Mixture of Toluene + Ethane, 1,2-dibromo-

Datasets

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

Mole fraction of Toluene (1) [ref]

Fixed		Measured
Mole fraction of Toluene (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Toluene (1) - Gas
0.0000	102.11	0.0000
0.0246	102.12	0.0484
0.0790	102.15	0.1443
0.1027	102.15	0.1828
0.1592	102.14	0.2657
0.1852	102.11	0.3011
0.2371	102.12	0.3668
0.2863	102.05	0.4245
0.3241	102.13	0.4659
0.3574	102.13	0.5007
0.4252	102.12	0.5686
0.4914	102.13	0.6298
0.5382	102.12	0.6702
0.6122	102.11	0.7307
0.6793	102.11	0.7825
0.7527	102.12	0.8361
0.8281	102.12	0.8891
0.8740	102.11	0.9201
0.9543	102.10	0.9719
1.0000	102.09	1.0000

Mole fraction of Toluene (1) [ref]

Fixed		Measured
Mole fraction of Toluene (1) - Liquid	Pressure, kPa - Liquid	Mole fraction of Toluene (1) - Gas
0.0000	102.11	0.0000
0.0246	102.12	0.0484
0.0790	102.15	0.1443
0.1027	102.15	0.1828
0.1592	102.14	0.2657
0.1852	102.11	0.3011
0.2371	102.12	0.3668
0.2863	102.05	0.4245
0.3241	102.13	0.4659
0.3574	102.13	0.5007
0.4252	102.12	0.5686
0.4914	102.13	0.6298
0.5382	102.12	0.6702
0.6122	102.11	0.7307
0.6793	102.11	0.7825
0.7527	102.12	0.8361
0.8281	102.12	0.8891
0.8740	102.11	0.9201
0.9543	102.10	0.9719
1.0000	102.09	1.0000

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Toluene (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	102.11	405.50
0.0246	102.12	404.70
0.0790	102.15	403.00
0.1027	102.15	402.30
0.1592	102.14	400.50
0.1852	102.11	399.90
0.2371	102.12	398.50
0.2863	102.05	397.20
0.3241	102.13	396.60
0.3574	102.13	395.90
0.4252	102.12	394.50
0.4914	102.13	393.20
0.5382	102.12	392.30
0.6122	102.11	391.10
0.6793	102.11	389.80
0.7527	102.12	388.70
0.8281	102.12	387.50
0.8740	102.11	386.80
0.9543	102.10	385.50
1.0000	102.09	384.90

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Toluene (1) - Liquid	Pressure, kPa - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	102.11	405.50
0.0246	102.12	404.70
0.0790	102.15	403.00
0.1027	102.15	402.30
0.1592	102.14	400.50
0.1852	102.11	399.90
0.2371	102.12	398.50
0.2863	102.05	397.20
0.3241	102.13	396.60
0.3574	102.13	395.90
0.4252	102.12	394.50
0.4914	102.13	393.20
0.5382	102.12	392.30
0.6122	102.11	391.10
0.6793	102.11	389.80
0.7527	102.12	388.70
0.8281	102.12	387.50
0.8740	102.11	386.80
0.9543	102.10	385.50
1.0000	102.09	384.90

Sources

• Isobaric Vapor-Liquid Equilibria for Binary Mixtures of 1,2-Dibromoethane with Benzene, Toluene, Fluorobenzene, and Bromobenzene at Atmospheric Pressure