TY - JOUR
T1 - Isothermal vapor-liquid equilibrium data for the ethene+2,2,3-trifluoro-3-(trifluoromethyl)oxirane binary system between 258 and 308K at pressures up to 4.5MPa
AU - Subramoney, Shalendra Clinton
AU - Nelson, Wayne Michael
AU - Naidoo, Paramespri
AU - Coquelet, Christophe
AU - Richon, Dominique
AU - Ramjugernath, Deresh
PY - 2015/5/5
Y1 - 2015/5/5
N2 - Isothermal vapor-liquid equilibrium data (. P-x-. y) are presented for ethene. +. 2,2,3-trifluoro-3-(trifluoromethyl)oxirane mixtures at six temperatures in the range 258.38-307.38. K, and pressures up to 4.54. MPa. Experimental P-x-. y data were measured using an apparatus based on the "static-analytic" method. The experimental data were correlated with a model composed of the Peng-Robinson equation of state using the Mathias-Copeman alpha function, Wong-Sandler mixing rules and the NRTL local composition model. The thermodynamic model accurately represents the experimental VLE data over the entire temperature range investigated.
AB - Isothermal vapor-liquid equilibrium data (. P-x-. y) are presented for ethene. +. 2,2,3-trifluoro-3-(trifluoromethyl)oxirane mixtures at six temperatures in the range 258.38-307.38. K, and pressures up to 4.54. MPa. Experimental P-x-. y data were measured using an apparatus based on the "static-analytic" method. The experimental data were correlated with a model composed of the Peng-Robinson equation of state using the Mathias-Copeman alpha function, Wong-Sandler mixing rules and the NRTL local composition model. The thermodynamic model accurately represents the experimental VLE data over the entire temperature range investigated.
KW - Ethylene
KW - Hexafluoropropylene oxide
KW - Static-analytic
KW - Vapor-liquid equilibrium
UR - http://www.scopus.com/inward/record.url?scp=84925002449&partnerID=8YFLogxK
U2 - 10.1016/j.fluid.2015.03.006
DO - 10.1016/j.fluid.2015.03.006
M3 - Article
AN - SCOPUS:84925002449
VL - 394
SP - 88
EP - 92
JO - Fluid Phase Equilibria
JF - Fluid Phase Equilibria
SN - 0378-3812
ER -