Mixture of Styrene + o-Xylene

Datasets

1. Mole fraction (2)
2. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of o-Xylene (2) [ref]

Fixed		Measured
Mole fraction of o-Xylene (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of o-Xylene (2) - Gas
0.0470	5.00	0.0500
0.0480	15.00	0.0510
0.0910	5.00	0.0970
0.0920	15.00	0.0950
0.1380	15.00	0.1410
0.1410	5.00	0.1490
0.1860	15.00	0.1910
0.1920	5.00	0.2030
0.2300	15.00	0.2380
0.2460	5.00	0.2590
0.2750	15.00	0.2850
0.3070	5.00	0.3220
0.3210	15.00	0.3320
0.3640	5.00	0.3780
0.3710	15.00	0.3800
0.4120	5.00	0.4270
0.4310	15.00	0.4400
0.4730	15.00	0.4910
0.4780	5.00	0.4950
0.5020	5.00	0.5170
0.5320	15.00	0.5370
0.5520	5.00	0.5660
0.5820	15.00	0.5900
0.5980	5.00	0.6140
0.6350	15.00	0.6400
0.6490	5.00	0.6620
0.6880	15.00	0.6960
0.6970	5.00	0.7100
0.7420	5.00	0.7530
0.7440	15.00	0.7500
0.7890	5.00	0.7980
0.8030	15.00	0.8120
0.8380	5.00	0.8460
0.8640	15.00	0.8690
0.9010	5.00	0.9050
0.9260	15.00	0.9290
0.9480	5.00	0.9500
0.9700	15.00	0.9710

Mole fraction of o-Xylene (2) [ref]

Fixed		Measured
Mole fraction of o-Xylene (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of o-Xylene (2) - Gas
0.0470	5.00	0.0500
0.0480	15.00	0.0510
0.0910	5.00	0.0970
0.0920	15.00	0.0950
0.1380	15.00	0.1410
0.1410	5.00	0.1490
0.1860	15.00	0.1910
0.1920	5.00	0.2030
0.2300	15.00	0.2380
0.2460	5.00	0.2590
0.2750	15.00	0.2850
0.3070	5.00	0.3220
0.3210	15.00	0.3320
0.3640	5.00	0.3780
0.3710	15.00	0.3800
0.4120	5.00	0.4270
0.4310	15.00	0.4400
0.4730	15.00	0.4910
0.4780	5.00	0.4950
0.5020	5.00	0.5170
0.5320	15.00	0.5370
0.5520	5.00	0.5660
0.5820	15.00	0.5900
0.5980	5.00	0.6140
0.6350	15.00	0.6400
0.6490	5.00	0.6620
0.6880	15.00	0.6960
0.6970	5.00	0.7100
0.7420	5.00	0.7530
0.7440	15.00	0.7500
0.7890	5.00	0.7980
0.8030	15.00	0.8120
0.8380	5.00	0.8460
0.8640	15.00	0.8690
0.9010	5.00	0.9050
0.9260	15.00	0.9290
0.9480	5.00	0.9500
0.9700	15.00	0.9710

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of o-Xylene (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0470	5.00	331.85
0.0480	15.00	358.31
0.0910	5.00	331.80
0.0920	15.00	358.27
0.1380	15.00	358.23
0.1410	5.00	331.73
0.1860	15.00	358.18
0.1920	5.00	331.66
0.2300	15.00	358.14
0.2460	5.00	331.60
0.2750	15.00	358.09
0.3070	5.00	331.52
0.3210	15.00	358.04
0.3640	5.00	331.45
0.3710	15.00	357.99
0.4120	5.00	331.38
0.4310	15.00	357.93
0.4730	15.00	357.88
0.4780	5.00	331.31
0.5020	5.00	331.26
0.5320	15.00	357.82
0.5520	5.00	331.20
0.5820	15.00	357.75
0.5980	5.00	331.15
0.6350	15.00	357.69
0.6490	5.00	331.10
0.6880	15.00	357.62
0.6970	5.00	331.05
0.7420	5.00	330.98
0.7440	15.00	357.56
0.7890	5.00	330.94
0.8030	15.00	357.48
0.8380	5.00	330.90
0.8640	15.00	357.40
0.9010	5.00	330.83
0.9260	15.00	357.31
0.9480	5.00	330.79
0.9700	15.00	357.25

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of o-Xylene (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0470	5.00	331.85
0.0480	15.00	358.31
0.0910	5.00	331.80
0.0920	15.00	358.27
0.1380	15.00	358.23
0.1410	5.00	331.73
0.1860	15.00	358.18
0.1920	5.00	331.66
0.2300	15.00	358.14
0.2460	5.00	331.60
0.2750	15.00	358.09
0.3070	5.00	331.52
0.3210	15.00	358.04
0.3640	5.00	331.45
0.3710	15.00	357.99
0.4120	5.00	331.38
0.4310	15.00	357.93
0.4730	15.00	357.88
0.4780	5.00	331.31
0.5020	5.00	331.26
0.5320	15.00	357.82
0.5520	5.00	331.20
0.5820	15.00	357.75
0.5980	5.00	331.15
0.6350	15.00	357.69
0.6490	5.00	331.10
0.6880	15.00	357.62
0.6970	5.00	331.05
0.7420	5.00	330.98
0.7440	15.00	357.56
0.7890	5.00	330.94
0.8030	15.00	357.48
0.8380	5.00	330.90
0.8640	15.00	357.40
0.9010	5.00	330.83
0.9260	15.00	357.31
0.9480	5.00	330.79
0.9700	15.00	357.25

Sources

• Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene