Isothermal Vapor–Liquid Equilibrium for the Tetrafluoromethane (R14) + Octafluoropropane (R218) Binary Mixture at Five Temperatures from 173.150 to 213.150 K
- 27 September 2022
- journal article
- research article
- Published by American Chemical Society (ACS) in Journal of Chemical & Engineering Data
- Vol. 67 (10), 3116-3124
- https://doi.org/10.1021/acs.jced.2c00444
Abstract
No abstract availableKeywords
Funding Information
- Youth Innovation Promotion Association of the Chinese Academy of Sciences (2021028)
- National Natural Science Foundation of China (51876215, 52036010)
- Qingdao Casfuture Research Institute CO., LTD (21-8-1-1-qy)
This publication has 28 references indexed in Scilit:
- Vapor−Liquid Equilibrium Data of the Methane + Tetrafluoromethane System at Temperatures from (159.61 to 178.93) KJournal of Chemical & Engineering Data, 2007
- Isothermal Vapor−Liquid Equilibrium Data for Tetrafluoromethane + Ethane over a Temperature Range from (179.68 to 210.03) KJournal of Chemical & Engineering Data, 2006
- Short Fundamental Equations of State for 20 Industrial FluidsJournal of Chemical & Engineering Data, 2006
- A modified Huron-Vidal mixing rule for cubic equations of stateFluid Phase Equilibria, 1990
- The corelation and estimation of vapour pressures IV. Observations on Wagner's method of fitting equations to vapour pressuresThe Journal of Chemical Thermodynamics, 1986
- Calculation of thermodynamic properties and vapor-liquid equilibria of refrigerantsChemical Engineering Science, 1978
- Vapor‐Liquid equilibrium: Part I. An appraisal of data reduction methodsAIChE Journal, 1973
- Equilibrium constants from a modified Redlich-Kwong equation of stateChemical Engineering Science, 1972
- Local compositions in thermodynamic excess functions for liquid mixturesAIChE Journal, 1968
- Thermodynamic Properties of Octafluoropropane from 14°K to Its Normal Boiling Point. An Estimate of the Barrier to Internal Rotation from the Entropy and Heat Capacity of the GasThe Journal of Chemical Physics, 1967