Calculation of vapour—liquid equilibrium data for binary chlorofluorocarbon mixtures using the Peng-Robinson equation of state-Reference-Cited by-同舟云学术

Calculation of vapour—liquid equilibrium data for binary chlorofluorocarbon mixtures using the Peng-Robinson equation of state

Published:1991-01 Issue:1-2 Volume:62 Page:41-52
ISSN:0378-3812
Container-title:Fluid Phase Equilibria
language:en
Short-container-title:Fluid Phase Equilibria

Author:

Abu-Eishah Samir I.

Publisher

Elsevier BV

Subject

Physical and Theoretical Chemistry,General Physics and Astronomy,General Chemical Engineering

Reference20 articles.

1. Vapor—liquid equilibria for CO2C2H2F;Adams;J. Chem. Eng. Data,1971

2. Calculation of thermodynamic properties and vapor—liquid equilibria of refrigerants;Asselineau;Chem. Eng. Sci.,1978

3. Peng-Robinson equation of state checks validity of PVT experiments;Conard;Oil Gas J.,1980

4. Fluorocarbon Solutions at Low Temperatures. IV. The Liquid Mixtures CH4 + CClF3, CH2F2 + CClF3, CHF3 + CClF3, CF4 + CClF3, C2H6 + CClF3, C2H6 + CF4, and CHF3 + CF4

5. Liquid—vapor phase equilibria of the binary system difluoromonochloromethane (R22)—difluorodichloromethane (R12);Kriebel;Kaltetechnik-Klimatiseirung,1967

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