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]
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...
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Veröffentlicht in: | International journal of refrigeration 2019-08, Vol.104, p.386-389 |
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Hauptverfasser: | , , , , , |
Format: | Artikel |
Sprache: | eng |
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Online-Zugang: | Volltext |
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Zusammenfassung: | 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. |
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ISSN: | 0140-7007 1879-2081 |
DOI: | 10.1016/j.ijrefrig.2019.05.039 |