Mixture of Toluene + Butanoic acid, 4-chloro-, methyl ester

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butanoic acid, 4-chloro-, methyl ester (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0006
298.15	0.1000	0.0006
298.15	0.2000	0.0007
298.15	0.3000	0.0008
298.15	0.4001	0.0008
298.15	0.5000	0.0009
298.15	0.6000	0.0010
298.15	0.7000	0.0011
298.15	0.8000	0.0012
298.15	0.8998	0.0014
298.15	1.0000	0.0015
308.15	0.0000	0.0005
308.15	0.1000	0.0006
308.15	0.2000	0.0006
308.15	0.3000	0.0007
308.15	0.4001	0.0007
308.15	0.5000	0.0008
308.15	0.6000	0.0009
308.15	0.7000	0.0010
308.15	0.8000	0.0011
308.15	0.8998	0.0012
308.15	1.0000	0.0013
318.15	0.0000	0.0004
318.15	0.1000	0.0005
318.15	0.2000	0.0005
318.15	0.3000	0.0006
318.15	0.4001	0.0006
318.15	0.5000	0.0007
318.15	0.6000	0.0008
318.15	0.7000	0.0008
318.15	0.8000	0.0009
318.15	0.8998	0.0010
318.15	1.0000	0.0011

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butanoic acid, 4-chloro-, methyl ester (2) - Liquid	Viscosity, Pa*s - Liquid
298.15	0.0000	0.0006
298.15	0.1000	0.0006
298.15	0.2000	0.0007
298.15	0.3000	0.0008
298.15	0.4001	0.0008
298.15	0.5000	0.0009
298.15	0.6000	0.0010
298.15	0.7000	0.0011
298.15	0.8000	0.0012
298.15	0.8998	0.0014
298.15	1.0000	0.0015
308.15	0.0000	0.0005
308.15	0.1000	0.0006
308.15	0.2000	0.0006
308.15	0.3000	0.0007
308.15	0.4001	0.0007
308.15	0.5000	0.0008
308.15	0.6000	0.0009
308.15	0.7000	0.0010
308.15	0.8000	0.0011
308.15	0.8998	0.0012
308.15	1.0000	0.0013
318.15	0.0000	0.0004
318.15	0.1000	0.0005
318.15	0.2000	0.0005
318.15	0.3000	0.0006
318.15	0.4001	0.0006
318.15	0.5000	0.0007
318.15	0.6000	0.0008
318.15	0.7000	0.0008
318.15	0.8000	0.0009
318.15	0.8998	0.0010
318.15	1.0000	0.0011

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butanoic acid, 4-chloro-, methyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	862.18
298.15	0.1000	891.28
298.15	0.2000	919.47
298.15	0.3000	946.73
298.15	0.4001	973.21
298.15	0.5000	998.81
298.15	0.6000	1023.69
298.15	0.7000	1047.84
298.15	0.8000	1071.31
298.15	0.8998	1094.05
298.15	1.0000	1116.24
308.15	0.0000	852.81
308.15	0.1000	881.71
308.15	0.2000	909.69
308.15	0.3000	936.79
308.15	0.4001	963.07
308.15	0.5000	988.49
308.15	0.6000	1013.23
308.15	0.7000	1037.22
308.15	0.8000	1060.54
308.15	0.8998	1083.16
308.15	1.0000	1105.22
318.15	0.0000	843.4
318.15	0.1000	872.09
318.15	0.2000	899.87
318.15	0.3000	926.77
318.15	0.4001	952.89
318.15	0.5000	978.14
318.15	0.6000	1002.74
318.15	0.7000	1026.57
318.15	0.8000	1049.74
318.15	0.8998	1072.21
318.15	1.0000	1094.13

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Butanoic acid, 4-chloro-, methyl ester (2) - Liquid	Mass density, kg/m3 - Liquid
298.15	0.0000	862.18
298.15	0.1000	891.28
298.15	0.2000	919.47
298.15	0.3000	946.73
298.15	0.4001	973.21
298.15	0.5000	998.81
298.15	0.6000	1023.69
298.15	0.7000	1047.84
298.15	0.8000	1071.31
298.15	0.8998	1094.05
298.15	1.0000	1116.24
308.15	0.0000	852.81
308.15	0.1000	881.71
308.15	0.2000	909.69
308.15	0.3000	936.79
308.15	0.4001	963.07
308.15	0.5000	988.49
308.15	0.6000	1013.23
308.15	0.7000	1037.22
308.15	0.8000	1060.54
308.15	0.8998	1083.16
308.15	1.0000	1105.22
318.15	0.0000	843.4
318.15	0.1000	872.09
318.15	0.2000	899.87
318.15	0.3000	926.77
318.15	0.4001	952.89
318.15	0.5000	978.14
318.15	0.6000	1002.74
318.15	0.7000	1026.57
318.15	0.8000	1049.74
318.15	0.8998	1072.21
318.15	1.0000	1094.13

Sources

• Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K