Mixture of 1-Butene + Propene, hexafluoro-

Datasets

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

Mole fraction of Propene, hexafluoro- (2) [ref]

Fixed		Measured
Mole fraction of Propene, hexafluoro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propene, hexafluoro- (2) - Gas
0.0400	313.05	0.1860
0.1060	313.05	0.3440
0.2010	313.05	0.4640
0.3690	313.05	0.5850
0.5150	313.05	0.6630
0.6500	313.05	0.7350
0.7180	313.05	0.7750
0.7800	313.05	0.8150
0.4670	313.05	0.6360
0.6770	313.05	0.7500
0.7810	313.05	0.8150
0.9110	313.05	0.9200
0.9390	313.05	0.9440
0.0500	327.81	0.1920
0.0600	327.81	0.2190
0.0770	327.81	0.2600
0.1410	327.81	0.3670
0.1960	327.81	0.4320
0.3010	327.81	0.5060
0.3780	327.81	0.5600
0.5210	327.81	0.6370
0.7130	327.81	0.7540
0.7300	327.81	0.7680
0.8360	327.81	0.8470
0.0260	343.10	0.1020
0.0980	343.10	0.2680
0.1800	343.10	0.3780
0.2870	343.10	0.4750
0.3610	343.10	0.5270
0.4730	343.10	0.5860
0.5620	343.10	0.6490
0.6420	343.10	0.7020
0.7360	343.10	0.7670
0.8600	343.10	0.8690

Mole fraction of Propene, hexafluoro- (2) [ref]

Fixed		Measured
Mole fraction of Propene, hexafluoro- (2) - Liquid	Temperature, K - Liquid	Mole fraction of Propene, hexafluoro- (2) - Gas
0.0400	313.05	0.1860
0.1060	313.05	0.3440
0.2010	313.05	0.4640
0.3690	313.05	0.5850
0.5150	313.05	0.6630
0.6500	313.05	0.7350
0.7180	313.05	0.7750
0.7800	313.05	0.8150
0.4670	313.05	0.6360
0.6770	313.05	0.7500
0.7810	313.05	0.8150
0.9110	313.05	0.9200
0.9390	313.05	0.9440
0.0500	327.81	0.1920
0.0600	327.81	0.2190
0.0770	327.81	0.2600
0.1410	327.81	0.3670
0.1960	327.81	0.4320
0.3010	327.81	0.5060
0.3780	327.81	0.5600
0.5210	327.81	0.6370
0.7130	327.81	0.7540
0.7300	327.81	0.7680
0.8360	327.81	0.8470
0.0260	343.10	0.1020
0.0980	343.10	0.2680
0.1800	343.10	0.3780
0.2870	343.10	0.4750
0.3610	343.10	0.5270
0.4730	343.10	0.5860
0.5620	343.10	0.6490
0.6420	343.10	0.7020
0.7360	343.10	0.7670
0.8600	343.10	0.8690

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propene, hexafluoro- (2) - Liquid	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Liquid
0.0400	313.05	547.00
0.1060	313.05	664.00
0.2010	313.05	779.00
0.3690	313.05	907.00
0.5150	313.05	983.00
0.6500	313.05	1033.00
0.7180	313.05	1054.00
0.7800	313.05	1065.00
0.4670	313.05	957.00
0.6770	313.05	1040.00
0.7810	313.05	1068.00
0.9110	313.05	1078.00
0.9390	313.05	1081.00
0.0500	327.81	821.00
0.0600	327.81	848.00
0.0770	327.81	897.00
0.1410	327.81	1017.00
0.1960	327.81	1108.00
0.3010	327.81	1232.00
0.3780	327.81	1293.00
0.5210	327.81	1402.00
0.7130	327.81	1510.00
0.7300	327.81	1518.00
0.8360	327.81	1557.00
0.0260	343.10	1076.00
0.0980	343.10	1305.00
0.1800	343.10	1499.00
0.2870	343.10	1690.00
0.3610	343.10	1791.00
0.4730	343.10	1910.00
0.5620	343.10	2021.00
0.6420	343.10	2086.00
0.7360	343.10	2151.00
0.8600	343.10	2215.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propene, hexafluoro- (2) - Liquid	Temperature, K - Gas	Vapor or sublimation pressure, kPa - Liquid
0.0400	313.05	547.00
0.1060	313.05	664.00
0.2010	313.05	779.00
0.3690	313.05	907.00
0.5150	313.05	983.00
0.6500	313.05	1033.00
0.7180	313.05	1054.00
0.7800	313.05	1065.00
0.4670	313.05	957.00
0.6770	313.05	1040.00
0.7810	313.05	1068.00
0.9110	313.05	1078.00
0.9390	313.05	1081.00
0.0500	327.81	821.00
0.0600	327.81	848.00
0.0770	327.81	897.00
0.1410	327.81	1017.00
0.1960	327.81	1108.00
0.3010	327.81	1232.00
0.3780	327.81	1293.00
0.5210	327.81	1402.00
0.7130	327.81	1510.00
0.7300	327.81	1518.00
0.8360	327.81	1557.00
0.0260	343.10	1076.00
0.0980	343.10	1305.00
0.1800	343.10	1499.00
0.2870	343.10	1690.00
0.3610	343.10	1791.00
0.4730	343.10	1910.00
0.5620	343.10	2021.00
0.6420	343.10	2086.00
0.7360	343.10	2151.00
0.8600	343.10	2215.00

Sources

• Experimental vapour liquid equilibrium data and modeling for binary mixtures of 1-butene with 1,1,2,3,3,3-hexafluoro-1-propene, 2,2,3-trifluoro-3-(trifluoromethyl)oxirane, or difluoromethane