Mixture of Piperazine, 1-methyl- + Methyl Alcohol

Datasets

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

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0021
293.15	0.1021	0.0021
293.15	0.1999	0.0021
293.15	0.3286	0.0022
293.15	0.4143	0.0021
293.15	0.4991	0.0020
293.15	0.6016	0.0019
293.15	0.6999	0.0016
293.15	0.7998	0.0013
293.15	0.8999	0.0009
293.15	1.0000	0.0006
298.15	0.0000	0.0018
298.15	0.1021	0.0018
298.15	0.1999	0.0019
298.15	0.3286	0.0019
298.15	0.4143	0.0019
298.15	0.4991	0.0018
298.15	0.6016	0.0017
298.15	0.6999	0.0014
298.15	0.7998	0.0012
298.15	0.8999	0.0009
298.15	1.0000	0.0006
303.15	0.0000	0.0016
303.15	0.1021	0.0016
303.15	0.1999	0.0017
303.15	0.3286	0.0017
303.15	0.4143	0.0017
303.15	0.4991	0.0016
303.15	0.6016	0.0015
303.15	0.6999	0.0013
303.15	0.7998	0.0011
303.15	0.8999	0.0008
303.15	1.0000	0.0005

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.0000	0.0021
293.15	0.1021	0.0021
293.15	0.1999	0.0021
293.15	0.3286	0.0022
293.15	0.4143	0.0021
293.15	0.4991	0.0020
293.15	0.6016	0.0019
293.15	0.6999	0.0016
293.15	0.7998	0.0013
293.15	0.8999	0.0009
293.15	1.0000	0.0006
298.15	0.0000	0.0018
298.15	0.1021	0.0018
298.15	0.1999	0.0019
298.15	0.3286	0.0019
298.15	0.4143	0.0019
298.15	0.4991	0.0018
298.15	0.6016	0.0017
298.15	0.6999	0.0014
298.15	0.7998	0.0012
298.15	0.8999	0.0009
298.15	1.0000	0.0006
303.15	0.0000	0.0016
303.15	0.1021	0.0016
303.15	0.1999	0.0017
303.15	0.3286	0.0017
303.15	0.4143	0.0017
303.15	0.4991	0.0016
303.15	0.6016	0.0015
303.15	0.6999	0.0013
303.15	0.7998	0.0011
303.15	0.8999	0.0008
303.15	1.0000	0.0005

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	903.8
293.15	0.1021	902.85
293.15	0.1999	901.87
293.15	0.3286	899.35
293.15	0.4143	896.64
293.15	0.4991	892.94
293.15	0.6016	886.48
293.15	0.6999	876.84
293.15	0.7998	860.91
293.15	0.8999	834.46
293.15	1.0000	791.09
298.15	0.0000	899.8
298.15	0.1021	899.04
298.15	0.1999	898.08
298.15	0.3286	895.54
298.15	0.4143	892.82
298.15	0.4991	889.13
298.15	0.6016	882.68
298.15	0.6999	873.0
298.15	0.7998	856.96
298.15	0.8999	830.26
298.15	1.0000	786.48
303.15	0.0000	894.52
303.15	0.1021	893.84
303.15	0.1999	892.86
303.15	0.3286	890.39
303.15	0.4143	887.8
303.15	0.4991	884.25
303.15	0.6016	877.91
303.15	0.6999	868.21
303.15	0.7998	851.99
303.15	0.8999	825.04
303.15	1.0000	781.22

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.0000	903.8
293.15	0.1021	902.85
293.15	0.1999	901.87
293.15	0.3286	899.35
293.15	0.4143	896.64
293.15	0.4991	892.94
293.15	0.6016	886.48
293.15	0.6999	876.84
293.15	0.7998	860.91
293.15	0.8999	834.46
293.15	1.0000	791.09
298.15	0.0000	899.8
298.15	0.1021	899.04
298.15	0.1999	898.08
298.15	0.3286	895.54
298.15	0.4143	892.82
298.15	0.4991	889.13
298.15	0.6016	882.68
298.15	0.6999	873.0
298.15	0.7998	856.96
298.15	0.8999	830.26
298.15	1.0000	786.48
303.15	0.0000	894.52
303.15	0.1021	893.84
303.15	0.1999	892.86
303.15	0.3286	890.39
303.15	0.4143	887.8
303.15	0.4991	884.25
303.15	0.6016	877.91
303.15	0.6999	868.21
303.15	0.7998	851.99
303.15	0.8999	825.04
303.15	1.0000	781.22

Sources

• Viscosities and densities for binary mixtures of N-methylpiperazine with methanol, ethanol, n-propanol, iso-propanol, n-butanol and iso-butanol at 293.15, 298.15 and 303.15K