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Vapor−Liquid Equilibrium Measurements for the Ethane + Hexafluoroethane System over a Temperature Range from (199.64 to 242.93) K

https://doi.org/10.1021/je050281w
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What this work says

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

inferredcites →https://doi.org/10.1016/0140-7007(93)90069-kopenalex-snapshot
Azeotropy in refrigerant mixtures
inferredcites →https://doi.org/10.1016/0378-3812(83)85007-9openalex-snapshot
An apparatus for the investigation of low-temperature, high-pressure, vapor—liquid and vapor—liquid—liquid equilibria
inferredcites →https://doi.org/10.1016/s0140-7007(96)00076-xopenalex-snapshot
Refrigerant conversion of auto-refrigerating cascade (ARC) systems
inferredcites →https://doi.org/10.1021/i160057a012openalex-snapshot
Creation and Survival of Secondary Crystal Nuciel. The Potassium Sulfate-Water System

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/jccs.200800143openalex-snapshot
Computational Study of the Dissolution of Some Atomic and Diatomic Species in the Square and Hexagonal 2‐D Helium Lattices
inferred← citeshttps://doi.org/10.1007/978-3-540-49315-0_306openalex-snapshot
Hexafluoroethane C2F6 + C2H6 Ethane
inferred← citeshttps://doi.org/10.1016/j.fluid.2005.12.004openalex-snapshot
Vapor–liquid equilibrium measurements and correlations for an azeotropic system of ethane+hexafluoroethane
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.2016.06.029openalex-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.2022.113456openalex-snapshot
The impressive impact of including enthalpy and heat capacity of mixing data when parameterising equations of state. Application to the development of the E-PPR78 (Enhanced-Predictive-Peng-Robinson-78) model.
inferred← citeshttps://doi.org/10.1016/j.ijrefrig.2016.09.013openalex-snapshot
Fluid-phase-equilibrium prediction of fluorocompound-containing binary systems with the predictive E -PPR78 model
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/10.1021/acs.jced.7b00485openalex-snapshot
Isothermal Vapor–Liquid Equilibrium Data for the Hexafluoroethane (R116) + n -Butane System at Temperatures from 273 to 323 K
inferred← citeshttps://doi.org/10.1021/acs.jced.7b00836openalex-snapshot
Isothermal Vapor–Liquid Equilibrium Data for Binary Mixtures of Hexafluoroethane (R116) + n-Pentane or n-Hexane at Two Temperatures, 288 and 296 K
inferred← citeshttps://doi.org/10.1021/ie070911iopenalex-snapshot
Vapor−Liquid Equilibria Predictions for New Refrigerant Mixtures Based on Group Contribution Theory
inferred← citeshttps://doi.org/10.1021/je100143kopenalex-snapshot
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/je800505yopenalex-snapshot
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/je800849sopenalex-snapshot
Isothermal Vapor−Liquid Equilibrium Data for the Hexafluoroethane (R116) + Propane System at Temperatures from (263 to 323) K
inferred← citeshttps://doi.org/10.1021/jp9072137openalex-snapshot
Mie Potentials for Phase Equilibria Calculations: Application to Alkanes and Perfluoroalkanes
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