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

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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

1-Butanol

Name
1-Butanol
InChI
InChI=1S/C4H10O/c1-2-3-4-5/h5H,2-4H2,1H3
InChI Key
LRHPLDYGYMQRHN-UHFFFAOYSA-N
Formula
C4H10O
SMILES
CCCCO
Mol. Weight (g/mol)
74.12
CAS
71-36-3
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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-Butanol (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0021
293.15 0.0982 0.0022
293.15 0.1990 0.0024
293.15 0.2966 0.0026
293.15 0.3973 0.0028
293.15 0.5001 0.0030
293.15 0.6004 0.0032
293.15 0.6995 0.0033
293.15 0.7537 0.0033
293.15 0.7936 0.0033
293.15 0.8002 0.0032
293.15 0.8419 0.0032
293.15 0.8997 0.0031
293.15 1.0000 0.0029
298.15 0.0000 0.0018
298.15 0.0982 0.0020
298.15 0.1990 0.0021
298.15 0.2966 0.0023
298.15 0.3973 0.0025
298.15 0.5001 0.0026
298.15 0.6004 0.0028
298.15 0.6995 0.0028
298.15 0.7537 0.0028
298.15 0.7936 0.0028
298.15 0.8002 0.0028
298.15 0.8419 0.0028
298.15 0.8997 0.0028
298.15 1.0000 0.0026
303.15 0.0000 0.0016
303.15 0.0982 0.0017
303.15 0.1990 0.0019
303.15 0.2966 0.0020
303.15 0.3973 0.0022
303.15 0.5001 0.0023
303.15 0.6004 0.0024
303.15 0.6995 0.0025
303.15 0.7537 0.0025
303.15 0.7936 0.0025
303.15 0.8002 0.0025
303.15 0.8419 0.0025
303.15 0.8997 0.0024
303.15 1.0000 0.0023

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Viscosity, Pa*s - Liquid
293.15 0.0000 0.0021
293.15 0.0982 0.0022
293.15 0.1990 0.0024
293.15 0.2966 0.0026
293.15 0.3973 0.0028
293.15 0.5001 0.0030
293.15 0.6004 0.0032
293.15 0.6995 0.0033
293.15 0.7537 0.0033
293.15 0.7936 0.0033
293.15 0.8002 0.0032
293.15 0.8419 0.0032
293.15 0.8997 0.0031
293.15 1.0000 0.0029
298.15 0.0000 0.0018
298.15 0.0982 0.0020
298.15 0.1990 0.0021
298.15 0.2966 0.0023
298.15 0.3973 0.0025
298.15 0.5001 0.0026
298.15 0.6004 0.0028
298.15 0.6995 0.0028
298.15 0.7537 0.0028
298.15 0.7936 0.0028
298.15 0.8002 0.0028
298.15 0.8419 0.0028
298.15 0.8997 0.0028
298.15 1.0000 0.0026
303.15 0.0000 0.0016
303.15 0.0982 0.0017
303.15 0.1990 0.0019
303.15 0.2966 0.0020
303.15 0.3973 0.0022
303.15 0.5001 0.0023
303.15 0.6004 0.0024
303.15 0.6995 0.0025
303.15 0.7537 0.0025
303.15 0.7936 0.0025
303.15 0.8002 0.0025
303.15 0.8419 0.0025
303.15 0.8997 0.0024
303.15 1.0000 0.0023

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 903.79
293.15 0.0982 898.89
293.15 0.1990 893.13
293.15 0.2966 886.88
293.15 0.3973 879.73
293.15 0.5001 871.61
293.15 0.6004 862.72
293.15 0.6995 852.72
293.15 0.7537 846.6
293.15 0.7936 841.74
293.15 0.8002 840.9
293.15 0.8419 835.38
293.15 0.8997 827.0
293.15 1.0000 809.97
298.15 0.0000 899.8
298.15 0.0982 894.98
298.15 0.1990 889.24
298.15 0.2966 883.01
298.15 0.3973 875.91
298.15 0.5001 867.85
298.15 0.6004 859.01
298.15 0.6995 849.01
298.15 0.7537 842.86
298.15 0.7936 837.97
298.15 0.8002 837.13
298.15 0.8419 831.58
298.15 0.8997 823.16
298.15 1.0000 806.15
303.15 0.0000 894.54
303.15 0.0982 889.88
303.15 0.1990 884.23
303.15 0.2966 878.11
303.15 0.3973 871.16
303.15 0.5001 863.29
303.15 0.6004 854.62
303.15 0.6995 844.76
303.15 0.7537 838.67
303.15 0.7936 833.81
303.15 0.8002 832.97
303.15 0.8419 827.45
303.15 0.8997 819.05
303.15 1.0000 802.14

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.325 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1-Butanol (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 903.79
293.15 0.0982 898.89
293.15 0.1990 893.13
293.15 0.2966 886.88
293.15 0.3973 879.73
293.15 0.5001 871.61
293.15 0.6004 862.72
293.15 0.6995 852.72
293.15 0.7537 846.6
293.15 0.7936 841.74
293.15 0.8002 840.9
293.15 0.8419 835.38
293.15 0.8997 827.0
293.15 1.0000 809.97
298.15 0.0000 899.8
298.15 0.0982 894.98
298.15 0.1990 889.24
298.15 0.2966 883.01
298.15 0.3973 875.91
298.15 0.5001 867.85
298.15 0.6004 859.01
298.15 0.6995 849.01
298.15 0.7537 842.86
298.15 0.7936 837.97
298.15 0.8002 837.13
298.15 0.8419 831.58
298.15 0.8997 823.16
298.15 1.0000 806.15
303.15 0.0000 894.54
303.15 0.0982 889.88
303.15 0.1990 884.23
303.15 0.2966 878.11
303.15 0.3973 871.16
303.15 0.5001 863.29
303.15 0.6004 854.62
303.15 0.6995 844.76
303.15 0.7537 838.67
303.15 0.7936 833.81
303.15 0.8002 832.97
303.15 0.8419 827.45
303.15 0.8997 819.05
303.15 1.0000 802.14

Sources