Mixture of Isopropyl Alcohol + Piperazine, 1-methyl-

Excel

Isopropyl Alcohol

Name
Isopropyl Alcohol
InChI
InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
InChI Key
KFZMGEQAYNKOFK-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CC(C)O
Mol. Weight (g/mol)
60.09
CAS
67-63-0

Piperazine, 1-methyl-

Name
Piperazine, 1-methyl-
InChI
InChI=1S/C5H12N2/c1-7-4-2-6-3-5-7/h6H,2-5H2,1H3
InChI Key
PVOAHINGSUIXLS-UHFFFAOYSA-N
Formula
C5H12N2
SMILES
CN1CCNCC1
Mol. Weight (g/mol)
100.16
CAS
109-01-3
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry. Do not hesitate to contact us for your projects.

Datasets

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

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Isopropyl Alcohol (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0021
293.15 0.0998 0.0023
293.15 0.1988 0.0024
293.15 0.3003 0.0025
293.15 0.3998 0.0026
293.15 0.5000 0.0027
293.15 0.5996 0.0027
293.15 0.7000 0.0027
293.15 0.7991 0.0027
293.15 0.8503 0.0026
293.15 0.9003 0.0026
293.15 0.9489 0.0025
293.15 1.0000 0.0024
298.15 0.0000 0.0018
298.15 0.0998 0.0020
298.15 0.1988 0.0021
298.15 0.3003 0.0022
298.15 0.3998 0.0022
298.15 0.5000 0.0023
298.15 0.5996 0.0023
298.15 0.7000 0.0023
298.15 0.7991 0.0023
298.15 0.8503 0.0023
298.15 0.9003 0.0022
298.15 0.9489 0.0022
298.15 1.0000 0.0021
303.15 0.0000 0.0016
303.15 0.0998 0.0017
303.15 0.1988 0.0018
303.15 0.3003 0.0019
303.15 0.3998 0.0019
303.15 0.5000 0.0020
303.15 0.5996 0.0020
303.15 0.7000 0.0020
303.15 0.7991 0.0020
303.15 0.8503 0.0020
303.15 0.9003 0.0020
303.15 0.9489 0.0019
303.15 1.0000 0.0018

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Isopropyl Alcohol (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0021
293.15 0.0998 0.0023
293.15 0.1988 0.0024
293.15 0.3003 0.0025
293.15 0.3998 0.0026
293.15 0.5000 0.0027
293.15 0.5996 0.0027
293.15 0.7000 0.0027
293.15 0.7991 0.0027
293.15 0.8503 0.0026
293.15 0.9003 0.0026
293.15 0.9489 0.0025
293.15 1.0000 0.0024
298.15 0.0000 0.0018
298.15 0.0998 0.0020
298.15 0.1988 0.0021
298.15 0.3003 0.0022
298.15 0.3998 0.0022
298.15 0.5000 0.0023
298.15 0.5996 0.0023
298.15 0.7000 0.0023
298.15 0.7991 0.0023
298.15 0.8503 0.0023
298.15 0.9003 0.0022
298.15 0.9489 0.0022
298.15 1.0000 0.0021
303.15 0.0000 0.0016
303.15 0.0998 0.0017
303.15 0.1988 0.0018
303.15 0.3003 0.0019
303.15 0.3998 0.0019
303.15 0.5000 0.0020
303.15 0.5996 0.0020
303.15 0.7000 0.0020
303.15 0.7991 0.0020
303.15 0.8503 0.0020
303.15 0.9003 0.0020
303.15 0.9489 0.0019
303.15 1.0000 0.0018

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Isopropyl Alcohol (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 903.78
293.15 0.0998 897.99
293.15 0.1988 891.42
293.15 0.3003 883.75
293.15 0.3998 875.22
293.15 0.5000 865.48
293.15 0.5996 854.41
293.15 0.7000 841.49
293.15 0.7991 826.48
293.15 0.8503 817.61
293.15 0.9003 808.06
293.15 0.9489 797.8
293.15 1.0000 785.84
298.15 0.0000 899.8
298.15 0.0998 893.98
298.15 0.1988 887.39
298.15 0.3003 879.73
298.15 0.3998 871.21
298.15 0.5000 861.47
298.15 0.5996 850.38
298.15 0.7000 837.39
298.15 0.7991 822.27
298.15 0.8503 813.32
298.15 0.9003 803.69
298.15 0.9489 793.36
298.15 1.0000 781.3
303.15 0.0000 894.54
303.15 0.0998 888.87
303.15 0.1988 882.45
303.15 0.3003 874.96
303.15 0.3998 866.62
303.15 0.5000 857.07
303.15 0.5996 846.15
303.15 0.7000 833.32
303.15 0.7991 818.3
303.15 0.8503 809.39
303.15 0.9003 799.79
303.15 0.9489 789.46
303.15 1.0000 777.41

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Isopropyl Alcohol (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 903.78
293.15 0.0998 897.99
293.15 0.1988 891.42
293.15 0.3003 883.75
293.15 0.3998 875.22
293.15 0.5000 865.48
293.15 0.5996 854.41
293.15 0.7000 841.49
293.15 0.7991 826.48
293.15 0.8503 817.61
293.15 0.9003 808.06
293.15 0.9489 797.8
293.15 1.0000 785.84
298.15 0.0000 899.8
298.15 0.0998 893.98
298.15 0.1988 887.39
298.15 0.3003 879.73
298.15 0.3998 871.21
298.15 0.5000 861.47
298.15 0.5996 850.38
298.15 0.7000 837.39
298.15 0.7991 822.27
298.15 0.8503 813.32
298.15 0.9003 803.69
298.15 0.9489 793.36
298.15 1.0000 781.3
303.15 0.0000 894.54
303.15 0.0998 888.87
303.15 0.1988 882.45
303.15 0.3003 874.96
303.15 0.3998 866.62
303.15 0.5000 857.07
303.15 0.5996 846.15
303.15 0.7000 833.32
303.15 0.7991 818.3
303.15 0.8503 809.39
303.15 0.9003 799.79
303.15 0.9489 789.46
303.15 1.0000 777.41

Sources