Mixture of Benzene + 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	0.0007
298.15	0.2001	0.0007
298.15	0.3000	0.0008
298.15	0.4001	0.0009
298.15	0.5000	0.0010
298.15	0.5999	0.0011
298.15	0.7000	0.0012
298.15	0.8000	0.0013
298.15	0.9000	0.0014
298.15	1.0000	0.0015
308.15	0.0000	0.0005
308.15	0.1000	0.0006
308.15	0.2001	0.0006
308.15	0.3000	0.0007
308.15	0.4001	0.0008
308.15	0.5000	0.0008
308.15	0.5999	0.0009
308.15	0.7000	0.0010
308.15	0.8000	0.0011
308.15	0.9000	0.0012
308.15	1.0000	0.0013
318.15	0.0000	0.0005
318.15	0.1000	0.0005
318.15	0.2001	0.0006
318.15	0.3000	0.0006
318.15	0.4001	0.0007
318.15	0.5000	0.0007
318.15	0.5999	0.0008
318.15	0.7000	0.0009
318.15	0.8000	0.0009
318.15	0.9000	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	0.0007
298.15	0.2001	0.0007
298.15	0.3000	0.0008
298.15	0.4001	0.0009
298.15	0.5000	0.0010
298.15	0.5999	0.0011
298.15	0.7000	0.0012
298.15	0.8000	0.0013
298.15	0.9000	0.0014
298.15	1.0000	0.0015
308.15	0.0000	0.0005
308.15	0.1000	0.0006
308.15	0.2001	0.0006
308.15	0.3000	0.0007
308.15	0.4001	0.0008
308.15	0.5000	0.0008
308.15	0.5999	0.0009
308.15	0.7000	0.0010
308.15	0.8000	0.0011
308.15	0.9000	0.0012
308.15	1.0000	0.0013
318.15	0.0000	0.0005
318.15	0.1000	0.0005
318.15	0.2001	0.0006
318.15	0.3000	0.0006
318.15	0.4001	0.0007
318.15	0.5000	0.0007
318.15	0.5999	0.0008
318.15	0.7000	0.0009
318.15	0.8000	0.0009
318.15	0.9000	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	873.61
298.15	0.1000	905.57
298.15	0.2001	935.29
298.15	0.3000	962.99
298.15	0.4001	989.08
298.15	0.5000	1013.66
298.15	0.5999	1036.89
298.15	0.7000	1058.82
298.15	0.8000	1079.42
298.15	0.9000	1098.6
298.15	1.0000	1116.24
308.15	0.0000	862.28
308.15	0.1000	894.74
308.15	0.2001	924.42
308.15	0.3000	952.12
308.15	0.4001	978.2
308.15	0.5000	1002.77
308.15	0.5999	1026.01
308.15	0.7000	1047.97
308.15	0.8000	1068.49
308.15	0.9000	1087.62
308.15	1.0000	1105.22
318.15	0.0000	852.08
318.15	0.1000	883.87
318.15	0.2001	913.49
318.15	0.3000	941.13
318.15	0.4001	967.18
318.15	0.5000	991.75
318.15	0.5999	1014.99
318.15	0.7000	1036.94
318.15	0.8000	1057.55
318.15	0.9000	1076.65
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	873.61
298.15	0.1000	905.57
298.15	0.2001	935.29
298.15	0.3000	962.99
298.15	0.4001	989.08
298.15	0.5000	1013.66
298.15	0.5999	1036.89
298.15	0.7000	1058.82
298.15	0.8000	1079.42
298.15	0.9000	1098.6
298.15	1.0000	1116.24
308.15	0.0000	862.28
308.15	0.1000	894.74
308.15	0.2001	924.42
308.15	0.3000	952.12
308.15	0.4001	978.2
308.15	0.5000	1002.77
308.15	0.5999	1026.01
308.15	0.7000	1047.97
308.15	0.8000	1068.49
308.15	0.9000	1087.62
308.15	1.0000	1105.22
318.15	0.0000	852.08
318.15	0.1000	883.87
318.15	0.2001	913.49
318.15	0.3000	941.13
318.15	0.4001	967.18
318.15	0.5000	991.75
318.15	0.5999	1014.99
318.15	0.7000	1036.94
318.15	0.8000	1057.55
318.15	0.9000	1076.65
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