Mixture of Perfluorooctane + Ethylene

Datasets

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

Mole fraction of Ethylene (2) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Ethylene (2) - Liquid	Mole fraction of Ethylene (2) - Gas
293.25	0.1860	0.9926
293.25	0.2600	0.9949
293.25	0.3430	0.9960
293.25	0.3970	0.9963
293.25	0.4790	0.9955
293.25	0.5720	0.9955
293.25	0.6540	0.9955
293.25	0.7580	0.9952
293.25	0.8570	0.9939
308.19	0.1550	0.9897
308.19	0.2160	0.9922
308.19	0.3130	0.9934
308.19	0.3430	0.9936
308.19	0.4300	0.9935
308.19	0.4800	0.9935
308.19	0.5140	0.9933
308.19	0.5830	0.9927
308.19	0.6630	0.9918
308.19	0.7430	0.9899
308.19	0.8240	0.9864
323.22	0.1140	0.9745
323.22	0.2270	0.9871
323.22	0.2990	0.9887
323.22	0.3540	0.9896
323.22	0.4380	0.9892
323.22	0.5050	0.9881
323.22	0.5510	0.9872
323.22	0.6140	0.9861
323.22	0.6760	0.9839
323.22	0.7400	0.9808
323.22	0.8540	0.9652
338.21	0.1140	0.9692
338.21	0.1810	0.9771
338.21	0.2520	0.9802
338.21	0.2970	0.9826
338.21	0.3480	0.9829
338.21	0.3870	0.9831
338.21	0.4350	0.9831
338.21	0.4770	0.9821
338.21	0.5540	0.9806
338.21	0.6500	0.9759
338.21	0.7400	0.9667
338.21	0.8310	0.9440
353.24	0.1200	0.9529
353.24	0.1540	0.9609
353.24	0.2240	0.9689
353.24	0.2730	0.9717
353.24	0.3320	0.9730
353.24	0.3780	0.9739
353.24	0.4430	0.9731
353.24	0.5020	0.9719
353.24	0.5770	0.9682
353.24	0.6160	0.9654
353.24	0.6550	0.9617
353.24	0.7050	0.9544
353.24	0.7720	0.9384

Mole fraction of Ethylene (2) [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of Ethylene (2) - Liquid	Mole fraction of Ethylene (2) - Gas
293.25	0.1860	0.9926
293.25	0.2600	0.9949
293.25	0.3430	0.9960
293.25	0.3970	0.9963
293.25	0.4790	0.9955
293.25	0.5720	0.9955
293.25	0.6540	0.9955
293.25	0.7580	0.9952
293.25	0.8570	0.9939
308.19	0.1550	0.9897
308.19	0.2160	0.9922
308.19	0.3130	0.9934
308.19	0.3430	0.9936
308.19	0.4300	0.9935
308.19	0.4800	0.9935
308.19	0.5140	0.9933
308.19	0.5830	0.9927
308.19	0.6630	0.9918
308.19	0.7430	0.9899
308.19	0.8240	0.9864
323.22	0.1140	0.9745
323.22	0.2270	0.9871
323.22	0.2990	0.9887
323.22	0.3540	0.9896
323.22	0.4380	0.9892
323.22	0.5050	0.9881
323.22	0.5510	0.9872
323.22	0.6140	0.9861
323.22	0.6760	0.9839
323.22	0.7400	0.9808
323.22	0.8540	0.9652
338.21	0.1140	0.9692
338.21	0.1810	0.9771
338.21	0.2520	0.9802
338.21	0.2970	0.9826
338.21	0.3480	0.9829
338.21	0.3870	0.9831
338.21	0.4350	0.9831
338.21	0.4770	0.9821
338.21	0.5540	0.9806
338.21	0.6500	0.9759
338.21	0.7400	0.9667
338.21	0.8310	0.9440
353.24	0.1200	0.9529
353.24	0.1540	0.9609
353.24	0.2240	0.9689
353.24	0.2730	0.9717
353.24	0.3320	0.9730
353.24	0.3780	0.9739
353.24	0.4430	0.9731
353.24	0.5020	0.9719
353.24	0.5770	0.9682
353.24	0.6160	0.9654
353.24	0.6550	0.9617
353.24	0.7050	0.9544
353.24	0.7720	0.9384

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylene (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
293.25	0.1860	1218.00
293.25	0.2600	1710.00
293.25	0.3430	2284.00
293.25	0.3970	2632.00
293.25	0.4790	3160.00
293.25	0.5720	3718.00
293.25	0.6540	4174.00
293.25	0.7580	4670.00
293.25	0.8570	5085.00
308.19	0.1550	1149.00
308.19	0.2160	1622.00
308.19	0.3130	2345.00
308.19	0.3430	2589.00
308.19	0.4300	3284.00
308.19	0.4800	3688.00
308.19	0.5140	3957.00
308.19	0.5830	4483.00
308.19	0.6630	5068.00
308.19	0.7430	5615.00
308.19	0.8240	6118.00
323.22	0.1140	932.00
323.22	0.2270	1902.00
323.22	0.2990	2519.00
323.22	0.3540	3018.00
323.22	0.4380	3816.00
323.22	0.5050	4441.00
323.22	0.5510	4873.00
323.22	0.6140	5457.00
323.22	0.6760	6014.00
323.22	0.7400	6575.00
323.22	0.8540	7459.00
338.21	0.1140	1065.00
338.21	0.1810	1655.00
338.21	0.2520	2343.00
338.21	0.2970	2802.00
338.21	0.3480	3314.00
338.21	0.3870	3726.00
338.21	0.4350	4236.00
338.21	0.4770	4676.00
338.21	0.5540	5517.00
338.21	0.6500	6542.00
338.21	0.7400	7484.00
338.21	0.8310	8278.00
353.24	0.1200	1178.00
353.24	0.1540	1494.00
353.24	0.2240	2205.00
353.24	0.2730	2691.00
353.24	0.3320	3367.00
353.24	0.3780	3880.00
353.24	0.4430	4624.00
353.24	0.5020	5325.00
353.24	0.5770	6230.00
353.24	0.6160	6700.00
353.24	0.6550	7171.00
353.24	0.7050	7751.00
353.24	0.7720	8447.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethylene (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
293.25	0.1860	1218.00
293.25	0.2600	1710.00
293.25	0.3430	2284.00
293.25	0.3970	2632.00
293.25	0.4790	3160.00
293.25	0.5720	3718.00
293.25	0.6540	4174.00
293.25	0.7580	4670.00
293.25	0.8570	5085.00
308.19	0.1550	1149.00
308.19	0.2160	1622.00
308.19	0.3130	2345.00
308.19	0.3430	2589.00
308.19	0.4300	3284.00
308.19	0.4800	3688.00
308.19	0.5140	3957.00
308.19	0.5830	4483.00
308.19	0.6630	5068.00
308.19	0.7430	5615.00
308.19	0.8240	6118.00
323.22	0.1140	932.00
323.22	0.2270	1902.00
323.22	0.2990	2519.00
323.22	0.3540	3018.00
323.22	0.4380	3816.00
323.22	0.5050	4441.00
323.22	0.5510	4873.00
323.22	0.6140	5457.00
323.22	0.6760	6014.00
323.22	0.7400	6575.00
323.22	0.8540	7459.00
338.21	0.1140	1065.00
338.21	0.1810	1655.00
338.21	0.2520	2343.00
338.21	0.2970	2802.00
338.21	0.3480	3314.00
338.21	0.3870	3726.00
338.21	0.4350	4236.00
338.21	0.4770	4676.00
338.21	0.5540	5517.00
338.21	0.6500	6542.00
338.21	0.7400	7484.00
338.21	0.8310	8278.00
353.24	0.1200	1178.00
353.24	0.1540	1494.00
353.24	0.2240	2205.00
353.24	0.2730	2691.00
353.24	0.3320	3367.00
353.24	0.3780	3880.00
353.24	0.4430	4624.00
353.24	0.5020	5325.00
353.24	0.5770	6230.00
353.24	0.6160	6700.00
353.24	0.6550	7171.00
353.24	0.7050	7751.00
353.24	0.7720	8447.00

Sources

• High-pressure phase equilibria data for mixtures involving ethene and perfluoro-n-octane from 293 to 353 K