Mixture of Toluene + Methyl Alcohol

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. n₀ - Refractive index (Na D-line) (2)
4. ρ_l - Mass density, kg/m3 (4)
5. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Temperature, K = 318.15 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid	Mole fraction of Methyl Alcohol (2) - Gas
0.0250	0.5800
0.0820	0.7280
0.1010	0.7430
0.1830	0.7710
0.2020	0.7800
0.2510	0.7900
0.3030	0.7920
0.3940	0.7950
0.4500	0.8010
0.4980	0.8070
0.5580	0.8090
0.6010	0.8100
0.6250	0.8110
0.7020	0.8220
0.7640	0.8330
0.8670	0.8670
0.9030	0.9000
0.9600	0.9350

Mole fraction of Methyl Alcohol (2) [ref]

Operational condition: Temperature, K = 318.15 (Liquid)

Mole fraction of Methyl Alcohol (2) - Liquid	Mole fraction of Methyl Alcohol (2) - Gas
0.0250	0.5800
0.0820	0.7280
0.1010	0.7430
0.1830	0.7710
0.2020	0.7800
0.2510	0.7900
0.3030	0.7920
0.3940	0.7950
0.4500	0.8010
0.4980	0.8070
0.5580	0.8090
0.6010	0.8100
0.6250	0.8110
0.7020	0.8220
0.7640	0.8330
0.8670	0.8670
0.9030	0.9000
0.9600	0.9350

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of Methyl Alcohol (2) - Liquid	Viscosity, Pa*s - Liquid
0.0499	0.0006
0.0998	0.0005
0.1993	0.0005
0.2998	0.0005
0.4007	0.0006
0.4998	0.0006
0.6002	0.0006
0.7000	0.0006
0.8000	0.0006
0.9000	0.0006
0.9501	0.0006

Viscosity, Pa*s [ref]

Operational conditions:

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

Mole fraction of Methyl Alcohol (2) - Liquid	Viscosity, Pa*s - Liquid
0.0499	0.0006
0.0998	0.0005
0.1993	0.0005
0.2998	0.0005
0.4007	0.0006
0.4998	0.0006
0.6002	0.0006
0.7000	0.0006
0.8000	0.0006
0.9000	0.0006
0.9501	0.0006

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.32 (Liquid)

Mole fraction of Toluene (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0491	1.3464
0.1058	1.366
0.1990	1.3921
0.3361	1.4215
0.4097	1.4337
0.4501	1.4402
0.5024	1.4478
0.5393	1.4527
0.5818	1.4579
0.6961	1.47
0.7764	1.4778
0.8695	1.485
0.9416	1.4904

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.32 (Liquid)

Mole fraction of Toluene (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0491	1.3464
0.1058	1.366
0.1990	1.3921
0.3361	1.4215
0.4097	1.4337
0.4501	1.4402
0.5024	1.4478
0.5393	1.4527
0.5818	1.4579
0.6961	1.47
0.7764	1.4778
0.8695	1.485
0.9416	1.4904

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.32 (Liquid)

Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0491	797.2
0.1058	806.2
0.1990	818.1
0.3361	831.1
0.4097	836.6
0.4501	839.2
0.5024	842.4
0.5393	844.4
0.5818	846.6
0.6961	851.7
0.7764	854.8
0.8695	858.0
0.9416	860.2

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
0.0499	860.7
0.0998	859.1
0.1993	855.9
0.2998	852.1
0.4007	847.5
0.4998	842.1
0.6002	835.6
0.7000	827.7
0.8000	817.7
0.9000	804.4
0.9501	796.3

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 101.32 (Liquid)

Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0491	797.2
0.1058	806.2
0.1990	818.1
0.3361	831.1
0.4097	836.6
0.4501	839.2
0.5024	842.4
0.5393	844.4
0.5818	846.6
0.6961	851.7
0.7764	854.8
0.8695	858.0
0.9416	860.2

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
0.0499	860.7
0.0998	859.1
0.1993	855.9
0.2998	852.1
0.4007	847.5
0.4998	842.1
0.6002	835.6
0.7000	827.7
0.8000	817.7
0.9000	804.4
0.9501	796.3

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Methyl Alcohol (2) - Gas	Mole fraction of Methyl Alcohol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.7860	0.2000	313.15
0.7910	0.3000	313.15
0.8110	0.4500	313.15
0.8200	0.6000	313.15
0.8280	0.7000	313.15
0.8960	0.9000	313.15
0.7760	0.2000	318.15
0.7920	0.3000	318.15
0.8020	0.4500	318.15
0.8100	0.6000	318.15
0.8230	0.7000	318.15
0.9350	0.9000	318.15

Boiling temperature at pressure P, K [ref]

Fixed		Measured
Mole fraction of Methyl Alcohol (2) - Gas	Mole fraction of Methyl Alcohol (2) - Liquid	Boiling temperature at pressure P, K - Liquid
0.7860	0.2000	313.15
0.7910	0.3000	313.15
0.8110	0.4500	313.15
0.8200	0.6000	313.15
0.8280	0.7000	313.15
0.8960	0.9000	313.15
0.7760	0.2000	318.15
0.7920	0.3000	318.15
0.8020	0.4500	318.15
0.8100	0.6000	318.15
0.8230	0.7000	318.15
0.9350	0.9000	318.15

Sources

• Experimental and predicted volumetric and refractive index properties of ternary mixtures of iodoethane with toluene and alcohols at temperature 298.15 K and pressure 101 kPa
• Isothermal Vapor Liquid Equilibrium Data for the Toluene + Methanol + N-Butylpyridinium Bromide System
• Densities and Viscosities for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Benzene and Methyl tert-Butyl Ether + Methanol + Toluene and Their Sub-binary Systems at 298.15 K
• Isothermal Vapor-Liquid Equilibrium Data for the System Methanol + Toluene + Triphenylbenzylphosphonium Chloride