Mixture of Heptane, hexadecafluoro- + 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
0.1920	308.20	0.9822
0.2660	308.19	0.9859
0.3570	308.18	0.9874
0.4250	308.17	0.9879
0.4940	308.18	0.9879
0.5740	308.18	0.9870
0.6310	308.18	0.9862
0.7080	308.19	0.9846
0.7920	308.19	0.9758
0.8590	308.19	0.9724
0.1280	323.18	0.9634
0.2350	323.18	0.9752
0.3600	323.18	0.9788
0.4200	323.18	0.9793
0.4900	323.18	0.9790
0.5370	323.18	0.9782
0.5940	323.18	0.9768
0.6490	323.19	0.9751
0.7260	323.19	0.9705
0.7730	323.19	0.9659
0.8430	323.19	0.9525
0.1360	338.18	0.9447
0.2300	338.18	0.9605
0.3180	338.18	0.9661
0.4350	338.21	0.9680
0.4990	338.19	0.9672
0.5390	338.20	0.9661
0.6020	338.18	0.9633
0.6460	338.20	0.9605
0.6970	338.20	0.9556
0.7280	338.18	0.9512
0.7910	338.18	0.9375

Mole fraction of Ethylene (2) [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethylene (2) - Gas
0.1920	308.20	0.9822
0.2660	308.19	0.9859
0.3570	308.18	0.9874
0.4250	308.17	0.9879
0.4940	308.18	0.9879
0.5740	308.18	0.9870
0.6310	308.18	0.9862
0.7080	308.19	0.9846
0.7920	308.19	0.9758
0.8590	308.19	0.9724
0.1280	323.18	0.9634
0.2350	323.18	0.9752
0.3600	323.18	0.9788
0.4200	323.18	0.9793
0.4900	323.18	0.9790
0.5370	323.18	0.9782
0.5940	323.18	0.9768
0.6490	323.19	0.9751
0.7260	323.19	0.9705
0.7730	323.19	0.9659
0.8430	323.19	0.9525
0.1360	338.18	0.9447
0.2300	338.18	0.9605
0.3180	338.18	0.9661
0.4350	338.21	0.9680
0.4990	338.19	0.9672
0.5390	338.20	0.9661
0.6020	338.18	0.9633
0.6460	338.20	0.9605
0.6970	338.20	0.9556
0.7280	338.18	0.9512
0.7910	338.18	0.9375

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1920	308.20	1380.00
0.2660	308.19	1920.00
0.3570	308.18	2590.00
0.4250	308.17	3080.00
0.4940	308.18	3590.00
0.5740	308.18	4180.00
0.6310	308.18	4580.00
0.7080	308.19	5100.00
0.7920	308.19	5660.00
0.8590	308.19	6090.00
0.1280	323.18	1070.00
0.2350	323.18	1950.00
0.3600	323.18	3030.00
0.4200	323.18	3550.00
0.4900	323.18	4160.00
0.5370	323.18	4560.00
0.5940	323.18	5050.00
0.6490	323.19	5510.00
0.7260	323.19	6160.00
0.7730	323.19	6530.00
0.8430	323.19	7050.00
0.1360	338.18	1230.00
0.2300	338.18	2090.00
0.3180	338.18	2900.00
0.4350	338.21	4050.00
0.4990	338.19	4670.00
0.5390	338.20	5080.00
0.6020	338.18	5720.00
0.6460	338.20	6150.00
0.6970	338.20	6650.00
0.7280	338.18	6960.00
0.7910	338.18	7510.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1920	308.20	1380.00
0.2660	308.19	1920.00
0.3570	308.18	2590.00
0.4250	308.17	3080.00
0.4940	308.18	3590.00
0.5740	308.18	4180.00
0.6310	308.18	4580.00
0.7080	308.19	5100.00
0.7920	308.19	5660.00
0.8590	308.19	6090.00
0.1280	323.18	1070.00
0.2350	323.18	1950.00
0.3600	323.18	3030.00
0.4200	323.18	3550.00
0.4900	323.18	4160.00
0.5370	323.18	4560.00
0.5940	323.18	5050.00
0.6490	323.19	5510.00
0.7260	323.19	6160.00
0.7730	323.19	6530.00
0.8430	323.19	7050.00
0.1360	338.18	1230.00
0.2300	338.18	2090.00
0.3180	338.18	2900.00
0.4350	338.21	4050.00
0.4990	338.19	4670.00
0.5390	338.20	5080.00
0.6020	338.18	5720.00
0.6460	338.20	6150.00
0.6970	338.20	6650.00
0.7280	338.18	6960.00
0.7910	338.18	7510.00

Sources

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