Mixture of Propene, hexafluoro- + 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
0.1500	258.35	0.7160
0.2960	258.35	0.8370
0.4430	258.35	0.8860
0.6210	258.35	0.9190
0.7390	258.35	0.9380
0.8380	258.35	0.9570
0.9040	258.35	0.9690
0.9650	258.35	0.9870
0.0880	268.24	0.5410
0.2290	268.24	0.7460
0.3350	268.24	0.8170
0.4430	268.24	0.8570
0.5810	268.24	0.8920
0.7010	268.24	0.9180
0.8370	268.24	0.9460
0.9400	268.24	0.9750
0.0690	278.10	0.4210
0.2000	278.10	0.6750
0.3020	278.10	0.7630
0.4520	278.10	0.8240
0.5450	278.10	0.8510
0.6430	278.10	0.8780
0.7120	278.10	0.8930
0.8380	278.10	0.9240
0.1200	288.06	0.5000
0.2320	288.06	0.6610
0.3460	288.06	0.7490
0.4250	288.06	0.7910
0.5290	288.06	0.8240
0.6280	288.06	0.8530
0.7380	288.06	0.8810
0.8520	288.06	0.9110
0.0580	297.42	0.2760
0.1260	297.42	0.4650
0.2090	297.42	0.5790
0.3010	297.42	0.6630
0.4000	297.42	0.7190
0.5070	297.42	0.7600
0.6160	297.42	0.7950
0.7220	297.42	0.8180
0.0740	307.38	0.3060
0.1640	307.38	0.4780
0.2590	307.38	0.5720
0.3470	307.38	0.6340
0.4530	307.38	0.6770
0.5960	307.38	0.7210

Mole fraction of Ethylene (2) [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Mole fraction of Ethylene (2) - Gas
0.1500	258.35	0.7160
0.2960	258.35	0.8370
0.4430	258.35	0.8860
0.6210	258.35	0.9190
0.7390	258.35	0.9380
0.8380	258.35	0.9570
0.9040	258.35	0.9690
0.9650	258.35	0.9870
0.0880	268.24	0.5410
0.2290	268.24	0.7460
0.3350	268.24	0.8170
0.4430	268.24	0.8570
0.5810	268.24	0.8920
0.7010	268.24	0.9180
0.8370	268.24	0.9460
0.9400	268.24	0.9750
0.0690	278.10	0.4210
0.2000	278.10	0.6750
0.3020	278.10	0.7630
0.4520	278.10	0.8240
0.5450	278.10	0.8510
0.6430	278.10	0.8780
0.7120	278.10	0.8930
0.8380	278.10	0.9240
0.1200	288.06	0.5000
0.2320	288.06	0.6610
0.3460	288.06	0.7490
0.4250	288.06	0.7910
0.5290	288.06	0.8240
0.6280	288.06	0.8530
0.7380	288.06	0.8810
0.8520	288.06	0.9110
0.0580	297.42	0.2760
0.1260	297.42	0.4650
0.2090	297.42	0.5790
0.3010	297.42	0.6630
0.4000	297.42	0.7190
0.5070	297.42	0.7600
0.6160	297.42	0.7950
0.7220	297.42	0.8180
0.0740	307.38	0.3060
0.1640	307.38	0.4780
0.2590	307.38	0.5720
0.3470	307.38	0.6340
0.4530	307.38	0.6770
0.5960	307.38	0.7210

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1500	258.35	639.00
0.2960	258.35	1082.00
0.4430	258.35	1500.00
0.6210	258.35	1914.00
0.7390	258.35	2192.00
0.8380	258.35	2415.00
0.9040	258.35	2596.00
0.9650	258.35	2762.00
0.0880	268.24	601.00
0.2290	268.24	1097.00
0.3350	268.24	1472.00
0.4430	268.24	1811.00
0.5810	268.24	2244.00
0.7010	268.24	2603.00
0.8370	268.24	3024.00
0.9400	268.24	3417.00
0.0690	278.10	694.00
0.2000	278.10	1237.00
0.3020	278.10	1677.00
0.4520	278.10	2254.00
0.5450	278.10	2603.00
0.6430	278.10	2977.00
0.7120	278.10	3224.00
0.8380	278.10	3704.00
0.1200	288.06	1109.00
0.2320	288.06	1667.00
0.3460	288.06	2208.00
0.4250	288.06	2572.00
0.5290	288.06	3040.00
0.6280	288.06	3493.00
0.7380	288.06	4015.00
0.8520	288.06	4559.00
0.0580	297.42	1011.00
0.1260	297.42	1390.00
0.2090	297.42	1821.00
0.3010	297.42	2300.00
0.4000	297.42	2834.00
0.5070	297.42	3358.00
0.6160	297.42	3912.00
0.7220	297.42	4457.00
0.0740	307.38	1410.00
0.1640	307.38	1942.00
0.2590	307.38	2456.00
0.3470	307.38	2948.00
0.4530	307.38	3516.00
0.5960	307.38	4284.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Ethylene (2) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.1500	258.35	639.00
0.2960	258.35	1082.00
0.4430	258.35	1500.00
0.6210	258.35	1914.00
0.7390	258.35	2192.00
0.8380	258.35	2415.00
0.9040	258.35	2596.00
0.9650	258.35	2762.00
0.0880	268.24	601.00
0.2290	268.24	1097.00
0.3350	268.24	1472.00
0.4430	268.24	1811.00
0.5810	268.24	2244.00
0.7010	268.24	2603.00
0.8370	268.24	3024.00
0.9400	268.24	3417.00
0.0690	278.10	694.00
0.2000	278.10	1237.00
0.3020	278.10	1677.00
0.4520	278.10	2254.00
0.5450	278.10	2603.00
0.6430	278.10	2977.00
0.7120	278.10	3224.00
0.8380	278.10	3704.00
0.1200	288.06	1109.00
0.2320	288.06	1667.00
0.3460	288.06	2208.00
0.4250	288.06	2572.00
0.5290	288.06	3040.00
0.6280	288.06	3493.00
0.7380	288.06	4015.00
0.8520	288.06	4559.00
0.0580	297.42	1011.00
0.1260	297.42	1390.00
0.2090	297.42	1821.00
0.3010	297.42	2300.00
0.4000	297.42	2834.00
0.5070	297.42	3358.00
0.6160	297.42	3912.00
0.7220	297.42	4457.00
0.0740	307.38	1410.00
0.1640	307.38	1942.00
0.2590	307.38	2456.00
0.3470	307.38	2948.00
0.4530	307.38	3516.00
0.5960	307.38	4284.00

Sources

• Isothermal vapor-liquid equilibrium data for the ethylene + 1,1,2,3,3,3-hexafluoro-1-propene binary system between 258 and 308 K at pressures up to 4.56 MPa