Mixture of Toluene + Ethanol, 2-methoxy-

Datasets

1. Activity coefficient (2)
2. Mole fraction (2)
3. η - Viscosity, Pa*s (2)
4. n₀ - Refractive index (Na D-line) (2)
5. ρ_l - Mass density, kg/m3 (4)
6. c_sound,fluid - Speed of Sound, m/s (2)
7. T_boil - Boiling temperature at pressure P, K (2)
8. Azeotropic temperature, K (4)

Activity coefficient of Toluene (1) [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Toluene (1) - Liquid	Activity coefficient of Toluene (1) - Liquid
298.00	238.00	0.0000	3.6

Activity coefficient of Toluene (1) [ref]

Fixed			Measured
Temperature, K - Liquid	Pressure, kPa - Liquid	Mole fraction of Toluene (1) - Liquid	Activity coefficient of Toluene (1) - Liquid
298.00	238.00	0.0000	3.6

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Toluene (1) - Liquid	Mole fraction of Toluene (1) - Gas
0.9710	0.9450
0.9294	0.8807
0.8586	0.7949
0.8044	0.7502
0.7616	0.7311
0.7131	0.7080
0.6490	0.6836
0.5903	0.6601
0.5110	0.6200
0.3404	0.5557
0.2246	0.4755
0.1383	0.3745
0.0998	0.3085
0.0595	0.2130
0.0261	0.1045

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Toluene (1) - Liquid	Mole fraction of Toluene (1) - Gas
0.9710	0.9450
0.9294	0.8807
0.8586	0.7949
0.8044	0.7502
0.7616	0.7311
0.7131	0.7080
0.6490	0.6836
0.5903	0.6601
0.5110	0.6200
0.3404	0.5557
0.2246	0.4755
0.1383	0.3745
0.0998	0.3085
0.0595	0.2130
0.0261	0.1045

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-methoxy- (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0586	0.0006
298.15	0.1696	0.0006
298.15	0.2421	0.0007
298.15	0.3513	0.0007
298.15	0.4555	0.0008
298.15	0.4987	0.0008
298.15	0.5515	0.0009
298.15	0.6515	0.0010
298.15	0.7487	0.0011
298.15	0.8495	0.0013
298.15	0.9558	0.0015
308.15	0.0586	0.0005
308.15	0.1696	0.0005
308.15	0.2421	0.0006
308.15	0.3513	0.0006
308.15	0.4555	0.0007
308.15	0.4987	0.0007
308.15	0.5515	0.0007
308.15	0.6515	0.0008
308.15	0.7487	0.0009
308.15	0.8495	0.0010
308.15	0.9558	0.0012

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-methoxy- (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0586	0.0006
298.15	0.1696	0.0006
298.15	0.2421	0.0007
298.15	0.3513	0.0007
298.15	0.4555	0.0008
298.15	0.4987	0.0008
298.15	0.5515	0.0009
298.15	0.6515	0.0010
298.15	0.7487	0.0011
298.15	0.8495	0.0013
298.15	0.9558	0.0015
308.15	0.0586	0.0005
308.15	0.1696	0.0005
308.15	0.2421	0.0006
308.15	0.3513	0.0006
308.15	0.4555	0.0007
308.15	0.4987	0.0007
308.15	0.5515	0.0007
308.15	0.6515	0.0008
308.15	0.7487	0.0009
308.15	0.8495	0.0010
308.15	0.9558	0.0012

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0500	1.4048
0.0998	1.4113
0.1999	1.4233
0.3001	1.434
0.4000	1.4437
0.4999	1.453
0.6000	1.4616
0.7001	1.4701
0.8000	1.4782
0.9000	1.486
0.9498	1.4899

Refractive index (Na D-line) [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Refractive index (Na D-line) - Liquid
0.0500	1.4048
0.0998	1.4113
0.1999	1.4233
0.3001	1.434
0.4000	1.4437
0.4999	1.453
0.6000	1.4616
0.7001	1.4701
0.8000	1.4782
0.9000	1.486
0.9498	1.4899

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0500	953.61
0.0998	947.42
0.1999	935.21
0.3001	923.65
0.4000	912.84
0.4999	902.65
0.6000	893.14
0.7001	884.22
0.8000	875.94
0.9000	868.48
0.9498	865.12

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-methoxy- (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0586	866.02
298.15	0.1696	873.92
298.15	0.2421	879.54
298.15	0.3513	888.69
298.15	0.4555	898.18
298.15	0.4987	902.34
298.15	0.5515	907.6
298.15	0.6515	918.1
298.15	0.7487	928.97
298.15	0.8495	940.97
298.15	0.9558	954.41
303.15	0.0586	861.22
303.15	0.1696	868.96
303.15	0.2421	874.53
303.15	0.3513	883.68
303.15	0.4555	893.2
303.15	0.4987	897.37
303.15	0.5515	902.64
303.15	0.6515	913.16
303.15	0.7487	924.06
303.15	0.8495	936.09
303.15	0.9558	949.65
308.15	0.0586	856.54
308.15	0.1696	864.38
308.15	0.2421	870.06
308.15	0.3513	879.42
308.15	0.4555	889.2
308.15	0.4987	893.5
308.15	0.5515	898.93
308.15	0.6515	909.77
308.15	0.7487	921.02
308.15	0.8495	933.44
308.15	0.9558	947.44
313.15	0.0586	851.74
313.15	0.1696	859.29
313.15	0.2421	864.75
313.15	0.3513	873.72
313.15	0.4555	883.12
313.15	0.4987	887.26
313.15	0.5515	892.5
313.15	0.6515	903.02
313.15	0.7487	914.01
313.15	0.8495	926.26
313.15	0.9558	940.2

Mass density, kg/m3 [ref]

Operational conditions:

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

Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
0.0500	953.61
0.0998	947.42
0.1999	935.21
0.3001	923.65
0.4000	912.84
0.4999	902.65
0.6000	893.14
0.7001	884.22
0.8000	875.94
0.9000	868.48
0.9498	865.12

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-methoxy- (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0586	866.02
298.15	0.1696	873.92
298.15	0.2421	879.54
298.15	0.3513	888.69
298.15	0.4555	898.18
298.15	0.4987	902.34
298.15	0.5515	907.6
298.15	0.6515	918.1
298.15	0.7487	928.97
298.15	0.8495	940.97
298.15	0.9558	954.41
303.15	0.0586	861.22
303.15	0.1696	868.96
303.15	0.2421	874.53
303.15	0.3513	883.68
303.15	0.4555	893.2
303.15	0.4987	897.37
303.15	0.5515	902.64
303.15	0.6515	913.16
303.15	0.7487	924.06
303.15	0.8495	936.09
303.15	0.9558	949.65
308.15	0.0586	856.54
308.15	0.1696	864.38
308.15	0.2421	870.06
308.15	0.3513	879.42
308.15	0.4555	889.2
308.15	0.4987	893.5
308.15	0.5515	898.93
308.15	0.6515	909.77
308.15	0.7487	921.02
308.15	0.8495	933.44
308.15	0.9558	947.44
313.15	0.0586	851.74
313.15	0.1696	859.29
313.15	0.2421	864.75
313.15	0.3513	873.72
313.15	0.4555	883.12
313.15	0.4987	887.26
313.15	0.5515	892.5
313.15	0.6515	903.02
313.15	0.7487	914.01
313.15	0.8495	926.26
313.15	0.9558	940.2

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-methoxy- (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0586	1300.0
298.15	0.1696	1296.0
298.15	0.2421	1296.0
298.15	0.3513	1298.0
298.15	0.4555	1302.0
298.15	0.4987	1304.0
298.15	0.5515	1306.0
298.15	0.6515	1312.0
298.15	0.7487	1317.0
298.15	0.8495	1325.0
298.15	0.9558	1334.0
308.15	0.0586	1261.0
308.15	0.1696	1260.0
308.15	0.2421	1260.0
308.15	0.3513	1261.0
308.15	0.4555	1265.0
308.15	0.4987	1266.0
308.15	0.5515	1269.0
308.15	0.6515	1277.0
308.15	0.7487	1287.0
308.15	0.8495	1300.0
308.15	0.9558	1317.0

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethanol, 2-methoxy- (2) - Liquid	Speed of sound, m/s - Liquid
298.15	0.0586	1300.0
298.15	0.1696	1296.0
298.15	0.2421	1296.0
298.15	0.3513	1298.0
298.15	0.4555	1302.0
298.15	0.4987	1304.0
298.15	0.5515	1306.0
298.15	0.6515	1312.0
298.15	0.7487	1317.0
298.15	0.8495	1325.0
298.15	0.9558	1334.0
308.15	0.0586	1261.0
308.15	0.1696	1260.0
308.15	0.2421	1260.0
308.15	0.3513	1261.0
308.15	0.4555	1265.0
308.15	0.4987	1266.0
308.15	0.5515	1269.0
308.15	0.6515	1277.0
308.15	0.7487	1287.0
308.15	0.8495	1300.0
308.15	0.9558	1317.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Toluene (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.9710	382.76
0.9294	381.47
0.8586	380.08
0.8044	379.47
0.7616	379.27
0.7131	379.18
0.6490	379.12
0.5903	379.21
0.5110	379.64
0.3404	381.26
0.2246	383.60
0.1383	386.79
0.0998	389.06
0.0595	391.90
0.0261	394.94

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Mole fraction of Toluene (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.9710	382.76
0.9294	381.47
0.8586	380.08
0.8044	379.47
0.7616	379.27
0.7131	379.18
0.6490	379.12
0.5903	379.21
0.5110	379.64
0.3404	381.26
0.2246	383.60
0.1383	386.79
0.0998	389.06
0.0595	391.90
0.0261	394.94

Azeotropic temperature, K [ref]

Mole fraction of Toluene (1) - Liquid	Azeotropic temperature, K - Liquid
0.7020	379.08

Azeotropic pressure, kPa [ref]

Mole fraction of Toluene (1) - Liquid	Azeotropic pressure, kPa - Liquid
0.7020	101.30

Azeotropic temperature, K [ref]

Mole fraction of Toluene (1) - Liquid	Azeotropic temperature, K - Liquid
0.7020	379.08

Azeotropic pressure, kPa [ref]

Mole fraction of Toluene (1) - Liquid	Azeotropic pressure, kPa - Liquid
0.7020	101.30

Sources

• Isobaric vapor-liquid equilibrium for binary and ternary systems with toluene, 2-methoxyethanol and dimethyl sulfoxide at 101.3 kPa
• Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
• Thermodynamics of solvation in propylene glycol and methyl cellosolve
• Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane