Mixture of o-Xylene + Thiophene, tetrahydro-, 1,1-dioxide

Datasets

1. Activity coefficient (2)
2. η - Viscosity, Pa*s (2)
3. P_vap - Vapor or sublimation pressure, kPa (4)
4. ρ_g - Mass density, kg/m3 (4)
5. ρ_l - Mass density, kg/m3 (6)

Activity coefficient of o-Xylene (1) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of o-Xylene (1) - Liquid
333.15	4.568
343.15	4.388
353.15	4.281
363.15	4.174
373.15	4.035

Activity coefficient of o-Xylene (1) [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Mole fraction = 0 (Liquid)

Temperature, K - Liquid	Activity coefficient of o-Xylene (1) - Liquid
333.15	4.568
343.15	4.388
353.15	4.281
363.15	4.174
373.15	4.035

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0101
303.15	0.1118	0.0069
303.15	0.2206	0.0049
303.15	0.3267	0.0036
303.15	0.4301	0.0027
303.15	0.5311	0.0021
303.15	0.6293	0.0016
303.15	0.7254	0.0012
303.15	0.8191	0.0010
303.15	0.9105	0.0008
303.15	1.0000	0.0007
323.15	0.0000	0.0062
323.15	0.1118	0.0044
323.15	0.2206	0.0032
323.15	0.3267	0.0024
323.15	0.4301	0.0019
323.15	0.5311	0.0015
323.15	0.6293	0.0012
323.15	0.7254	0.0009
323.15	0.8191	0.0008
323.15	0.9105	0.0007
323.15	1.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Viscosity, Pa*s - Liquid
303.15	0.0000	0.0101
303.15	0.1118	0.0069
303.15	0.2206	0.0049
303.15	0.3267	0.0036
303.15	0.4301	0.0027
303.15	0.5311	0.0021
303.15	0.6293	0.0016
303.15	0.7254	0.0012
303.15	0.8191	0.0010
303.15	0.9105	0.0008
303.15	1.0000	0.0007
323.15	0.0000	0.0062
323.15	0.1118	0.0044
323.15	0.2206	0.0032
323.15	0.3267	0.0024
323.15	0.4301	0.0019
323.15	0.5311	0.0015
323.15	0.6293	0.0012
323.15	0.7254	0.0009
323.15	0.8191	0.0008
323.15	0.9105	0.0007
323.15	1.0000	0.0006

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
333.15	0.0000	0.01
333.15	0.0100	0.25
333.15	0.0150	0.38
333.15	0.0200	0.49
333.15	0.0300	0.72
333.15	0.1000	2.02
333.15	0.2000	3.56
333.15	0.3000	4.40
333.15	0.4000	4.97
333.15	0.4990	5.22
333.15	0.5990	5.26
333.15	0.6990	5.28
333.15	0.8010	5.34
333.15	0.8990	5.35
333.15	1.0000	5.44
353.15	0.0000	0.04
353.15	0.0100	0.05
353.15	0.0150	0.18
353.15	0.0200	0.49
353.15	0.0300	1.08
353.15	0.1000	3.34
353.15	0.2000	6.06
353.15	0.3000	8.21
353.15	0.4000	9.57
353.15	0.4990	10.82
353.15	0.5990	11.41
353.15	0.6990	11.68
353.15	0.8010	11.78
353.15	0.8990	11.95
353.15	1.0000	12.66

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
333.15	0.0000	0.01
333.15	0.0100	0.25
333.15	0.0150	0.38
333.15	0.0200	0.49
333.15	0.0300	0.72
333.15	0.1000	2.02
333.15	0.2000	3.56
333.15	0.3000	4.40
333.15	0.4000	4.97
333.15	0.4990	5.22
333.15	0.5990	5.26
333.15	0.6990	5.28
333.15	0.8010	5.34
333.15	0.8990	5.35
333.15	1.0000	5.44
353.15	0.0000	0.04
353.15	0.0100	0.05
353.15	0.0150	0.18
353.15	0.0200	0.49
353.15	0.0300	1.08
353.15	0.1000	3.34
353.15	0.2000	6.06
353.15	0.3000	8.21
353.15	0.4000	9.57
353.15	0.4990	10.82
353.15	0.5990	11.41
353.15	0.6990	11.68
353.15	0.8010	11.78
353.15	0.8990	11.95
353.15	1.0000	12.66

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
333.15	0.0000	0.01
333.15	0.0100	0.25
333.15	0.0150	0.38
333.15	0.0200	0.49
333.15	0.0300	0.72
333.15	0.1000	2.02
333.15	0.2000	3.56
333.15	0.3000	4.40
333.15	0.4000	4.97
333.15	0.4990	5.22
333.15	0.5990	5.26
333.15	0.6990	5.28
333.15	0.8010	5.34
333.15	0.8990	5.35
333.15	1.0000	5.44
353.15	0.0000	0.04
353.15	0.0100	0.05
353.15	0.0150	0.18
353.15	0.0200	0.49
353.15	0.0300	1.08
353.15	0.1000	3.34
353.15	0.2000	6.06
353.15	0.3000	8.21
353.15	0.4000	9.57
353.15	0.4990	10.82
353.15	0.5990	11.41
353.15	0.6990	11.68
353.15	0.8010	11.78
353.15	0.8990	11.95
353.15	1.0000	12.66

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Vapor or sublimation pressure, kPa - Liquid
333.15	0.0000	0.01
333.15	0.0100	0.25
333.15	0.0150	0.38
333.15	0.0200	0.49
333.15	0.0300	0.72
333.15	0.1000	2.02
333.15	0.2000	3.56
333.15	0.3000	4.40
333.15	0.4000	4.97
333.15	0.4990	5.22
333.15	0.5990	5.26
333.15	0.6990	5.28
333.15	0.8010	5.34
333.15	0.8990	5.35
333.15	1.0000	5.44
353.15	0.0000	0.04
353.15	0.0100	0.05
353.15	0.0150	0.18
353.15	0.0200	0.49
353.15	0.0300	1.08
353.15	0.1000	3.34
353.15	0.2000	6.06
353.15	0.3000	8.21
353.15	0.4000	9.57
353.15	0.4990	10.82
353.15	0.5990	11.41
353.15	0.6990	11.68
353.15	0.8010	11.78
353.15	0.8990	11.95
353.15	1.0000	12.66

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of o-Xylene (1) - Liquid	Mass density, kg/m3 - Gas
333.15	0.0000	0.0005
333.15	0.0100	0.0098
333.15	0.0150	0.0147
333.15	0.0200	0.0188
333.15	0.0300	0.0276
333.15	0.1000	0.0776
333.15	0.2000	0.1364
333.15	0.3000	0.1687
333.15	0.4000	0.1904
333.15	0.4990	0.2001
333.15	0.5990	0.2016
333.15	0.6990	0.2021
333.15	0.8010	0.1971
333.15	0.8990	0.1972
333.15	1.0000	0.2082
353.15	0.0000	0.0018
353.15	0.0100	0.0020
353.15	0.0150	0.0067
353.15	0.0200	0.0178
353.15	0.0300	0.0394
353.15	0.1000	0.1211
353.15	0.2000	0.2193
353.15	0.3000	0.2966
353.15	0.4000	0.3460
353.15	0.4990	0.3909
353.15	0.5990	0.4123
353.15	0.6990	0.4219
353.15	0.8010	0.4255
353.15	0.8990	0.4317
353.15	1.0000	0.4571

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of o-Xylene (1) - Gas	Mass density, kg/m3 - Gas
333.15	0.0000	0.0005
333.15	0.0100	0.0098
333.15	0.0150	0.0147
333.15	0.0200	0.0188
333.15	0.0300	0.0276
333.15	0.1000	0.0776
333.15	0.2000	0.1364
333.15	0.3000	0.1687
333.15	0.4000	0.1904
333.15	0.4990	0.2001
333.15	0.5990	0.2016
333.15	0.6990	0.2021
333.15	0.8010	0.1971
333.15	0.8990	0.1972
333.15	1.0000	0.2082
353.15	0.0000	0.0018
353.15	0.0100	0.0020
353.15	0.0150	0.0067
353.15	0.0200	0.0178
353.15	0.0300	0.0394
353.15	0.1000	0.1211
353.15	0.2000	0.2193
353.15	0.3000	0.2966
353.15	0.4000	0.3460
353.15	0.4990	0.3909
353.15	0.5990	0.4123
353.15	0.6990	0.4219
353.15	0.8010	0.4255
353.15	0.8990	0.4317
353.15	1.0000	0.4571

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of o-Xylene (1) - Liquid	Mass density, kg/m3 - Gas
333.15	0.0000	0.0005
333.15	0.0100	0.0098
333.15	0.0150	0.0147
333.15	0.0200	0.0188
333.15	0.0300	0.0276
333.15	0.1000	0.0776
333.15	0.2000	0.1364
333.15	0.3000	0.1687
333.15	0.4000	0.1904
333.15	0.4990	0.2001
333.15	0.5990	0.2016
333.15	0.6990	0.2021
333.15	0.8010	0.1971
333.15	0.8990	0.1972
333.15	1.0000	0.2082
353.15	0.0000	0.0018
353.15	0.0100	0.0020
353.15	0.0150	0.0067
353.15	0.0200	0.0178
353.15	0.0300	0.0394
353.15	0.1000	0.1211
353.15	0.2000	0.2193
353.15	0.3000	0.2966
353.15	0.4000	0.3460
353.15	0.4990	0.3909
353.15	0.5990	0.4123
353.15	0.6990	0.4219
353.15	0.8010	0.4255
353.15	0.8990	0.4317
353.15	1.0000	0.4571

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Gas	Mole fraction of o-Xylene (1) - Gas	Mass density, kg/m3 - Gas
333.15	0.0000	0.0005
333.15	0.0100	0.0098
333.15	0.0150	0.0147
333.15	0.0200	0.0188
333.15	0.0300	0.0276
333.15	0.1000	0.0776
333.15	0.2000	0.1364
333.15	0.3000	0.1687
333.15	0.4000	0.1904
333.15	0.4990	0.2001
333.15	0.5990	0.2016
333.15	0.6990	0.2021
333.15	0.8010	0.1971
333.15	0.8990	0.1972
333.15	1.0000	0.2082
353.15	0.0000	0.0018
353.15	0.0100	0.0020
353.15	0.0150	0.0067
353.15	0.0200	0.0178
353.15	0.0300	0.0394
353.15	0.1000	0.1211
353.15	0.2000	0.2193
353.15	0.3000	0.2966
353.15	0.4000	0.3460
353.15	0.4990	0.3909
353.15	0.5990	0.4123
353.15	0.6990	0.4219
353.15	0.8010	0.4255
353.15	0.8990	0.4317
353.15	1.0000	0.4571

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Mass density, kg/m3 - Liquid
333.15	0.0000	1231.12
333.15	0.0100	1227.27
333.15	0.0150	1225.35
333.15	0.0200	1223.42
333.15	0.0300	1219.57
333.15	0.1000	1192.25
333.15	0.2000	1153.84
333.15	0.3000	1115.37
333.15	0.4000	1076.99
333.15	0.4990	1038.59
333.15	0.5990	1000.24
333.15	0.6990	961.436
333.15	0.8010	922.401
333.15	0.8990	884.731
333.15	1.0000	845.839
353.15	0.0000	1214.39
353.15	0.0100	1210.53
353.15	0.0150	1208.6
353.15	0.0200	1206.67
353.15	0.0300	1202.81
353.15	0.1000	1175.45
353.15	0.2000	1136.98
353.15	0.3000	1098.46
353.15	0.4000	1060.02
353.15	0.4990	1021.56
353.15	0.5990	983.157
353.15	0.6990	944.296
353.15	0.8010	905.202
353.15	0.8990	867.477
353.15	1.0000	828.528

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	1260.8
303.15	0.1118	1210.86
303.15	0.2206	1163.38
303.15	0.3267	1118.72
303.15	0.4301	1076.59
303.15	0.5311	1037.09
303.15	0.6293	1000.09
303.15	0.7254	964.88
303.15	0.8191	931.97
303.15	0.9105	900.64
303.15	1.0000	870.66
323.15	0.0000	1243.36
323.15	0.1118	1193.29
323.15	0.2206	1145.77
323.15	0.3267	1101.18
323.15	0.4301	1059.09
323.15	0.5311	1019.64
323.15	0.6293	982.76
323.15	0.7254	947.64
323.15	0.8191	914.83
323.15	0.9105	883.61
323.15	1.0000	853.79

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Mass density, kg/m3 - Liquid
333.15	0.0000	1231.12
333.15	0.0100	1227.27
333.15	0.0150	1225.35
333.15	0.0200	1223.42
333.15	0.0300	1219.57
333.15	0.1000	1192.25
333.15	0.2000	1153.84
333.15	0.3000	1115.37
333.15	0.4000	1076.99
333.15	0.4990	1038.59
333.15	0.5990	1000.24
333.15	0.6990	961.436
333.15	0.8010	922.401
333.15	0.8990	884.731
333.15	1.0000	845.839
353.15	0.0000	1214.39
353.15	0.0100	1210.53
353.15	0.0150	1208.6
353.15	0.0200	1206.67
353.15	0.0300	1202.81
353.15	0.1000	1175.45
353.15	0.2000	1136.98
353.15	0.3000	1098.46
353.15	0.4000	1060.02
353.15	0.4990	1021.56
353.15	0.5990	983.157
353.15	0.6990	944.296
353.15	0.8010	905.202
353.15	0.8990	867.477
353.15	1.0000	828.528

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Mass density, kg/m3 - Liquid
333.15	0.0000	1231.12
333.15	0.0100	1227.27
333.15	0.0150	1225.35
333.15	0.0200	1223.42
333.15	0.0300	1219.57
333.15	0.1000	1192.25
333.15	0.2000	1153.84
333.15	0.3000	1115.37
333.15	0.4000	1076.99
333.15	0.4990	1038.59
333.15	0.5990	1000.24
333.15	0.6990	961.436
333.15	0.8010	922.401
333.15	0.8990	884.731
333.15	1.0000	845.839
353.15	0.0000	1214.39
353.15	0.0100	1210.53
353.15	0.0150	1208.6
353.15	0.0200	1206.67
353.15	0.0300	1202.81
353.15	0.1000	1175.45
353.15	0.2000	1136.98
353.15	0.3000	1098.46
353.15	0.4000	1060.02
353.15	0.4990	1021.56
353.15	0.5990	983.157
353.15	0.6990	944.296
353.15	0.8010	905.202
353.15	0.8990	867.477
353.15	1.0000	828.528

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Mass density, kg/m3 - Liquid
303.15	0.0000	1260.8
303.15	0.1118	1210.86
303.15	0.2206	1163.38
303.15	0.3267	1118.72
303.15	0.4301	1076.59
303.15	0.5311	1037.09
303.15	0.6293	1000.09
303.15	0.7254	964.88
303.15	0.8191	931.97
303.15	0.9105	900.64
303.15	1.0000	870.66
323.15	0.0000	1243.36
323.15	0.1118	1193.29
323.15	0.2206	1145.77
323.15	0.3267	1101.18
323.15	0.4301	1059.09
323.15	0.5311	1019.64
323.15	0.6293	982.76
323.15	0.7254	947.64
323.15	0.8191	914.83
323.15	0.9105	883.61
323.15	1.0000	853.79

Mass density, kg/m3 [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of o-Xylene (1) - Liquid	Mass density, kg/m3 - Liquid
333.15	0.0000	1231.12
333.15	0.0100	1227.27
333.15	0.0150	1225.35
333.15	0.0200	1223.42
333.15	0.0300	1219.57
333.15	0.1000	1192.25
333.15	0.2000	1153.84
333.15	0.3000	1115.37
333.15	0.4000	1076.99
333.15	0.4990	1038.59
333.15	0.5990	1000.24
333.15	0.6990	961.436
333.15	0.8010	922.401
333.15	0.8990	884.731
333.15	1.0000	845.839
353.15	0.0000	1214.39
353.15	0.0100	1210.53
353.15	0.0150	1208.6
353.15	0.0200	1206.67
353.15	0.0300	1202.81
353.15	0.1000	1175.45
353.15	0.2000	1136.98
353.15	0.3000	1098.46
353.15	0.4000	1060.02
353.15	0.4990	1021.56
353.15	0.5990	983.157
353.15	0.6990	944.296
353.15	0.8010	905.202
353.15	0.8990	867.477
353.15	1.0000	828.528

Sources

• Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
• Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
• Vapor-Liquid Equilibria and Density Measurement for Binary Mixtures of Benzene + Nonane, Methylbenzene + 1,2-Dimethylbenzene, 1,3-Dimethylbenzene + 2,3,4,5-Tetrahydrothiophene-1,1-dioxide (Sulfolane), 1,2-Dimethylbenzene + Sulfolane, 1,2-Dimethylbenzene + N-Methylformamide (NMF), 1,3-Dimethylbenzene + NMF, and 1,4-Dimethylbenzene + NMF from (333.15 to 353.15) K at Vacuum Conditions
• Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography