Mixture of Ethene, tetrafluoro- + Propene, hexafluoro-

Datasets

1. Mole fraction (2)
2. P_vap - Vapor or sublimation pressure, kPa (2)

Mole fraction of Ethene, tetrafluoro- (1) [ref]

Fixed		Measured
Mole fraction of Ethene, tetrafluoro- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethene, tetrafluoro- (1) - Gas
0.0000	248.14	0.0000
0.2180	248.14	0.6200
0.2700	248.14	0.6710
0.3380	248.14	0.7350
0.4030	248.14	0.7820
0.4920	248.14	0.8330
0.5430	248.14	0.8580
0.6020	248.14	0.8840
0.6480	248.14	0.9000
0.7030	248.14	0.9190
0.0000	263.01	0.0000
0.1200	263.01	0.3910
0.2290	263.01	0.5580
0.3310	263.01	0.6790
0.4220	263.01	0.7520
0.5000	263.01	0.8020
0.5680	263.01	0.8250
0.6270	263.01	0.8680
0.7130	263.01	0.9040
0.7850	263.01	0.9310
0.0000	282.89	0.0000
0.0710	282.89	0.2200
0.1440	282.89	0.3810
0.2630	282.89	0.5570
0.3670	282.89	0.6630
0.4430	282.89	0.7200
0.5070	282.89	0.7570
0.5700	282.89	0.8010
0.6260	282.89	0.8380
0.6770	282.89	0.8600
0.7390	282.89	0.8890
0.7900	282.89	0.9130
0.8320	282.89	0.9280

Mole fraction of Ethene, tetrafluoro- (1) [ref]

Fixed		Measured
Mole fraction of Ethene, tetrafluoro- (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethene, tetrafluoro- (1) - Gas
0.0000	248.14	0.0000
0.2180	248.14	0.6200
0.2700	248.14	0.6710
0.3380	248.14	0.7350
0.4030	248.14	0.7820
0.4920	248.14	0.8330
0.5430	248.14	0.8580
0.6020	248.14	0.8840
0.6480	248.14	0.9000
0.7030	248.14	0.9190
0.0000	263.01	0.0000
0.1200	263.01	0.3910
0.2290	263.01	0.5580
0.3310	263.01	0.6790
0.4220	263.01	0.7520
0.5000	263.01	0.8020
0.5680	263.01	0.8250
0.6270	263.01	0.8680
0.7130	263.01	0.9040
0.7850	263.01	0.9310
0.0000	282.89	0.0000
0.0710	282.89	0.2200
0.1440	282.89	0.3810
0.2630	282.89	0.5570
0.3670	282.89	0.6630
0.4430	282.89	0.7200
0.5070	282.89	0.7570
0.5700	282.89	0.8010
0.6260	282.89	0.8380
0.6770	282.89	0.8600
0.7390	282.89	0.8890
0.7900	282.89	0.9130
0.8320	282.89	0.9280

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethene, tetrafluoro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	248.14	120.20
0.2180	248.14	258.10
0.2700	248.14	300.40
0.3380	248.14	348.40
0.4030	248.14	394.40
0.4920	248.14	461.60
0.5430	248.14	489.90
0.6020	248.14	536.50
0.6480	248.14	573.40
0.7030	248.14	620.00
0.0000	263.01	224.60
0.1200	263.01	340.20
0.2290	263.01	440.80
0.3310	263.01	545.90
0.4220	263.01	645.30
0.5000	263.01	757.60
0.5680	263.01	807.80
0.6270	263.01	886.30
0.7130	263.01	986.60
0.7850	263.01	1075.50
0.0000	282.89	456.10
0.0710	282.89	551.00
0.1440	282.89	671.00
0.2630	282.89	854.70
0.3670	282.89	1041.40
0.4430	282.89	1165.90
0.5070	282.89	1282.10
0.5700	282.89	1396.50
0.6260	282.89	1509.40
0.6770	282.89	1622.00
0.7390	282.89	1759.90
0.7900	282.89	1873.60
0.8320	282.89	1956.40

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethene, tetrafluoro- (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	248.14	120.20
0.2180	248.14	258.10
0.2700	248.14	300.40
0.3380	248.14	348.40
0.4030	248.14	394.40
0.4920	248.14	461.60
0.5430	248.14	489.90
0.6020	248.14	536.50
0.6480	248.14	573.40
0.7030	248.14	620.00
0.0000	263.01	224.60
0.1200	263.01	340.20
0.2290	263.01	440.80
0.3310	263.01	545.90
0.4220	263.01	645.30
0.5000	263.01	757.60
0.5680	263.01	807.80
0.6270	263.01	886.30
0.7130	263.01	986.60
0.7850	263.01	1075.50
0.0000	282.89	456.10
0.0710	282.89	551.00
0.1440	282.89	671.00
0.2630	282.89	854.70
0.3670	282.89	1041.40
0.4430	282.89	1165.90
0.5070	282.89	1282.10
0.5700	282.89	1396.50
0.6260	282.89	1509.40
0.6770	282.89	1622.00
0.7390	282.89	1759.90
0.7900	282.89	1873.60
0.8320	282.89	1956.40

Sources

• Isothermal Vapor Liquid Equilibrium Data for the 1,1,2,2-Tetrafluoroethene + 1,1,2,3,3,3-Hexafluoroprop-1-ene Binary System: Measurement and Modeling from (248 to 283) K