Vapor−Liquid Equilibrium Measurements and Correlation of the Binary Refrigerant Mixture Propane (HC-290) + 1,1,1,2,3,3,3-Heptafluoropropane (HFC-227ea) at 278.15, 293.15, and 308.15 K
Author:
Affiliation:
1. Consiglio Nazionale delle Ricerche, Istituto per la Tecnica del Freddo, Corso Stati Uniti 4, 35127 Padova, Italy
Publisher
American Chemical Society (ACS)
Subject
General Chemical Engineering,General Chemistry
Link
https://pubs.acs.org/doi/pdf/10.1021/je010269d
Reference16 articles.
1. (Vapour + liquid) equilibrium measurements and correlations of the refrigerant mixture {dimethyl ether (RE170) + 1,1,1,3,3,3-hexafluoropropane (R236fa)} at the temperatures (303.68 and 323.75) K
2. Isothermal vapor–liquid equilibrium for the three binary systems 1,1,1,2,3,3-hexafluoropropane with dimethyl ether or propane, and 1,1,1,3,3,3-hexafluoropropane with dimethyl ether
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1. Experimental Investigation on Solubility and Viscosity of 1,1,1,2,3,3,3-Heptafluoropropane (R227ea) and Polyol Ester Oil (POE 22) Mixtures;Journal of Chemical & Engineering Data;2021-12-08
2. Experimental investigation on vapor liquid equilibrium and azeotropic behavior for the 1,1,1,2-tetrafluoroethane (R134a) + propane (R290) system at temperatures from 253.15 to 303.15 K;International Journal of Refrigeration;2020-12
3. Measurements of isobaric heat capacity of R143a and R227ea at liquid phase by quasi-steady scanning;Thermochimica Acta;2020-01
4. Reconsideration of the alpha coefficient in NRTL model on the vapor liquid phase equilibrium description of refrigerant mixtures;International Journal of Refrigeration;2019-04
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