Isothermal Vapor–Liquid Equilibrium Data for the Hexafluoroethane (R116) + n-Butane System at Temperatures from 273 to 323 K-Reference-Cited by-同舟云学术

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Isothermal Vapor–Liquid Equilibrium Data for the Hexafluoroethane (R116) + n-Butane System at Temperatures from 273 to 323 K

Published:2017-08-31 Issue:10 Volume:62 Page:3483-3487
ISSN:0021-9568
Container-title:Journal of Chemical & Engineering Data
language:en
Short-container-title:J. Chem. Eng. Data

Author:

Ramjugernath Deresh¹^ORCID,Valtz Alain²,Richon Dominique¹,Williams-Wynn Mark D.¹^ORCID,Coquelet Christophe²^ORCID

Affiliation:

1. Thermodynamics Research Unit, School of Engineering, University of KwaZulu-Natal, Howard College Campus, Durban, 4001, South Africa

2. Mines ParisTech, PSL Research University, CTP−Centre of Thermodynamics of Processes, 35 rue Saint Honoré, 77305 Fontainebleau Cedex, France

Funder

Department of Science and Technology, Republic of South Africa

National Research Foundation

Publisher

American Chemical Society (ACS)

Subject

General Chemical Engineering,General Chemistry

Link

https://pubs.acs.org/doi/pdf/10.1021/acs.jced.7b00485

Reference22 articles.

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

2. Vapor–liquid equilibrium measurements and correlations for an azeotropic system of ethane+hexafluoroethane

3. Vapor–liquid equilibrium data for the hexafluoroethane+carbon dioxide system at temperatures from 253 to 297K and pressures up to 6.5MPa

4. Vapor–liquid equilibrium data for the (hexafluoroethane +1,1,1,2-tetrafluoroethane) system at temperatures from 263 to 353K and pressures up to 4.16MPa

5. Isothermal Vapor−Liquid Equilibrium Data for the Hexafluoroethane (R116) + Propane System at Temperatures from (263 to 323) K

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1. Implementation of PC-SAFT for Predicting thermodynamic properties of pure refrigerants and vapor-liquid equilibria of refrigerants binary mixtures.;Fluid Phase Equilibria;2023-10

2. Vapor-liquid equilibrium predictions of refrigerant systems using COSMO based Gex-EoS methods;Fluid Phase Equilibria;2022-12

3. 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.;Fluid Phase Equilibria;2022-09

4. Isothermal Bubble Pressure Data for the Binary System of C2F6 and n-Octane;Journal of Chemical & Engineering Data;2018-12-04

5. Modeling of Trifluoromethane (R-23) or Hexafluoroethane (R-116) and Alkane Binary Mixtures using the Group-Contribution with Association Equation of State;Industrial & Engineering Chemistry Research;2018-07-05

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