Mixture of Styrene + p-Xylene

Datasets

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

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

Fixed		Measured
Mole fraction of p-Xylene (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of p-Xylene (2) - Gas
0.0170	5.00	0.0240
0.0450	5.00	0.0630
0.0470	15.00	0.0630
0.0880	5.00	0.1190
0.1030	15.00	0.1340
0.1300	5.00	0.1710
0.1470	15.00	0.1880
0.1770	5.00	0.2310
0.2110	15.00	0.2600
0.2200	5.00	0.2820
0.2610	5.00	0.3280
0.2680	15.00	0.3260
0.3070	5.00	0.3820
0.3180	15.00	0.3780
0.3550	5.00	0.4310
0.3700	15.00	0.4330
0.4060	5.00	0.4840
0.4190	15.00	0.4780
0.4470	15.00	0.5130
0.4510	5.00	0.5320
0.5100	15.00	0.5750
0.5110	5.00	0.5880
0.5560	15.00	0.6210
0.5690	5.00	0.6430
0.6110	15.00	0.6720
0.6210	5.00	0.6900
0.6550	15.00	0.7120
0.6740	5.00	0.7360
0.7130	15.00	0.7630
0.7250	5.00	0.7810
0.7650	15.00	0.8080
0.7800	5.00	0.8260
0.8280	5.00	0.8660
0.8290	15.00	0.8620
0.8860	5.00	0.9130
0.8940	15.00	0.9150
0.9420	5.00	0.9570
0.9490	15.00	0.9600
0.9770	5.00	0.9830

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

Fixed		Measured
Mole fraction of p-Xylene (2) - Liquid	Pressure, kPa - Liquid	Mole fraction of p-Xylene (2) - Gas
0.0170	5.00	0.0240
0.0450	5.00	0.0630
0.0470	15.00	0.0630
0.0880	5.00	0.1190
0.1030	15.00	0.1340
0.1300	5.00	0.1710
0.1470	15.00	0.1880
0.1770	5.00	0.2310
0.2110	15.00	0.2600
0.2200	5.00	0.2820
0.2610	5.00	0.3280
0.2680	15.00	0.3260
0.3070	5.00	0.3820
0.3180	15.00	0.3780
0.3550	5.00	0.4310
0.3700	15.00	0.4330
0.4060	5.00	0.4840
0.4190	15.00	0.4780
0.4470	15.00	0.5130
0.4510	5.00	0.5320
0.5100	15.00	0.5750
0.5110	5.00	0.5880
0.5560	15.00	0.6210
0.5690	5.00	0.6430
0.6110	15.00	0.6720
0.6210	5.00	0.6900
0.6550	15.00	0.7120
0.6740	5.00	0.7360
0.7130	15.00	0.7630
0.7250	5.00	0.7810
0.7650	15.00	0.8080
0.7800	5.00	0.8260
0.8280	5.00	0.8660
0.8290	15.00	0.8620
0.8860	5.00	0.9130
0.8940	15.00	0.9150
0.9420	5.00	0.9570
0.9490	15.00	0.9600
0.9770	5.00	0.9830

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of p-Xylene (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0170	5.00	331.96
0.0450	5.00	331.68
0.0470	15.00	357.88
0.0880	5.00	331.37
0.1030	15.00	357.50
0.1300	5.00	331.13
0.1470	15.00	357.21
0.1770	5.00	330.87
0.2110	15.00	356.74
0.2200	5.00	330.58
0.2610	5.00	330.26
0.2680	15.00	356.33
0.3070	5.00	329.88
0.3180	15.00	356.00
0.3550	5.00	329.54
0.3700	15.00	355.66
0.4060	5.00	329.21
0.4190	15.00	355.38
0.4470	15.00	355.15
0.4510	5.00	328.88
0.5100	15.00	354.78
0.5110	5.00	328.55
0.5560	15.00	354.45
0.5690	5.00	328.13
0.6110	15.00	354.05
0.6210	5.00	327.89
0.6550	15.00	353.79
0.6740	5.00	327.44
0.7130	15.00	353.43
0.7250	5.00	327.10
0.7650	15.00	353.12
0.7800	5.00	326.80
0.8280	5.00	326.59
0.8290	15.00	352.70
0.8860	5.00	326.25
0.8940	15.00	352.39
0.9420	5.00	325.95
0.9490	15.00	352.04
0.9770	5.00	325.80

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of p-Xylene (2) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0170	5.00	331.96
0.0450	5.00	331.68
0.0470	15.00	357.88
0.0880	5.00	331.37
0.1030	15.00	357.50
0.1300	5.00	331.13
0.1470	15.00	357.21
0.1770	5.00	330.87
0.2110	15.00	356.74
0.2200	5.00	330.58
0.2610	5.00	330.26
0.2680	15.00	356.33
0.3070	5.00	329.88
0.3180	15.00	356.00
0.3550	5.00	329.54
0.3700	15.00	355.66
0.4060	5.00	329.21
0.4190	15.00	355.38
0.4470	15.00	355.15
0.4510	5.00	328.88
0.5100	15.00	354.78
0.5110	5.00	328.55
0.5560	15.00	354.45
0.5690	5.00	328.13
0.6110	15.00	354.05
0.6210	5.00	327.89
0.6550	15.00	353.79
0.6740	5.00	327.44
0.7130	15.00	353.43
0.7250	5.00	327.10
0.7650	15.00	353.12
0.7800	5.00	326.80
0.8280	5.00	326.59
0.8290	15.00	352.70
0.8860	5.00	326.25
0.8940	15.00	352.39
0.9420	5.00	325.95
0.9490	15.00	352.04
0.9770	5.00	325.80

Sources

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