Corrigendum and Comments to "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" [Int. J. Refrig. 98 (2019) 362–371]. (August 2019)

• Record Type: Journal Article
• Authors: Fauve, Rémi; Coquelet, Christophe; Houriez, Céline; Artola, Pierre-Arnaud; Ahmar, Elise El; Rousseau, Bernard
• Is Part Of: International journal of refrigeration. Volume 104(2019)
• Page Start: 386
• Page End: 389
• Publication Date: 2019-08
• Subjects: Isothermal VLE data -- R744 -- R-1234ze(E) -- Critical point -- Modeling -- Gibbs Ensemble Monte Carlo; Données d'équilibre liquide-vapeur isotherme -- R744 -- R-1234ze(E) -- Point critique -- Modélisation -- Algorithme de Gibbs Ensemble Monte Carlo; Refrigeration and refrigerating machinery -- Periodicals; 621.56
• DOI: 10.1016/j.ijrefrig.2019.05.039
• Languages: English
• ISSNs: 0140-7007

Abstract

Abstract: We have published vapor liquid equilibrium data (VLE) for the binary mixture of CO2 + R-1234ze(E) (trans-1, 3, 3, 3-tetrafluoroprop-1-ene) in International Journal of Refrigeration, Volume 98, February 2019, Pages 362-371. In this paper, we presented Gibbs Ensemble Monte Carlo simulation data performed at 293.15 K and 353.02 K. It just so happened that there was a mistake in one of the initial configurations at 353.02 K and the results were not correct. We present here corrected MC values and we compare the results with Peng Robinson EoS calculation and REFPROP predictions.