Mixture of Carbon dioxide + Methane, trifluoroiodo-

Datasets

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

Mole fraction of Carbon dioxide (1) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Gas
0.0000	243.15	0.0000
0.1110	243.15	0.7510
0.1550	243.15	0.8140
0.1800	243.15	0.8380
0.2700	243.15	0.8960
0.4120	243.15	0.9300
0.5670	243.15	0.9580
1.0000	243.15	1.0000
0.0000	253.15	0.0000
0.1640	253.15	0.7900
0.1860	253.15	0.8140
0.2680	253.15	0.8580
0.4080	253.15	0.8960
0.5370	253.15	0.9300
0.6800	253.15	0.9620
1.0000	253.15	1.0000
0.0000	263.15	0.0000
0.1700	263.15	0.7610
0.2020	263.15	0.7870
0.2790	263.15	0.8450
0.3880	263.15	0.8930
0.5380	263.15	0.9310
0.6800	263.15	0.9540
1.0000	263.15	1.0000
0.0000	273.15	0.0000
0.1740	273.15	0.7340
0.2480	273.15	0.8140
0.3820	273.15	0.8720
0.4470	273.15	0.8900
0.5420	273.15	0.9200
0.6820	273.15	0.9410
1.0000	273.15	1.0000

Mole fraction of Carbon dioxide (1) [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Mole fraction of Carbon dioxide (1) - Gas
0.0000	243.15	0.0000
0.1110	243.15	0.7510
0.1550	243.15	0.8140
0.1800	243.15	0.8380
0.2700	243.15	0.8960
0.4120	243.15	0.9300
0.5670	243.15	0.9580
1.0000	243.15	1.0000
0.0000	253.15	0.0000
0.1640	253.15	0.7900
0.1860	253.15	0.8140
0.2680	253.15	0.8580
0.4080	253.15	0.8960
0.5370	253.15	0.9300
0.6800	253.15	0.9620
1.0000	253.15	1.0000
0.0000	263.15	0.0000
0.1700	263.15	0.7610
0.2020	263.15	0.7870
0.2790	263.15	0.8450
0.3880	263.15	0.8930
0.5380	263.15	0.9310
0.6800	263.15	0.9540
1.0000	263.15	1.0000
0.0000	273.15	0.0000
0.1740	273.15	0.7340
0.2480	273.15	0.8140
0.3820	273.15	0.8720
0.4470	273.15	0.8900
0.5420	273.15	0.9200
0.6820	273.15	0.9410
1.0000	273.15	1.0000

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	243.15	72.70
0.1110	243.15	286.00
0.1550	243.15	363.70
0.1800	243.15	407.00
0.2700	243.15	548.20
0.4120	243.15	732.10
0.5670	243.15	921.90
1.0000	243.15	1426.50
0.0000	253.15	110.10
0.1640	253.15	497.40
0.1860	253.15	579.40
0.2680	253.15	721.00
0.4080	253.15	961.10
0.5370	253.15	1241.30
0.6800	253.15	1455.90
1.0000	253.15	1968.40
0.0000	263.15	160.40
0.1700	263.15	644.40
0.2020	263.15	719.60
0.2790	263.15	933.20
0.3880	263.15	1223.10
0.5380	263.15	1566.80
0.6800	263.15	1914.80
1.0000	263.15	2647.50
0.0000	273.15	228.40
0.1740	273.15	819.80
0.2480	273.15	1061.70
0.3820	273.15	1520.40
0.4470	273.15	1663.30
0.5420	273.15	1980.70
0.6820	273.15	2464.10
1.0000	273.15	3483.80

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Carbon dioxide (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0000	243.15	72.70
0.1110	243.15	286.00
0.1550	243.15	363.70
0.1800	243.15	407.00
0.2700	243.15	548.20
0.4120	243.15	732.10
0.5670	243.15	921.90
1.0000	243.15	1426.50
0.0000	253.15	110.10
0.1640	253.15	497.40
0.1860	253.15	579.40
0.2680	253.15	721.00
0.4080	253.15	961.10
0.5370	253.15	1241.30
0.6800	253.15	1455.90
1.0000	253.15	1968.40
0.0000	263.15	160.40
0.1700	263.15	644.40
0.2020	263.15	719.60
0.2790	263.15	933.20
0.3880	263.15	1223.10
0.5380	263.15	1566.80
0.6800	263.15	1914.80
1.0000	263.15	2647.50
0.0000	273.15	228.40
0.1740	273.15	819.80
0.2480	273.15	1061.70
0.3820	273.15	1520.40
0.4470	273.15	1663.30
0.5420	273.15	1980.70
0.6820	273.15	2464.10
1.0000	273.15	3483.80

Sources

• Experimental research on (vapor + liquid) equilibria for the {trifluoroiodomethane (CF3I) + carbon dioxide (CO2)} system from 243.150 to 273.150 K