Mixture of Methane + Butane, decafluoro-

Datasets

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

Mole fraction of Methane (1) [ref]

Fixed		Measured
Mole fraction of Methane (1) - Liquid	Temperature, K - Liquid	Mole fraction of Methane (1) - Gas
0.0120	293.05	0.4230
0.0850	293.05	0.8030
0.1810	293.05	0.8670
0.3070	293.05	0.8750
0.3930	293.05	0.8580
0.2340	293.05	0.8750
0.1230	293.05	0.8470
0.4340	293.05	0.8460
0.5520	293.05	0.8040
0.6060	293.05	0.7730
0.4830	293.05	0.8340
0.0290	313.09	0.4670
0.0610	313.09	0.6260
0.0920	313.09	0.6990
0.1490	313.09	0.7540
0.1910	313.09	0.7670
0.2260	313.09	0.7740
0.2680	313.09	0.7750
0.3180	313.09	0.7680
0.3790	313.09	0.7490
0.4670	313.09	0.7060
0.5190	313.09	0.6650
0.3550	332.97	0.6190
0.0290	332.97	0.3360
0.0640	332.97	0.4990
0.0940	332.97	0.5630
0.1330	332.97	0.6180
0.1690	332.97	0.6350
0.2030	332.97	0.6460
0.2390	332.97	0.6480
0.2790	332.97	0.6450
0.3160	332.97	0.6340
0.4350	332.97	0.5470
0.3800	332.97	0.5970

Mole fraction of Methane (1) [ref]

Fixed		Measured
Mole fraction of Methane (1) - Liquid	Temperature, K - Liquid	Mole fraction of Methane (1) - Gas
0.0120	293.05	0.4230
0.0850	293.05	0.8030
0.1810	293.05	0.8670
0.3070	293.05	0.8750
0.3930	293.05	0.8580
0.2340	293.05	0.8750
0.1230	293.05	0.8470
0.4340	293.05	0.8460
0.5520	293.05	0.8040
0.6060	293.05	0.7730
0.4830	293.05	0.8340
0.0290	313.09	0.4670
0.0610	313.09	0.6260
0.0920	313.09	0.6990
0.1490	313.09	0.7540
0.1910	313.09	0.7670
0.2260	313.09	0.7740
0.2680	313.09	0.7750
0.3180	313.09	0.7680
0.3790	313.09	0.7490
0.4670	313.09	0.7060
0.5190	313.09	0.6650
0.3550	332.97	0.6190
0.0290	332.97	0.3360
0.0640	332.97	0.4990
0.0940	332.97	0.5630
0.1330	332.97	0.6180
0.1690	332.97	0.6350
0.2030	332.97	0.6460
0.2390	332.97	0.6480
0.2790	332.97	0.6450
0.3160	332.97	0.6340
0.4350	332.97	0.5470
0.3800	332.97	0.5970

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Methane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0120	293.05	473.00
0.0850	293.05	2015.00
0.1810	293.05	3988.00
0.3070	293.05	6587.00
0.3930	293.05	8058.00
0.2340	293.05	5188.00
0.1230	293.05	2914.00
0.4340	293.05	8901.00
0.5520	293.05	10276.00
0.6060	293.05	10655.00
0.4830	293.05	9562.00
0.0290	313.09	1052.00
0.0610	313.09	1853.00
0.0920	313.09	2687.00
0.1490	313.09	3924.00
0.1910	313.09	4788.00
0.2260	313.09	5603.00
0.2680	313.09	6459.00
0.3180	313.09	7447.00
0.3790	313.09	8432.00
0.4670	313.09	9446.00
0.5190	313.09	9837.00
0.3550	332.97	7753.00
0.0290	332.97	1321.00
0.0640	332.97	2168.00
0.0940	332.97	2839.00
0.1330	332.97	3704.00
0.1690	332.97	4541.00
0.2030	332.97	5301.00
0.2390	332.97	6017.00
0.2790	332.97	6743.00
0.3160	332.97	7368.00
0.4350	332.97	8466.00
0.3800	332.97	8138.00

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Mole fraction of Methane (1) - Liquid	Temperature, K - Liquid	Vapor or sublimation pressure, kPa - Liquid
0.0120	293.05	473.00
0.0850	293.05	2015.00
0.1810	293.05	3988.00
0.3070	293.05	6587.00
0.3930	293.05	8058.00
0.2340	293.05	5188.00
0.1230	293.05	2914.00
0.4340	293.05	8901.00
0.5520	293.05	10276.00
0.6060	293.05	10655.00
0.4830	293.05	9562.00
0.0290	313.09	1052.00
0.0610	313.09	1853.00
0.0920	313.09	2687.00
0.1490	313.09	3924.00
0.1910	313.09	4788.00
0.2260	313.09	5603.00
0.2680	313.09	6459.00
0.3180	313.09	7447.00
0.3790	313.09	8432.00
0.4670	313.09	9446.00
0.5190	313.09	9837.00
0.3550	332.97	7753.00
0.0290	332.97	1321.00
0.0640	332.97	2168.00
0.0940	332.97	2839.00
0.1330	332.97	3704.00
0.1690	332.97	4541.00
0.2030	332.97	5301.00
0.2390	332.97	6017.00
0.2790	332.97	6743.00
0.3160	332.97	7368.00
0.4350	332.97	8466.00
0.3800	332.97	8138.00

Sources

• Isothermal Vapor Liquid Equilibrium Data and Thermodynamic Modeling for Binary Systems of Perfluorobutane (R610) + (Methane or Hydrogen Sulfide) at (293, 313, and 333) K