Mixture of Propane + Propene, hexafluoro-

Datasets

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

Mole fraction of Propane (1) [ref]

Fixed		Measured
Mole fraction of Propane (1) - Liquid	Temperature, K - Liquid	Mole fraction of Propane (1) - Gas
0.0800	312.90	0.1460
0.1180	312.90	0.2010
0.1720	312.90	0.2650
0.2180	312.90	0.3150
0.3070	312.90	0.3970
0.3900	312.90	0.4630
0.5070	312.90	0.5430
0.6100	312.90	0.6160
0.6900	312.90	0.6720
0.7340	312.90	0.7020
0.8540	312.90	0.8000
0.9400	312.90	0.9040
0.0710	327.88	0.1130
0.1380	327.88	0.2020
0.1980	327.88	0.2700
0.3170	327.88	0.3820
0.3800	327.88	0.4340
0.4530	327.88	0.4910
0.5020	327.88	0.5280
0.6010	327.88	0.6040
0.7060	327.88	0.6820
0.7810	327.88	0.7430
0.8760	327.88	0.8390
0.9200	327.88	0.8860
0.1180	342.92	0.1560
0.2030	342.92	0.2480
0.2870	342.92	0.3280
0.0700	342.92	0.0980
0.3570	342.92	0.3930
0.4720	342.92	0.4870
0.5600	342.92	0.5640
0.6550	342.92	0.6460
0.7600	342.92	0.7350
0.8400	342.92	0.8100
0.9000	342.92	0.8730
0.9600	342.92	0.9450

Mole fraction of Propane (1) [ref]

Fixed		Measured
Mole fraction of Propane (1) - Liquid	Temperature, K - Liquid	Mole fraction of Propane (1) - Gas
0.0800	312.90	0.1460
0.1180	312.90	0.2010
0.1720	312.90	0.2650
0.2180	312.90	0.3150
0.3070	312.90	0.3970
0.3900	312.90	0.4630
0.5070	312.90	0.5430
0.6100	312.90	0.6160
0.6900	312.90	0.6720
0.7340	312.90	0.7020
0.8540	312.90	0.8000
0.9400	312.90	0.9040
0.0710	327.88	0.1130
0.1380	327.88	0.2020
0.1980	327.88	0.2700
0.3170	327.88	0.3820
0.3800	327.88	0.4340
0.4530	327.88	0.4910
0.5020	327.88	0.5280
0.6010	327.88	0.6040
0.7060	327.88	0.6820
0.7810	327.88	0.7430
0.8760	327.88	0.8390
0.9200	327.88	0.8860
0.1180	342.92	0.1560
0.2030	342.92	0.2480
0.2870	342.92	0.3280
0.0700	342.92	0.0980
0.3570	342.92	0.3930
0.4720	342.92	0.4870
0.5600	342.92	0.5640
0.6550	342.92	0.6460
0.7600	342.92	0.7350
0.8400	342.92	0.8100
0.9000	342.92	0.8730
0.9600	342.92	0.9450

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0800	312.90	1233.00
0.1180	312.90	1290.00
0.1720	312.90	1359.00
0.2180	312.90	1408.00
0.3070	312.90	1484.00
0.3900	312.90	1535.00
0.5070	312.90	1582.00
0.6100	312.90	1599.00
0.6900	312.90	1595.00
0.7340	312.90	1588.00
0.8540	312.90	1535.00
0.9400	312.90	1451.00
0.0710	327.88	1741.00
0.1380	327.88	1857.00
0.1980	327.88	1947.00
0.3170	327.88	2079.00
0.3800	327.88	2131.00
0.4530	327.88	2176.00
0.5020	327.88	2197.00
0.6010	327.88	2217.00
0.7060	327.88	2205.00
0.7810	327.88	2171.00
0.8760	327.88	2091.00
0.9200	327.88	2038.00
0.1180	342.92	2527.00
0.2030	342.92	2691.00
0.2870	342.92	2817.00
0.0700	342.92	2416.00
0.3570	342.92	2898.00
0.4720	342.92	2982.00
0.5600	342.92	3007.00
0.6550	342.92	3001.00
0.7600	342.92	2946.00
0.8400	342.92	2861.00
0.9000	342.92	2778.00
0.9600	342.92	2671.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Propane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0800	312.90	1233.00
0.1180	312.90	1290.00
0.1720	312.90	1359.00
0.2180	312.90	1408.00
0.3070	312.90	1484.00
0.3900	312.90	1535.00
0.5070	312.90	1582.00
0.6100	312.90	1599.00
0.6900	312.90	1595.00
0.7340	312.90	1588.00
0.8540	312.90	1535.00
0.9400	312.90	1451.00
0.0710	327.88	1741.00
0.1380	327.88	1857.00
0.1980	327.88	1947.00
0.3170	327.88	2079.00
0.3800	327.88	2131.00
0.4530	327.88	2176.00
0.5020	327.88	2197.00
0.6010	327.88	2217.00
0.7060	327.88	2205.00
0.7810	327.88	2171.00
0.8760	327.88	2091.00
0.9200	327.88	2038.00
0.1180	342.92	2527.00
0.2030	342.92	2691.00
0.2870	342.92	2817.00
0.0700	342.92	2416.00
0.3570	342.92	2898.00
0.4720	342.92	2982.00
0.5600	342.92	3007.00
0.6550	342.92	3001.00
0.7600	342.92	2946.00
0.8400	342.92	2861.00
0.9000	342.92	2778.00
0.9600	342.92	2671.00

Sources

• Phase equilibrium data for mixtures involving 1,1,2,3,3,3-hexafluoro-1-propene with either propane or n-butane between 312 and 343 K