Mixture of Ethane + Perfluorooctane

Datasets

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

Mole fraction of Ethane (1) [ref]

Fixed		Measured
Mole fraction of Ethane (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane (1) - Gas
0.0000	308.45	0.0000
0.1146	308.45	0.9885
0.1905	308.45	0.9924
0.2740	308.45	0.9939
0.3470	308.45	0.9943
0.4220	308.45	0.9942
0.5310	308.45	0.9943
0.6410	308.45	0.9937
0.7770	308.45	0.9931
0.8825	308.45	0.9919
0.9700	308.45	0.9915
0.0000	318.42	0.0000
0.1248	318.42	0.9830
0.2050	318.42	0.9874
0.2960	318.42	0.9904
0.3670	318.42	0.9923
0.4490	318.42	0.9919
0.5390	318.42	0.9925
0.6320	318.42	0.9919
0.7301	318.42	0.9908
0.8577	318.42	0.9893
0.9658	318.42	0.9830
0.0000	323.48	0.0000
0.1039	323.48	0.9748
0.1894	323.48	0.9837
0.2553	323.48	0.9884
0.3380	323.48	0.9892
0.4320	323.48	0.9904
0.5230	323.48	0.9908
0.6250	323.48	0.9898
0.7199	323.48	0.9885
0.8472	323.48	0.9874
0.0000	328.48	0.0000
0.1300	328.48	0.9783
0.2050	328.48	0.9845
0.2900	328.48	0.9872
0.3670	328.48	0.9883
0.4450	328.48	0.9886
0.5110	328.48	0.9885
0.6080	328.48	0.9874
0.6844	328.48	0.9860
0.7810	328.48	0.9839
0.0000	338.43	0.0000
0.0960	338.43	0.9588
0.1799	338.43	0.9756
0.2520	338.43	0.9804
0.3290	338.43	0.9829
0.4010	338.43	0.9838
0.4690	338.43	0.9840
0.5330	338.43	0.9833
0.5966	338.43	0.9822
0.6648	338.43	0.9824
0.7424	338.43	0.9764

Mole fraction of Ethane (1) [ref]

Fixed		Measured
Mole fraction of Ethane (1) - Liquid	Temperature, K - Liquid	Mole fraction of Ethane (1) - Gas
0.0000	308.45	0.0000
0.1146	308.45	0.9885
0.1905	308.45	0.9924
0.2740	308.45	0.9939
0.3470	308.45	0.9943
0.4220	308.45	0.9942
0.5310	308.45	0.9943
0.6410	308.45	0.9937
0.7770	308.45	0.9931
0.8825	308.45	0.9919
0.9700	308.45	0.9915
0.0000	318.42	0.0000
0.1248	318.42	0.9830
0.2050	318.42	0.9874
0.2960	318.42	0.9904
0.3670	318.42	0.9923
0.4490	318.42	0.9919
0.5390	318.42	0.9925
0.6320	318.42	0.9919
0.7301	318.42	0.9908
0.8577	318.42	0.9893
0.9658	318.42	0.9830
0.0000	323.48	0.0000
0.1039	323.48	0.9748
0.1894	323.48	0.9837
0.2553	323.48	0.9884
0.3380	323.48	0.9892
0.4320	323.48	0.9904
0.5230	323.48	0.9908
0.6250	323.48	0.9898
0.7199	323.48	0.9885
0.8472	323.48	0.9874
0.0000	328.48	0.0000
0.1300	328.48	0.9783
0.2050	328.48	0.9845
0.2900	328.48	0.9872
0.3670	328.48	0.9883
0.4450	328.48	0.9886
0.5110	328.48	0.9885
0.6080	328.48	0.9874
0.6844	328.48	0.9860
0.7810	328.48	0.9839
0.0000	338.43	0.0000
0.0960	338.43	0.9588
0.1799	338.43	0.9756
0.2520	338.43	0.9804
0.3290	338.43	0.9829
0.4010	338.43	0.9838
0.4690	338.43	0.9840
0.5330	338.43	0.9833
0.5966	338.43	0.9822
0.6648	338.43	0.9824
0.7424	338.43	0.9764

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	308.45	6.10
0.1146	308.45	577.30
0.1905	308.45	982.90
0.2740	308.45	1408.30
0.3470	308.45	1797.40
0.4220	308.45	2238.80
0.5310	308.45	2752.70
0.6410	308.45	3243.30
0.7770	308.45	3782.50
0.8825	308.45	4227.30
0.9700	308.45	4779.20
0.0000	318.42	10.10
0.1248	318.42	714.60
0.2050	318.42	1171.20
0.2960	318.42	1695.90
0.3670	318.42	2185.00
0.4490	318.42	2659.30
0.5390	318.42	3165.60
0.6320	318.42	3651.40
0.7301	318.42	4149.30
0.8577	318.42	4799.30
0.9658	318.42	5476.60
0.0000	323.48	12.80
0.1039	323.48	599.10
0.1894	323.48	1105.90
0.2553	323.48	1523.70
0.3380	323.48	2103.40
0.4320	323.48	2666.10
0.5230	323.48	3259.60
0.6250	323.48	3848.10
0.7199	323.48	4367.00
0.8472	323.48	5083.80
0.0000	328.48	16.00
0.1300	328.48	806.10
0.2050	328.48	1281.40
0.2900	328.48	1818.10
0.3670	328.48	2351.50
0.4450	328.48	2893.70
0.5110	328.48	3394.20
0.6080	328.48	4040.00
0.6844	328.48	4574.00
0.7810	328.48	5304.30
0.0000	338.43	24.30
0.0960	338.43	623.30
0.1799	338.43	1184.10
0.2520	338.43	1700.50
0.3290	338.43	2280.00
0.4010	338.43	2835.80
0.4690	338.43	3365.50
0.5330	338.43	3899.10
0.5966	338.43	4416.90
0.6648	338.43	4972.30
0.7424	338.43	5691.60

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	308.45	6.10
0.1146	308.45	577.30
0.1905	308.45	982.90
0.2740	308.45	1408.30
0.3470	308.45	1797.40
0.4220	308.45	2238.80
0.5310	308.45	2752.70
0.6410	308.45	3243.30
0.7770	308.45	3782.50
0.8825	308.45	4227.30
0.9700	308.45	4779.20
0.0000	318.42	10.10
0.1248	318.42	714.60
0.2050	318.42	1171.20
0.2960	318.42	1695.90
0.3670	318.42	2185.00
0.4490	318.42	2659.30
0.5390	318.42	3165.60
0.6320	318.42	3651.40
0.7301	318.42	4149.30
0.8577	318.42	4799.30
0.9658	318.42	5476.60
0.0000	323.48	12.80
0.1039	323.48	599.10
0.1894	323.48	1105.90
0.2553	323.48	1523.70
0.3380	323.48	2103.40
0.4320	323.48	2666.10
0.5230	323.48	3259.60
0.6250	323.48	3848.10
0.7199	323.48	4367.00
0.8472	323.48	5083.80
0.0000	328.48	16.00
0.1300	328.48	806.10
0.2050	328.48	1281.40
0.2900	328.48	1818.10
0.3670	328.48	2351.50
0.4450	328.48	2893.70
0.5110	328.48	3394.20
0.6080	328.48	4040.00
0.6844	328.48	4574.00
0.7810	328.48	5304.30
0.0000	338.43	24.30
0.0960	338.43	623.30
0.1799	338.43	1184.10
0.2520	338.43	1700.50
0.3290	338.43	2280.00
0.4010	338.43	2835.80
0.4690	338.43	3365.50
0.5330	338.43	3899.10
0.5966	338.43	4416.90
0.6648	338.43	4972.30
0.7424	338.43	5691.60

Sources

• Isothermal vapor-liquid equilibrium of R170 + n-perfluorooctane at 308 - 338 K: Measurement, equation of state modelling, and molecular simulation