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Vapor–liquid equilibrium and molecular simulation data for carbon dioxide (CO2)?+?trans-1,3,3,3-tetrafluoroprop-1-ene (R-1234ze(E)) mixture at temperatures from 283.32 to 353.02?K and pressures up to 7.6?MPa.

Author(s) : WANG S., FAUVE R., COQUELET C., et al.

Type of article: Article, IJR article

Summary

Isothermal Vapor–Liquid Equilibrium (VLE) data for the binary mixture of CO2?+?R-1234ze(E)(trans-1,3,3,3-tetrafluoroprop-1-ene) were measured using a static-analytic method apparatus at seven temperatures between 283.32 and 353.02?K and pressures up to 7.6?MPa. For temperatures over the critical temperature of pure CO2, the critical compositions and pressures of binary mixtures were approximated applying power laws with asymptotic behavior at critical point. The data were well correlated using the Peng–Robinson equation of state incorporating the generalized alpha function, with the Wong–Sandler mixing rules involving NRTL activity coefficient model. The experimental and correlated phase compositions were compared with Gibbs Ensemble Monte Carlo simulation data obtained at 293.15?K and 353.02?K. Though the molecular simulation predictions at low temperature (293.15?K) properly match experimental data, a slight shift appeared at high temperature (353.02?K), and the expected convergence of phase compositions near critical point was not fully observed.

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Pages: 362-371

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  • Original title: Vapor–liquid equilibrium and molecular simulation data for carbon dioxide (CO2)?+?trans-1,3,3,3-tetrafluoroprop-1-ene (R-1234ze(E)) mixture at temperatures from 283.32 to 353.02?K and pressures up to 7.6?MPa.
  • Record ID : 30025408
  • Languages: English
  • Source: International Journal of Refrigeration - Revue Internationale du Froid - vol. 98
  • Publication date: 2019/02
  • DOI: http://dx.doi.org/10.1016/j.ijrefrig.2018.10.032

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