(96)81780-4openalex-snapshot

Vapour-liquid equilibrium of ternary mixtures of the refrigerants R32, R125 and R134a

inferredcites →https://doi.org/10.1021/je970071mopenalex-snapshot

Vapor−Liquid Equilibria for the Difluoromethane (HFC-32) + 1,1,1,2-Tetrafluoroethane (HFC-134a) System

inferredcites →https://doi.org/10.6028/nbs.tn.1226openalex-snapshot

Application of a hard sphere equation of state to refrigerants and refrigerant mixtures

What points at this work

Incoming claims: where this work appears in other papers’ reference lists and arguments.

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Predicting the Vle, Sle and Surface Tension of Refrigerant Systems Using a Saft-Based Activity Coefficient Model

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Beyond Temperature Glide: The Compressor is Key to Realizing Benefits of Zeotropic Mixtures in Heat Pumps

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Difluoromethane CH2F2 + C2H4F2 1,1-Difluoroethane

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Difluoromethane CH2F2 + C2H3F3 1,1,1-Trifluoroethane

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Study on the Interaction Coefficients in PR Equation with vdW Mixing Rules for HFC and HC Binary Mixtures

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A New Theoretically-Derived Simplified Equation of State with Applications to Refrigerants

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Deep learning based combining rule for the estimation of vapor–liquid equilibrium

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The cubic-plus-association equation of state for hydrofluorocarbons, hydrofluoroolefins, and their binary mixtures

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Retrofits and options for the alternatives to HCFC-22

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Vapor–liquid equilibrium of difluoromethane +1,1,1,2-tetrafluoroethane systems over a temperature range from 258.15 to 343.15K

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Gradient theory modeling of surface tension for pure fluids and binary mixtures

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Molecular models for 267 binary mixtures validated by vapor–liquid equilibria: A systematic approach

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Vapor–liquid equilibrium measurement and modeling for the difluoromethane+pentafluoroethane+propane ternary mixture

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A modified differential-model for interaction parameters in PR EoS with vdW mixing rules for mixtures containing HFCs and HCs

inferred← citeshttps://doi.org/10.1016/j.fluid.2015.03.019openalex-snapshot

Molecular modeling and simulation of vapor–liquid equilibrium of the refrigerant R152a and its mixture R152a+R32

inferred← citeshttps://doi.org/10.1016/j.fluid.2016.05.010openalex-snapshot

Prediction of ternary azeotropic refrigerants with a simple method

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A simple model for temperature-independent k of the PR-vdW model for mixtures containing HCs, HFCs, PFCs, HFOs, CO2, RE170 and R13I1

inferred← citeshttps://doi.org/10.1016/j.fluid.2016.10.011openalex-snapshot

Isothermal vapor liquid equilibrium measurements for difluoromethane (R32) + trans-1,3,3,3-tetrafluoropropene (R1234ze(E))

inferred← citeshttps://doi.org/10.1016/j.fluid.2019.06.020openalex-snapshot

Experimental measurements of saturated vapor pressure and isothermal vapor-liquid equilibria for 1,1,1,2-Tetrafluoroethane (HFC-134a) + 3,3,3-trifluoropropene (HFO-1243zf) binary system

inferred← citeshttps://doi.org/10.1016/j.ijrefrig.2010.06.005openalex-snapshot

Application of M4 cubic equation of state for refrigerants

inferred← citeshttps://doi.org/10.1016/j.ijrefrig.2019.02.017openalex-snapshot

Reconsideration of the alpha coefficient in NRTL model on the vapor liquid phase equilibrium description of refrigerant mixtures

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Predictions of thermodynamic properties and phase equilibria of refrigerant systems with COSMO approaches

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Vapor-liquid equilibrium measurements and models for the ternary mixtures of R1234yf + R32 + R125 and R1234yf + R32 + CO2

inferred← citeshttps://doi.org/10.1016/j.ijrefrig.2024.12.016openalex-snapshot

Vapor–liquid phase equilibria for the unary, binary, and ternary components of carbon dioxide (CO2), Difluoromethane (R32), and 1,1,1,2-tetrafluoroethane (R134a)

inferred← citeshttps://doi.org/10.1016/j.ijrefrig.2026.01.027openalex-snapshot

A general nonlinear prediction model for binary interaction parameter of vdW mixing rules in PR EOS for phase Equilibria of HFO mixtures

inferred← citeshttps://doi.org/10.1016/j.molliq.2018.07.056openalex-snapshot

On the anomalous composition dependence of viscosity and surface tension in refrigerant blends

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Hunting sustainable refrigerants fulfilling technical, environmental, safety and economic requirements

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Absorption separation of fluorinated refrigerant gases with ionic liquids: Equilibrium, mass transport, and process design

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Phase equilibria of 1,1,1-trifluoroethane (HFC-143a) + 1,1,1,2-tetrafluoroethane (HFC-134a), and + 1,1-difluoroethane (HFC-152a) at 273.15, 293.15, 303.15, and 313.15 K

inferred← citeshttps://doi.org/10.1016/s0378-3812(02)00096-1openalex-snapshot

High-pressure fluid phase equilibria

inferred← citeshttps://doi.org/10.1016/s0378-3812(02)00216-9openalex-snapshot

Prediction of vapor–liquid equilibria properties of several HFC binary refrigerant mixtures

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Phase Equilibria of Difluoromethane (R32), 1,1,1,2-Tetrafluoroethane (R134a), and trans -1,3,3,3-Tetrafluoro-1-propene (R1234ze(E)) Probed by Experimental Measurements and Monte Carlo Simulations

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Rate-Based Model Simulation with Experimental Mixture Properties for R-410A Separation Using 1-Ethyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide [C2C1im][Tf2N]

inferred← citeshttps://doi.org/10.1021/acs.jced.1c00654openalex-snapshot

Bubble Point Measurements of Mixtures of HFO and HFC Refrigerants

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Molecular Modeling of HFC Separation in Fluorinated Ionic Liquids: A SAFT-VR Mie Study

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Vapor–Liquid Equilibria for the Binary and Ternary Systems of Difluoromethane (R32), 1,1-Difluoroethane (R152a), and 2,3,3,3-Tetrafluoroprop-1-ene (R1234yf)

inferred← citeshttps://doi.org/10.1021/acs.jpcb.3c01058openalex-snapshot

Multipolar SAFT-VR Mie Equation of State: Predictions of Phase Equilibria in Refrigerant Systems with No Binary Interaction Parameter

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Molecular Origin of Interfacial Anomalies in Azeotropic Refrigerant Mixtures

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Vapor−Liquid Equilibria Predictions for New Refrigerant Mixtures Based on Group Contribution Theory

inferred← citeshttps://doi.org/10.1023/a:1006653309953openalex-snapshot

Vapor–Liquid Equilibria of CFC Alternative Refrigerant Mixtures: Trifluoromethane (HFC-23)+Difluoromethane (HFC-32), Trifluoromethane (HFC-23)+Pentafluoroethane (HFC-125), and Pentafluoroethane (HFC-125)+1,1-Difluoroethane (HFC-152a)

inferred← citeshttps://doi.org/10.1023/a:1010735318011openalex-snapshot

Phase Equilibria of CFC Alternative Refrigerant Mixtures: 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea)+Difluoromethane (HFC-32), +1,1,1,2-Tetrafluoroethane (HFC-134a), and +1,1-Difluoroethane (HFC-152a)

inferred← citeshttps://doi.org/10.1142/9789812702623_0012openalex-snapshot

BINARY VAPOR-LIQUID EQUILIBRIA OF THE N -BUTANE + DIFLUOROMETHANE, + PENTAFLUOROETHANE, AND + 1,1,1,2-TETRAFLUOROETHANE SYSTEMS

inferred← citeshttps://doi.org/10.1252/jcej.17we024openalex-snapshot

Modified Vapor Pressure Model Based on Corresponding-States Principle for Pure and Mixed Refrigerants

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