Mixture of Toluene + N-Formylmorpholine

Datasets

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

Activity coefficient of Toluene (1) [ref]

Operational conditions:

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

Temperature, K - Liquid	Activity coefficient of Toluene (1) - Liquid
333.20	2.71
348.20	4.04
363.20	2.55

Activity coefficient of Toluene (1) [ref]

Operational conditions:

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

Temperature, K - Liquid	Activity coefficient of Toluene (1) - Liquid
333.20	2.71
348.20	4.04
363.20	2.55

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Toluene (1) - Liquid	Mole fraction of Toluene (1) - Gas
0.3580	0.9668
0.4071	0.9733
0.4281	0.9757
0.4732	0.9797
0.5074	0.9819
0.5553	0.9839
0.5903	0.9857
0.6448	0.9873
0.7098	0.9892
0.7882	0.9909

Mole fraction of Toluene (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of Toluene (1) - Liquid	Mole fraction of Toluene (1) - Gas
0.3580	0.9668
0.4071	0.9733
0.4281	0.9757
0.4732	0.9797
0.5074	0.9819
0.5553	0.9839
0.5903	0.9857
0.6448	0.9873
0.7098	0.9892
0.7882	0.9909

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0080
298.15	0.0997	0.0060
298.15	0.1857	0.0043
298.15	0.2987	0.0031
298.15	0.3979	0.0023
298.15	0.4996	0.0018
298.15	0.5993	0.0014
298.15	0.7010	0.0011
298.15	0.8004	0.0008
298.15	0.9000	0.0007
298.15	1.0000	0.0006
303.15	0.0000	0.0069
303.15	0.0997	0.0052
303.15	0.1857	0.0038
303.15	0.2987	0.0028
303.15	0.3979	0.0021
303.15	0.4996	0.0016
303.15	0.5993	0.0013
303.15	0.7010	0.0010
303.15	0.8004	0.0008
303.15	0.9000	0.0006
303.15	1.0000	0.0005
313.15	0.0000	0.0052
313.15	0.0997	0.0040
313.15	0.1857	0.0030
313.15	0.2987	0.0022
313.15	0.3979	0.0018
313.15	0.4996	0.0013
313.15	0.5993	0.0011
313.15	0.7010	0.0009
313.15	0.8004	0.0007
313.15	0.9000	0.0006
313.15	1.0000	0.0005
323.15	0.0000	0.0041
323.15	0.0997	0.0032
323.15	0.1857	0.0025
323.15	0.2987	0.0019
323.15	0.3979	0.0015
323.15	0.4996	0.0011
323.15	0.5993	0.0009
323.15	0.7010	0.0007
323.15	0.8004	0.0006
323.15	0.9000	0.0005
323.15	1.0000	0.0004
333.15	0.0000	0.0033
333.15	0.0997	0.0026
333.15	0.1857	0.0021
333.15	0.2987	0.0016
333.15	0.3979	0.0013
333.15	0.4996	0.0010
333.15	0.5993	0.0008
333.15	0.7010	0.0007
333.15	0.8004	0.0005
333.15	0.9000	0.0005
333.15	1.0000	0.0004
343.15	0.0000	0.0027
343.15	0.0997	0.0022
343.15	0.1857	0.0017
343.15	0.2987	0.0014
343.15	0.3979	0.0011
343.15	0.4996	0.0009
343.15	0.5993	0.0007
343.15	0.7010	0.0006
343.15	0.8004	0.0005
343.15	0.9000	0.0004
343.15	1.0000	0.0003
353.15	0.0000	0.0023
353.15	0.0997	0.0018
353.15	0.1857	0.0015
353.15	0.2987	0.0012
353.15	0.3979	0.0010
353.15	0.4996	0.0008
353.15	0.5993	0.0006
353.15	0.7010	0.0005
353.15	0.8004	0.0004
353.15	0.9000	0.0004
353.15	1.0000	0.0003

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0080
298.15	0.0997	0.0060
298.15	0.1857	0.0043
298.15	0.2987	0.0031
298.15	0.3979	0.0023
298.15	0.4996	0.0018
298.15	0.5993	0.0014
298.15	0.7010	0.0011
298.15	0.8004	0.0008
298.15	0.9000	0.0007
298.15	1.0000	0.0006
303.15	0.0000	0.0069
303.15	0.0997	0.0052
303.15	0.1857	0.0038
303.15	0.2987	0.0028
303.15	0.3979	0.0021
303.15	0.4996	0.0016
303.15	0.5993	0.0013
303.15	0.7010	0.0010
303.15	0.8004	0.0008
303.15	0.9000	0.0006
303.15	1.0000	0.0005
313.15	0.0000	0.0052
313.15	0.0997	0.0040
313.15	0.1857	0.0030
313.15	0.2987	0.0022
313.15	0.3979	0.0018
313.15	0.4996	0.0013
313.15	0.5993	0.0011
313.15	0.7010	0.0009
313.15	0.8004	0.0007
313.15	0.9000	0.0006
313.15	1.0000	0.0005
323.15	0.0000	0.0041
323.15	0.0997	0.0032
323.15	0.1857	0.0025
323.15	0.2987	0.0019
323.15	0.3979	0.0015
323.15	0.4996	0.0011
323.15	0.5993	0.0009
323.15	0.7010	0.0007
323.15	0.8004	0.0006
323.15	0.9000	0.0005
323.15	1.0000	0.0004
333.15	0.0000	0.0033
333.15	0.0997	0.0026
333.15	0.1857	0.0021
333.15	0.2987	0.0016
333.15	0.3979	0.0013
333.15	0.4996	0.0010
333.15	0.5993	0.0008
333.15	0.7010	0.0007
333.15	0.8004	0.0005
333.15	0.9000	0.0005
333.15	1.0000	0.0004
343.15	0.0000	0.0027
343.15	0.0997	0.0022
343.15	0.1857	0.0017
343.15	0.2987	0.0014
343.15	0.3979	0.0011
343.15	0.4996	0.0009
343.15	0.5993	0.0007
343.15	0.7010	0.0006
343.15	0.8004	0.0005
343.15	0.9000	0.0004
343.15	1.0000	0.0003
353.15	0.0000	0.0023
353.15	0.0997	0.0018
353.15	0.1857	0.0015
353.15	0.2987	0.0012
353.15	0.3979	0.0010
353.15	0.4996	0.0008
353.15	0.5993	0.0006
353.15	0.7010	0.0005
353.15	0.8004	0.0004
353.15	0.9000	0.0004
353.15	1.0000	0.0003

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	1146.06
298.15	0.0997	1118.85
298.15	0.1857	1095.98
298.15	0.2987	1064.62
298.15	0.3979	1036.62
298.15	0.4996	1007.87
298.15	0.5993	979.41
298.15	0.7010	949.94
298.15	0.8004	920.72
298.15	0.9000	891.62
298.15	1.0000	861.65
303.15	0.0000	1141.7
303.15	0.0997	1114.45
303.15	0.1857	1091.57
303.15	0.2987	1060.17
303.15	0.3979	1032.11
303.15	0.4996	1003.25
303.15	0.5993	974.76
303.15	0.7010	945.23
303.15	0.8004	916.11
303.15	0.9000	887.0
303.15	1.0000	857.01
313.15	0.0000	1132.96
313.15	0.0997	1105.62
313.15	0.1857	1082.68
313.15	0.2987	1051.22
313.15	0.3979	1022.87
313.15	0.4996	993.89
313.15	0.5993	965.36
313.15	0.7010	935.9
313.15	0.8004	906.8
313.15	0.9000	877.53
313.15	1.0000	847.63
323.15	0.0000	1124.33
323.15	0.0997	1096.88
323.15	0.1857	1073.89
323.15	0.2987	1042.33
323.15	0.3979	1013.75
323.15	0.4996	984.5
323.15	0.5993	955.91
323.15	0.7010	926.58
323.15	0.8004	897.51
323.15	0.9000	868.21
323.15	1.0000	838.23
333.15	0.0000	1115.63
333.15	0.0997	1088.08
333.15	0.1857	1065.0
333.15	0.2987	1033.38
333.15	0.3979	1004.52
333.15	0.4996	975.06
333.15	0.5993	946.52
333.15	0.7010	917.23
333.15	0.8004	888.11
333.15	0.9000	858.77
333.15	1.0000	828.71
343.15	0.0000	1107.96
343.15	0.0997	1080.32
343.15	0.1857	1057.15
343.15	0.2987	1025.32
343.15	0.3979	996.41
343.15	0.4996	966.84
343.15	0.5993	938.07
343.15	0.7010	908.7
343.15	0.8004	879.44
343.15	0.9000	850.05
343.15	1.0000	819.86
353.15	0.0000	1098.76
353.15	0.0997	1070.98
353.15	0.1857	1047.73
353.15	0.2987	1015.94
353.15	0.3979	986.63
353.15	0.4996	957.13
353.15	0.5993	928.16
353.15	0.7010	898.81
353.15	0.8004	869.48
353.15	0.9000	839.94
353.15	1.0000	809.68

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Toluene (1) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	1146.06
298.15	0.0997	1118.85
298.15	0.1857	1095.98
298.15	0.2987	1064.62
298.15	0.3979	1036.62
298.15	0.4996	1007.87
298.15	0.5993	979.41
298.15	0.7010	949.94
298.15	0.8004	920.72
298.15	0.9000	891.62
298.15	1.0000	861.65
303.15	0.0000	1141.7
303.15	0.0997	1114.45
303.15	0.1857	1091.57
303.15	0.2987	1060.17
303.15	0.3979	1032.11
303.15	0.4996	1003.25
303.15	0.5993	974.76
303.15	0.7010	945.23
303.15	0.8004	916.11
303.15	0.9000	887.0
303.15	1.0000	857.01
313.15	0.0000	1132.96
313.15	0.0997	1105.62
313.15	0.1857	1082.68
313.15	0.2987	1051.22
313.15	0.3979	1022.87
313.15	0.4996	993.89
313.15	0.5993	965.36
313.15	0.7010	935.9
313.15	0.8004	906.8
313.15	0.9000	877.53
313.15	1.0000	847.63
323.15	0.0000	1124.33
323.15	0.0997	1096.88
323.15	0.1857	1073.89
323.15	0.2987	1042.33
323.15	0.3979	1013.75
323.15	0.4996	984.5
323.15	0.5993	955.91
323.15	0.7010	926.58
323.15	0.8004	897.51
323.15	0.9000	868.21
323.15	1.0000	838.23
333.15	0.0000	1115.63
333.15	0.0997	1088.08
333.15	0.1857	1065.0
333.15	0.2987	1033.38
333.15	0.3979	1004.52
333.15	0.4996	975.06
333.15	0.5993	946.52
333.15	0.7010	917.23
333.15	0.8004	888.11
333.15	0.9000	858.77
333.15	1.0000	828.71
343.15	0.0000	1107.96
343.15	0.0997	1080.32
343.15	0.1857	1057.15
343.15	0.2987	1025.32
343.15	0.3979	996.41
343.15	0.4996	966.84
343.15	0.5993	938.07
343.15	0.7010	908.7
343.15	0.8004	879.44
343.15	0.9000	850.05
343.15	1.0000	819.86
353.15	0.0000	1098.76
353.15	0.0997	1070.98
353.15	0.1857	1047.73
353.15	0.2987	1015.94
353.15	0.3979	986.63
353.15	0.4996	957.13
353.15	0.5993	928.16
353.15	0.7010	898.81
353.15	0.8004	869.48
353.15	0.9000	839.94
353.15	1.0000	809.68

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
0.3580	399.65
0.4071	397.06
0.4281	395.95
0.4732	394.75
0.5074	393.22
0.5553	391.90
0.5903	391.05
0.6448	389.46
0.7098	388.34
0.7882	386.90

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
0.3580	399.65
0.4071	397.06
0.4281	395.95
0.4732	394.75
0.5074	393.22
0.5553	391.90
0.5903	391.05
0.6448	389.46
0.7098	388.34
0.7882	386.90

Sources

• Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
• Densities and Viscosities of N-Formylmorpholine + Benzene, + Toluene at Different Temperatures and Atmospheric Pressures
• Vapor Liquid Equilibrium of N-Formylmorpholine with Toluene and Xylene at 101.33 kPa