Mixture of n-Hexane + o-Xylene

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (2)
3. ρ_l - Mass density, kg/m3 (4)
4. T_boil - Boiling temperature at pressure P, K (2)

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

Operational conditions:

• Temperature, K = 298.15 (Liquid mixture 2)
• Pressure, kPa = 101.3 (Liquid mixture 2)

Mole fraction of o-Xylene (2) - Liquid mixture 1
0.0700
0.1370
0.2010
0.2600
0.2610
0.3950
0.5320
0.6660
0.8010
0.9220

Mole fraction of n-Hexane (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mole fraction of n-Hexane (1) - Gas
1.0000	1.0000
0.9360	0.9900
0.8190	0.9730
0.7250	0.9560
0.6250	0.9350
0.5150	0.9100
0.4290	0.8750
0.3430	0.8360
0.2310	0.7370
0.1870	0.6670
0.1220	0.5340
0.0740	0.3930
0.0180	0.1130
0.0000	0.0000

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

Operational conditions:

• Temperature, K = 298.15 (Liquid mixture 2)
• Pressure, kPa = 101.3 (Liquid mixture 2)

Mole fraction of o-Xylene (2) - Liquid mixture 1
0.0700
0.1370
0.2010
0.2600
0.2610
0.3950
0.5320
0.6660
0.8010
0.9220

Mole fraction of n-Hexane (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mole fraction of n-Hexane (1) - Gas
1.0000	1.0000
0.9360	0.9900
0.8190	0.9730
0.7250	0.9560
0.6250	0.9350
0.5150	0.9100
0.4290	0.8750
0.3430	0.8360
0.2310	0.7370
0.1870	0.6670
0.1220	0.5340
0.0740	0.3930
0.0180	0.1130
0.0000	0.0000

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Viscosity, Pa*s - Liquid
0.0520	0.0007
0.1413	0.0006
0.2482	0.0005
0.2901	0.0005
0.3550	0.0005
0.4004	0.0004
0.4815	0.0004
0.5100	0.0004
0.5856	0.0004
0.6351	0.0004
0.6753	0.0004
0.7858	0.0003
0.8317	0.0003
0.9014	0.0003

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Viscosity, Pa*s - Liquid
0.0520	0.0007
0.1413	0.0006
0.2482	0.0005
0.2901	0.0005
0.3550	0.0005
0.4004	0.0004
0.4815	0.0004
0.5100	0.0004
0.5856	0.0004
0.6351	0.0004
0.6753	0.0004
0.7858	0.0003
0.8317	0.0003
0.9014	0.0003

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
0.0520	863.09
0.1413	842.86
0.2482	818.74
0.2901	809.33
0.3550	794.79
0.4004	784.66
0.4815	766.65
0.5100	760.35
0.5856	743.71
0.6351	732.88
0.6753	724.12
0.7858	700.23
0.8317	690.38
0.9014	675.52

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	875.37
0.0450	865.52
0.0970	853.5
0.1890	832.71
0.2950	809.05
0.3970	786.32
0.4950	764.54
0.5970	742.07
0.6970	720.32
0.7970	698.71
0.9010	676.45
0.9500	665.83
1.0000	655.19

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
0.0520	863.09
0.1413	842.86
0.2482	818.74
0.2901	809.33
0.3550	794.79
0.4004	784.66
0.4815	766.65
0.5100	760.35
0.5856	743.71
0.6351	732.88
0.6753	724.12
0.7858	700.23
0.8317	690.38
0.9014	675.52

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 101 (Liquid)
• Temperature, K = 298.15 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Mass density, kg/m3 - Liquid
0.0000	875.37
0.0450	865.52
0.0970	853.5
0.1890	832.71
0.2950	809.05
0.3970	786.32
0.4950	764.54
0.5970	742.07
0.6970	720.32
0.7970	698.71
0.9010	676.45
0.9500	665.83
1.0000	655.19

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	341.50
0.9360	344.40
0.8190	347.80
0.7250	351.40
0.6250	355.70
0.5150	359.60
0.4290	364.60
0.3430	369.50
0.2310	379.90
0.1870	385.50
0.1220	394.00
0.0740	402.60
0.0180	414.60
0.0000	417.30

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of n-Hexane (1) - Liquid	Boiling temperature at pressure P, K - Liquid
1.0000	341.50
0.9360	344.40
0.8190	347.80
0.7250	351.40
0.6250	355.70
0.5150	359.60
0.4290	364.60
0.3430	369.50
0.2310	379.90
0.1870	385.50
0.1220	394.00
0.0740	402.60
0.0180	414.60
0.0000	417.30

Sources

• Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
• Application of [EMpy][ESO4] ionic liquid as solvent for the liquid extraction of xylenes from hexane
• Study of [EMim][ESO4] ionic liquid as solvent in the liquid-liquid extraction of xylenes from their mixtures with hexane
• Isobaric Vapor Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa