Mixture of 1-Propanol + Piperazine, 1-methyl-

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1-Propanol

Name
1-Propanol
InChI
InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
InChI Key
BDERNNFJNOPAEC-UHFFFAOYSA-N
Formula
C3H8O
SMILES
CCCO
Mol. Weight (g/mol)
60.09
CAS
71-23-8

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
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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 1-Propanol (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0021
293.15 0.1017 0.0022
293.15 0.1987 0.0024
293.15 0.3000 0.0025
293.15 0.4007 0.0027
293.15 0.4998 0.0028
293.15 0.5504 0.0029
293.15 0.6011 0.0029
293.15 0.6542 0.0029
293.15 0.7001 0.0029
293.15 0.7495 0.0028
293.15 0.7991 0.0028
293.15 0.9020 0.0025
293.15 1.0000 0.0022
298.15 0.0000 0.0018
298.15 0.1017 0.0020
298.15 0.1987 0.0021
298.15 0.3000 0.0022
298.15 0.4007 0.0023
298.15 0.4998 0.0024
298.15 0.5504 0.0025
298.15 0.6011 0.0025
298.15 0.6542 0.0025
298.15 0.7001 0.0025
298.15 0.7495 0.0025
298.15 0.7991 0.0024
298.15 0.9020 0.0022
298.15 1.0000 0.0019
303.15 0.0000 0.0016
303.15 0.1017 0.0017
303.15 0.1987 0.0018
303.15 0.3000 0.0019
303.15 0.4007 0.0020
303.15 0.4998 0.0021
303.15 0.5504 0.0022
303.15 0.6011 0.0022
303.15 0.6542 0.0022
303.15 0.7001 0.0022
303.15 0.7495 0.0022
303.15 0.7991 0.0021
303.15 0.9020 0.0020
303.15 1.0000 0.0017

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propanol (1) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0021
293.15 0.1017 0.0022
293.15 0.1987 0.0024
293.15 0.3000 0.0025
293.15 0.4007 0.0027
293.15 0.4998 0.0028
293.15 0.5504 0.0029
293.15 0.6011 0.0029
293.15 0.6542 0.0029
293.15 0.7001 0.0029
293.15 0.7495 0.0028
293.15 0.7991 0.0028
293.15 0.9020 0.0025
293.15 1.0000 0.0022
298.15 0.0000 0.0018
298.15 0.1017 0.0020
298.15 0.1987 0.0021
298.15 0.3000 0.0022
298.15 0.4007 0.0023
298.15 0.4998 0.0024
298.15 0.5504 0.0025
298.15 0.6011 0.0025
298.15 0.6542 0.0025
298.15 0.7001 0.0025
298.15 0.7495 0.0025
298.15 0.7991 0.0024
298.15 0.9020 0.0022
298.15 1.0000 0.0019
303.15 0.0000 0.0016
303.15 0.1017 0.0017
303.15 0.1987 0.0018
303.15 0.3000 0.0019
303.15 0.4007 0.0020
303.15 0.4998 0.0021
303.15 0.5504 0.0022
303.15 0.6011 0.0022
303.15 0.6542 0.0022
303.15 0.7001 0.0022
303.15 0.7495 0.0022
303.15 0.7991 0.0021
303.15 0.9020 0.0020
303.15 1.0000 0.0017

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propanol (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 903.79
293.15 0.1017 899.72
293.15 0.1987 895.17
293.15 0.3000 889.62
293.15 0.4007 883.15
293.15 0.4998 875.68
293.15 0.5504 871.35
293.15 0.6011 866.59
293.15 0.6542 861.09
293.15 0.7001 855.83
293.15 0.7495 849.57
293.15 0.7991 842.55
293.15 0.9020 825.1
293.15 1.0000 803.79
298.15 0.0000 899.8
298.15 0.1017 895.76
298.15 0.1987 891.23
298.15 0.3000 885.71
298.15 0.4007 879.31
298.15 0.4998 871.91
298.15 0.5504 867.6
298.15 0.6011 862.85
298.15 0.6542 857.34
298.15 0.7001 852.05
298.15 0.7495 845.75
298.15 0.7991 838.67
298.15 0.9020 821.08
298.15 1.0000 799.74
303.15 0.0000 894.54
303.15 0.1017 890.62
303.15 0.1987 886.21
303.15 0.3000 880.86
303.15 0.4007 874.64
303.15 0.4998 867.4
303.15 0.5504 863.18
303.15 0.6011 858.5
303.15 0.6542 853.04
303.15 0.7001 847.8
303.15 0.7495 841.53
303.15 0.7991 834.47
303.15 0.9020 816.93
303.15 1.0000 795.68

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Propanol (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 903.79
293.15 0.1017 899.72
293.15 0.1987 895.17
293.15 0.3000 889.62
293.15 0.4007 883.15
293.15 0.4998 875.68
293.15 0.5504 871.35
293.15 0.6011 866.59
293.15 0.6542 861.09
293.15 0.7001 855.83
293.15 0.7495 849.57
293.15 0.7991 842.55
293.15 0.9020 825.1
293.15 1.0000 803.79
298.15 0.0000 899.8
298.15 0.1017 895.76
298.15 0.1987 891.23
298.15 0.3000 885.71
298.15 0.4007 879.31
298.15 0.4998 871.91
298.15 0.5504 867.6
298.15 0.6011 862.85
298.15 0.6542 857.34
298.15 0.7001 852.05
298.15 0.7495 845.75
298.15 0.7991 838.67
298.15 0.9020 821.08
298.15 1.0000 799.74
303.15 0.0000 894.54
303.15 0.1017 890.62
303.15 0.1987 886.21
303.15 0.3000 880.86
303.15 0.4007 874.64
303.15 0.4998 867.4
303.15 0.5504 863.18
303.15 0.6011 858.5
303.15 0.6542 853.04
303.15 0.7001 847.8
303.15 0.7495 841.53
303.15 0.7991 834.47
303.15 0.9020 816.93
303.15 1.0000 795.68

Sources