Mixture of Ethylene + nonane, eicosafluoro-

Datasets

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

Mole fraction of Ethylene (1) [ref]

Fixed		Measured
Mole fraction of Ethylene (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethylene (1) - Gas
0.1760	293.21	0.9981
0.2440	293.23	0.9983
0.3240	293.23	0.9985
0.3860	293.24	0.9985
0.4780	293.23	0.9984
0.5440	293.24	0.9983
0.6350	293.24	0.9979
0.7240	293.24	0.9973
0.8370	293.24	0.9954
0.9410	293.24	0.9918
0.1580	308.18	0.9946
0.2170	308.18	0.9971
0.2950	308.18	0.9971
0.3510	308.18	0.9971
0.4600	308.18	0.9970
0.4120	308.19	0.9974
0.5300	308.19	0.9964
0.6080	308.20	0.9958
0.6830	308.20	0.9952
0.7390	308.20	0.9941
0.8150	308.20	0.9899
0.8890	308.20	0.9867
0.1470	323.20	0.9922
0.2600	323.20	0.9946
0.3540	323.20	0.9950
0.4540	323.19	0.9945
0.5120	323.21	0.9943
0.5700	323.20	0.9935
0.6130	323.20	0.9925
0.6800	323.21	0.9905
0.7270	323.21	0.9886
0.7880	323.21	0.9844
0.8400	323.20	0.9778
0.1480	338.21	0.9879
0.2290	338.20	0.9911
0.3200	338.22	0.9914
0.4290	338.21	0.9914
0.5120	338.21	0.9900
0.5490	338.21	0.9893
0.6070	338.22	0.9876
0.6360	338.21	0.9862
0.6820	338.20	0.9839
0.7300	338.20	0.9802
0.7740	338.21	0.9743
0.7970	338.22	0.9708
0.1160	353.21	0.9761
0.2300	353.20	0.9849
0.2970	353.21	0.9860
0.3820	353.21	0.9862
0.4660	353.22	0.9850
0.5390	353.24	0.9831
0.5720	353.21	0.9820
0.5980	353.22	0.9806
0.6360	353.21	0.9783
0.6630	353.21	0.9763
0.7020	353.19	0.9722
0.7490	353.21	0.9651

Mole fraction of Ethylene (1) [ref]

Fixed		Measured
Mole fraction of Ethylene (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethylene (1) - Gas
0.1760	293.21	0.9981
0.2440	293.23	0.9983
0.3240	293.23	0.9985
0.3860	293.24	0.9985
0.4780	293.23	0.9984
0.5440	293.24	0.9983
0.6350	293.24	0.9979
0.7240	293.24	0.9973
0.8370	293.24	0.9954
0.9410	293.24	0.9918
0.1580	308.18	0.9946
0.2170	308.18	0.9971
0.2950	308.18	0.9971
0.3510	308.18	0.9971
0.4600	308.18	0.9970
0.4120	308.19	0.9974
0.5300	308.19	0.9964
0.6080	308.20	0.9958
0.6830	308.20	0.9952
0.7390	308.20	0.9941
0.8150	308.20	0.9899
0.8890	308.20	0.9867
0.1470	323.20	0.9922
0.2600	323.20	0.9946
0.3540	323.20	0.9950
0.4540	323.19	0.9945
0.5120	323.21	0.9943
0.5700	323.20	0.9935
0.6130	323.20	0.9925
0.6800	323.21	0.9905
0.7270	323.21	0.9886
0.7880	323.21	0.9844
0.8400	323.20	0.9778
0.1480	338.21	0.9879
0.2290	338.20	0.9911
0.3200	338.22	0.9914
0.4290	338.21	0.9914
0.5120	338.21	0.9900
0.5490	338.21	0.9893
0.6070	338.22	0.9876
0.6360	338.21	0.9862
0.6820	338.20	0.9839
0.7300	338.20	0.9802
0.7740	338.21	0.9743
0.7970	338.22	0.9708
0.1160	353.21	0.9761
0.2300	353.20	0.9849
0.2970	353.21	0.9860
0.3820	353.21	0.9862
0.4660	353.22	0.9850
0.5390	353.24	0.9831
0.5720	353.21	0.9820
0.5980	353.22	0.9806
0.6360	353.21	0.9783
0.6630	353.21	0.9763
0.7020	353.19	0.9722
0.7490	353.21	0.9651

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethylene (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1760	293.21	1170.00
0.2440	293.23	1620.00
0.3240	293.23	2180.00
0.3860	293.24	2590.00
0.4780	293.23	3220.00
0.5440	293.24	3610.00
0.6350	293.24	4170.00
0.7240	293.24	4650.00
0.8370	293.24	5140.00
0.9410	293.24	5550.00
0.1580	308.18	1140.00
0.2170	308.18	1600.00
0.2950	308.18	2220.00
0.3510	308.18	2670.00
0.4600	308.18	3570.00
0.4120	308.19	3140.00
0.5300	308.19	4120.00
0.6080	308.20	4760.00
0.6830	308.20	5350.00
0.7390	308.20	5750.00
0.8150	308.20	6260.00
0.8890	308.20	6690.00
0.1470	323.20	1220.00
0.2600	323.20	2220.00
0.3540	323.20	3100.00
0.4540	323.19	4070.00
0.5120	323.21	4650.00
0.5700	323.20	5210.00
0.6130	323.20	5640.00
0.6800	323.21	6270.00
0.7270	323.21	6720.00
0.7880	323.21	7260.00
0.8400	323.20	7670.00
0.1480	338.21	1320.00
0.2290	338.20	2100.00
0.3200	338.22	3020.00
0.4290	338.21	4190.00
0.5120	338.21	5130.00
0.5490	338.21	5540.00
0.6070	338.22	6220.00
0.6360	338.21	6560.00
0.6820	338.20	7090.00
0.7300	338.20	7620.00
0.7740	338.21	8100.00
0.7970	338.22	8340.00
0.1160	353.21	1100.00
0.2300	353.20	2270.00
0.2970	353.21	3000.00
0.3820	353.21	3980.00
0.4660	353.22	5000.00
0.5390	353.24	5910.00
0.5720	353.21	6340.00
0.5980	353.22	6680.00
0.6360	353.21	7170.00
0.6630	353.21	7520.00
0.7020	353.19	8030.00
0.7490	353.21	8610.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethylene (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1760	293.21	1170.00
0.2440	293.23	1620.00
0.3240	293.23	2180.00
0.3860	293.24	2590.00
0.4780	293.23	3220.00
0.5440	293.24	3610.00
0.6350	293.24	4170.00
0.7240	293.24	4650.00
0.8370	293.24	5140.00
0.9410	293.24	5550.00
0.1580	308.18	1140.00
0.2170	308.18	1600.00
0.2950	308.18	2220.00
0.3510	308.18	2670.00
0.4600	308.18	3570.00
0.4120	308.19	3140.00
0.5300	308.19	4120.00
0.6080	308.20	4760.00
0.6830	308.20	5350.00
0.7390	308.20	5750.00
0.8150	308.20	6260.00
0.8890	308.20	6690.00
0.1470	323.20	1220.00
0.2600	323.20	2220.00
0.3540	323.20	3100.00
0.4540	323.19	4070.00
0.5120	323.21	4650.00
0.5700	323.20	5210.00
0.6130	323.20	5640.00
0.6800	323.21	6270.00
0.7270	323.21	6720.00
0.7880	323.21	7260.00
0.8400	323.20	7670.00
0.1480	338.21	1320.00
0.2290	338.20	2100.00
0.3200	338.22	3020.00
0.4290	338.21	4190.00
0.5120	338.21	5130.00
0.5490	338.21	5540.00
0.6070	338.22	6220.00
0.6360	338.21	6560.00
0.6820	338.20	7090.00
0.7300	338.20	7620.00
0.7740	338.21	8100.00
0.7970	338.22	8340.00
0.1160	353.21	1100.00
0.2300	353.20	2270.00
0.2970	353.21	3000.00
0.3820	353.21	3980.00
0.4660	353.22	5000.00
0.5390	353.24	5910.00
0.5720	353.21	6340.00
0.5980	353.22	6680.00
0.6360	353.21	7170.00
0.6630	353.21	7520.00
0.7020	353.19	8030.00
0.7490	353.21	8610.00

Sources

• Binary vapour-liquid equilibrium data for C7 and C9 straight-chain perfluorocarbons with ethylene