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Vapor−Liquid Equilibrium Data for the Ethane + Trifluoromethane System at Temperatures from (188.31 to 243.76) K

https://doi.org/10.1021/je0601107
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What this work says

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

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Local compositions in thermodynamic excess functions for liquid mixtures
inferredcites →https://doi.org/10.1016/0009-2509(72)80096-4openalex-snapshot
Equilibrium constants from a modified Redlich-Kwong equation of state
inferredcites →https://doi.org/10.1016/0378-3812(79)80001-1openalex-snapshot
New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixtures
inferredcites →https://doi.org/10.1016/j.fluid.2005.12.004openalex-snapshot
Vapor–liquid equilibrium measurements and correlations for an azeotropic system of ethane+hexafluoroethane

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
inferred← citeshttps://doi.org/10.1002/apj.1884openalex-snapshot
The study of binary interaction parameters on VLE for alternative refrigerant mixtures
inferred← citeshttps://doi.org/10.1016/j.fluid.2008.04.012openalex-snapshot
Prediction of homogeneous azeotropes by Wilson equation for binary HFCs and HCs refrigerant mixtures
inferred← citeshttps://doi.org/10.1016/j.fluid.2009.08.008openalex-snapshot
High-pressure fluid-phase equilibria: Experimental methods and systems investigated (2000–2004)
inferred← citeshttps://doi.org/10.1016/j.fluid.2010.09.017openalex-snapshot
High-pressure fluid-phase equilibria: Experimental methods and systems investigated (2005–2008)
inferred← citeshttps://doi.org/10.1016/j.fluid.2016.05.010openalex-snapshot
Prediction of ternary azeotropic refrigerants with a simple method
inferred← citeshttps://doi.org/10.1016/j.fluid.2016.06.029openalex-snapshot
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.2017.07.002openalex-snapshot
Vapor-liquid and vapor-liquid-liquid equilibrium measurements and correlation of the binary mixtures 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) + (tetrafluoromethane (R14), trifluoromethane (R23), octafluoropropane (R218), nitrogen (R728) and argon (R740)) and ethane (R170) + trifluoromethane (R23)
inferred← citeshttps://doi.org/10.1016/j.icheatmasstransfer.2006.12.005openalex-snapshot
Nucleate pool boiling heat transfer measurements of HC170/HFC23 system
inferred← citeshttps://doi.org/10.1016/j.ijrefrig.2008.11.007openalex-snapshot
Performance of R170 mixtures as refrigerants for refrigeration at −80 °C temperature range
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
inferred← citeshttps://doi.org/10.1016/j.jct.2010.04.016openalex-snapshot
Isothermal (vapour + liquid) equilibrium for the binary {1,1,2,2-tetrafluoroethane (R134) + propane (R290)} and {1,1,2,2-tetrafluoroethane (R134) + isobutane (R600a)} systems
inferred← citeshttps://doi.org/10.1016/j.jct.2010.11.001openalex-snapshot
Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows
inferred← citeshttps://doi.org/10.1016/j.jct.2019.105996openalex-snapshot
The investigation on the vapor-liquid phase equilibrium of (trifluoromethane + difluoromethane) system at temperatures ranging from (223.150 to 273.150) K
inferred← citeshttps://doi.org/10.1016/j.jct.2021.106567openalex-snapshot
Binary mixture isothermal vapour-liquid equilibrium: Trifluoromethane (R23) + octafluoropropane (R218) at the temperature from 223.150 K to 263.150 K
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Benchmark Database Containing Binary-System-High-Quality-Certified Data for Cross-Comparing Thermodynamic Models and Assessing Their Accuracy
inferred← citeshttps://doi.org/10.1021/acs.iecr.2c00719openalex-snapshot
Searching for Sustainable Refrigerants by Bridging Molecular Modeling with Machine Learning
inferred← citeshttps://doi.org/10.1021/acs.iecr.8b01933openalex-snapshot
Modeling of Trifluoromethane (R-23) or Hexafluoroethane (R-116) and Alkane Binary Mixtures using the Group-Contribution with Association Equation of State
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
inferred← citeshttps://doi.org/10.1021/acssuschemeng.1c05985openalex-snapshot
Assessment of Low Global Warming Potential Refrigerants for Drop-In Replacement by Connecting their Molecular Features to Their Performance
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Vapor−Liquid Equilibria Predictions for New Refrigerant Mixtures Based on Group Contribution Theory
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Vapor−Liquid Equilibria for 1,1,2,2-Tetrafluoroethane (R134) + Fluoroethane (R161) at Temperatures between (263.15 and 288.15) K
inferred← citeshttps://doi.org/10.1021/je200921uopenalex-snapshot
Isobaric Vapor–Liquid Equilibrium for Binary Systems of Toluene + Ethanol and Toluene + Isopropanol at (101.3, 121.3, 161.3, and 201.3) kPa
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Vapor−Liquid Equilibria of the Fluoroethane (R161) + 1,1,1,2-Tetrafluoroethane (R134a) System at Various Temperatures from (253.15 to 292.92) K
inferred← citeshttps://doi.org/10.1021/je900693qopenalex-snapshot
Prediction of Homogeneous Azeotropes by the UNIFAC Method for Binary Refrigerant Mixtures
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Isothermal Vapor−Liquid Equilibria for 1,1-Difluoroethane (R152a) + Propane (R290) at Temperatures between (254.31 and 287.94) K
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CONSISTÊNCIA TERMODINÂMICA DE DADOS EXPERIMENTAIS DE EQUILÍBRIO DE FASES EM SISTEMAS BINÁRIOS
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Parametrization of equations of state : definition of a methodology applicable to SAFT models for pure species (with and without association term) and evaluation of their influence on model performances
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Développement d’équations d’état cubiques adaptées à la représentation de mélanges contenant des molécules polaires (eau, alcools, amines …) et des hydrocarbures
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