Mixture of Butane, decafluoro- + Ethylene

Datasets

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

Mole fraction of Ethylene (2) [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethylene (2) - Gas
0.0000	268.13	0.0000
0.0000	278.36	0.0000
0.0000	288.16	0.0000
0.0000	298.13	0.0000
0.0440	298.13	0.5030
0.0450	288.16	0.5890
0.0490	278.36	0.6360
0.0660	268.13	0.7440
0.1050	278.36	0.7940
0.1100	288.16	0.7390
0.1100	298.13	0.7060
0.1270	268.13	0.8480
0.1640	278.36	0.8570
0.1690	288.16	0.8070
0.1740	298.13	0.7930
0.1940	268.13	0.8880
0.2160	278.36	0.8810
0.2220	288.16	0.8470
0.2680	298.13	0.8290
0.2830	268.13	0.9110
0.2840	278.36	0.9000
0.2860	288.16	0.8710
0.3290	298.13	0.8520
0.3510	278.36	0.9110
0.3510	288.16	0.8860
0.3710	268.13	0.9260
0.4010	298.13	0.8720
0.4060	288.16	0.8960
0.4270	278.36	0.9100
0.4490	288.16	0.9010
0.4630	268.13	0.9310
0.4830	298.13	0.8870
0.4990	288.16	0.9070
0.5110	278.36	0.9200
0.5640	298.13	0.8880
0.5750	268.13	0.9410
0.5860	278.36	0.9270
0.5860	288.16	0.9160
0.6140	298.13	0.8960
0.6660	268.13	0.9470
0.6720	288.16	0.9210
0.6850	278.36	0.9270
0.6980	298.13	0.9040
0.7390	288.16	0.9270
0.7710	278.36	0.9350
0.7750	268.13	0.9550
0.7810	298.13	0.9130
0.8230	298.13	0.9160
0.8260	278.36	0.9410
0.8510	268.13	0.9570
0.9080	268.13	0.9670
0.9160	288.16	0.9370
0.9190	278.36	0.9570
0.9520	268.13	0.9810
1.0000	268.13	1.0000
1.0000	278.36	1.0000

Mole fraction of Ethylene (2) [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethylene (2) - Gas
0.0000	268.13	0.0000
0.0000	278.36	0.0000
0.0000	288.16	0.0000
0.0000	298.13	0.0000
0.0440	298.13	0.5030
0.0450	288.16	0.5890
0.0490	278.36	0.6360
0.0660	268.13	0.7440
0.1050	278.36	0.7940
0.1100	288.16	0.7390
0.1100	298.13	0.7060
0.1270	268.13	0.8480
0.1640	278.36	0.8570
0.1690	288.16	0.8070
0.1740	298.13	0.7930
0.1940	268.13	0.8880
0.2160	278.36	0.8810
0.2220	288.16	0.8470
0.2680	298.13	0.8290
0.2830	268.13	0.9110
0.2840	278.36	0.9000
0.2860	288.16	0.8710
0.3290	298.13	0.8520
0.3510	278.36	0.9110
0.3510	288.16	0.8860
0.3710	268.13	0.9260
0.4010	298.13	0.8720
0.4060	288.16	0.8960
0.4270	278.36	0.9100
0.4490	288.16	0.9010
0.4630	268.13	0.9310
0.4830	298.13	0.8870
0.4990	288.16	0.9070
0.5110	278.36	0.9200
0.5640	298.13	0.8880
0.5750	268.13	0.9410
0.5860	278.36	0.9270
0.5860	288.16	0.9160
0.6140	298.13	0.8960
0.6660	268.13	0.9470
0.6720	288.16	0.9210
0.6850	278.36	0.9270
0.6980	298.13	0.9040
0.7390	288.16	0.9270
0.7710	278.36	0.9350
0.7750	268.13	0.9550
0.7810	298.13	0.9130
0.8230	298.13	0.9160
0.8260	278.36	0.9410
0.8510	268.13	0.9570
0.9080	268.13	0.9670
0.9160	288.16	0.9370
0.9190	278.36	0.9570
0.9520	268.13	0.9810
1.0000	268.13	1.0000
1.0000	278.36	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	268.13	91.00
0.0000	278.36	134.60
0.0000	288.16	192.90
0.0000	298.13	268.80
0.0440	298.13	570.90
0.0450	288.16	485.40
0.0490	278.36	418.10
0.0660	268.13	434.00
0.1050	278.36	764.60
0.1100	288.16	904.70
0.1100	298.13	1051.40
0.1270	268.13	763.50
0.1640	278.36	1139.30
0.1690	288.16	1300.80
0.1740	298.13	1557.50
0.1940	268.13	1114.80
0.2160	278.36	1414.40
0.2220	288.16	1643.10
0.2680	298.13	2156.80
0.2830	268.13	1480.80
0.2840	278.36	1732.50
0.2860	288.16	1999.60
0.3290	298.13	2511.00
0.3510	278.36	2026.10
0.3510	288.16	2316.50
0.3710	268.13	1791.00
0.4010	298.13	2902.60
0.4060	288.16	2573.90
0.4270	278.36	2322.20
0.4490	288.16	2764.30
0.4630	268.13	2078.90
0.4830	298.13	3317.60
0.4990	288.16	2977.20
0.5110	278.36	2616.70
0.5640	298.13	3703.40
0.5750	268.13	2377.80
0.5860	278.36	2862.80
0.5860	288.16	3324.50
0.6140	298.13	4083.40
0.6660	268.13	2595.30
0.6720	288.16	3667.60
0.6850	278.36	3179.60
0.6980	298.13	4499.90
0.7390	288.16	3944.20
0.7710	278.36	3459.40
0.7750	268.13	2859.50
0.7810	298.13	4931.40
0.8230	298.13	5115.20
0.8260	278.36	3655.10
0.8510	268.13	3062.10
0.9080	268.13	3247.10
0.9160	288.16	4874.50
0.9190	278.36	4077.20
0.9520	268.13	3455.60
1.0000	268.13	3648.50
1.0000	278.36	4611.20

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	268.13	91.00
0.0000	278.36	134.60
0.0000	288.16	192.90
0.0000	298.13	268.80
0.0440	298.13	570.90
0.0450	288.16	485.40
0.0490	278.36	418.10
0.0660	268.13	434.00
0.1050	278.36	764.60
0.1100	288.16	904.70
0.1100	298.13	1051.40
0.1270	268.13	763.50
0.1640	278.36	1139.30
0.1690	288.16	1300.80
0.1740	298.13	1557.50
0.1940	268.13	1114.80
0.2160	278.36	1414.40
0.2220	288.16	1643.10
0.2680	298.13	2156.80
0.2830	268.13	1480.80
0.2840	278.36	1732.50
0.2860	288.16	1999.60
0.3290	298.13	2511.00
0.3510	278.36	2026.10
0.3510	288.16	2316.50
0.3710	268.13	1791.00
0.4010	298.13	2902.60
0.4060	288.16	2573.90
0.4270	278.36	2322.20
0.4490	288.16	2764.30
0.4630	268.13	2078.90
0.4830	298.13	3317.60
0.4990	288.16	2977.20
0.5110	278.36	2616.70
0.5640	298.13	3703.40
0.5750	268.13	2377.80
0.5860	278.36	2862.80
0.5860	288.16	3324.50
0.6140	298.13	4083.40
0.6660	268.13	2595.30
0.6720	288.16	3667.60
0.6850	278.36	3179.60
0.6980	298.13	4499.90
0.7390	288.16	3944.20
0.7710	278.36	3459.40
0.7750	268.13	2859.50
0.7810	298.13	4931.40
0.8230	298.13	5115.20
0.8260	278.36	3655.10
0.8510	268.13	3062.10
0.9080	268.13	3247.10
0.9160	288.16	4874.50
0.9190	278.36	4077.20
0.9520	268.13	3455.60
1.0000	268.13	3648.50
1.0000	278.36	4611.20

Sources

• Vapor-liquid equilibria of ethylene (C2H4) + decafluorobutane (C4F10) at 268 to 298 K from experiment, molecular simulation and the Peng-Robinson equation of state