Mixture of Propylene Glycol + 1-Hexanol

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Propylene Glycol

Name
Propylene Glycol
InChI
InChI=1S/C3H8O2/c1-3(5)2-4/h3-5H,2H2,1H3
InChI Key
DNIAPMSPPWPWGF-UHFFFAOYSA-N
Formula
C3H8O2
SMILES
CC(O)CO
Mol. Weight (g/mol)
76.09
CAS
57-55-6

1-Hexanol

Name
1-Hexanol
InChI
InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3
InChI Key
ZSIAUFGUXNUGDI-UHFFFAOYSA-N
Formula
C6H14O
SMILES
CCCCCCO
Mol. Weight (g/mol)
102.17
CAS
111-27-3
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Datasets

  1. η - Viscosity, Pa*s (2)
  2. Excess molar enthalpy (molar enthalpy (2)
  3. ρl - Mass density, kg/m3 (4)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of 1-Hexanol (2) - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
0.0000 298.15 0.0454
0.0000 303.15 0.0340
0.0000 308.15 0.0263
0.0771 298.15 0.0333
0.0771 303.15 0.0243
0.0771 308.15 0.0201
0.1213 298.15 0.0284
0.1213 303.15 0.0208
0.1213 308.15 0.0173
0.2425 298.15 0.0186
0.2425 303.15 0.0139
0.2425 308.15 0.0120
0.3311 298.15 0.0144
0.3311 303.15 0.0113
0.3311 308.15 0.0096
0.5225 298.15 0.0095
0.5225 303.15 0.0081
0.5225 308.15 0.0064
0.5377 298.15 0.0091
0.5377 303.15 0.0078
0.5377 308.15 0.0063
0.6309 298.15 0.0076
0.6309 303.15 0.0067
0.6309 308.15 0.0053
0.7444 298.15 0.0063
0.7444 303.15 0.0052
0.7444 308.15 0.0045
0.8611 298.15 0.0053
0.8611 303.15 0.0046
0.8611 308.15 0.0039
1.0000 298.15 0.0046
1.0000 303.15 0.0040
1.0000 308.15 0.0035

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of 1-Hexanol (2) - Liquid Temperature, K - Liquid Viscosity, Pa*s - Liquid
0.0000 298.15 0.0454
0.0000 303.15 0.0340
0.0000 308.15 0.0263
0.0771 298.15 0.0333
0.0771 303.15 0.0243
0.0771 308.15 0.0201
0.1213 298.15 0.0284
0.1213 303.15 0.0208
0.1213 308.15 0.0173
0.2425 298.15 0.0186
0.2425 303.15 0.0139
0.2425 308.15 0.0120
0.3311 298.15 0.0144
0.3311 303.15 0.0113
0.3311 308.15 0.0096
0.5225 298.15 0.0095
0.5225 303.15 0.0081
0.5225 308.15 0.0064
0.5377 298.15 0.0091
0.5377 303.15 0.0078
0.5377 308.15 0.0063
0.6309 298.15 0.0076
0.6309 303.15 0.0067
0.6309 308.15 0.0053
0.7444 298.15 0.0063
0.7444 303.15 0.0052
0.7444 308.15 0.0045
0.8611 298.15 0.0053
0.8611 303.15 0.0046
0.8611 308.15 0.0039
1.0000 298.15 0.0046
1.0000 303.15 0.0040
1.0000 308.15 0.0035

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Propylene Glycol (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0905 0.3487
0.1929 0.5773
0.2872 0.6911
0.3828 0.7465
0.4778 0.7564
0.5711 0.7235
0.6718 0.6564
0.7021 0.6117
0.7996 0.4848
0.9040 0.2816

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of Propylene Glycol (1) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0905 0.3487
0.1929 0.5773
0.2872 0.6911
0.3828 0.7465
0.4778 0.7564
0.5711 0.7235
0.6718 0.6564
0.7021 0.6117
0.7996 0.4848
0.9040 0.2816

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propylene Glycol (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 818.749
293.15 0.1014 831.496
293.15 0.1998 845.231
293.15 0.2999 860.667
293.15 0.4003 877.818
293.15 0.4939 895.533
293.15 0.5996 917.945
293.15 0.6965 941.028
293.15 0.7989 968.795
293.15 0.9005 1000.458
293.15 1.0000 1036.209
298.15 0.0000 815.188
298.15 0.1014 827.881
298.15 0.1998 841.574
298.15 0.2999 856.979
298.15 0.4003 874.105
298.15 0.4939 891.801
298.15 0.5996 914.203
298.15 0.6965 937.285
298.15 0.7989 965.064
298.15 0.9005 996.753
298.15 1.0000 1032.548
303.15 0.0000 811.6
303.15 0.1014 824.235
303.15 0.1998 837.887
303.15 0.2999 853.262
303.15 0.4003 870.363
303.15 0.4939 888.041
303.15 0.5996 910.432
303.15 0.6965 933.51
303.15 0.7989 961.302
303.15 0.9005 993.003
303.15 1.0000 1028.837
308.15 0.0000 807.984
308.15 0.1014 820.566
308.15 0.1998 834.178
308.15 0.2999 849.521
308.15 0.4003 866.596
308.15 0.4939 884.256
308.15 0.5996 906.63
308.15 0.6965 929.702
308.15 0.7989 957.503
308.15 0.9005 989.222
308.15 1.0000 1025.088
313.15 0.0000 804.339
313.15 0.1014 816.869
313.15 0.1998 830.44
313.15 0.2999 845.751
313.15 0.4003 862.8
313.15 0.4939 880.441
313.15 0.5996 902.801
313.15 0.6965 925.868
313.15 0.7989 953.677
313.15 0.9005 985.406
313.15 1.0000 1021.309
318.15 0.0000 800.657
318.15 0.1014 813.142
318.15 0.1998 826.676
318.15 0.2999 841.952
318.15 0.4003 858.977
318.15 0.4939 876.599
318.15 0.5996 898.941
318.15 0.6965 922.002
318.15 0.7989 949.81
318.15 0.9005 981.555
318.15 1.0000 1017.488

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of 1-Hexanol (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0000 298.15 1033.1
0.0000 303.15 1029.9
0.0000 308.15 1025.4
0.0771 298.15 1004.5
0.0771 303.15 1000.9
0.0771 308.15 996.1
0.1213 298.15 989.9
0.1213 303.15 986.2
0.1213 308.15 981.6
0.2425 298.15 953.6
0.2425 303.15 949.9
0.2425 308.15 945.8
0.3311 298.15 930.7
0.3311 303.15 927.0
0.3311 308.15 923.1
0.5225 298.15 888.7
0.5225 303.15 884.9
0.5225 308.15 881.3
0.5377 298.15 885.7
0.5377 303.15 881.9
0.5377 308.15 878.2
0.6309 298.15 868.9
0.6309 303.15 865.1
0.6309 308.15 861.5
0.7444 298.15 850.3
0.7444 303.15 846.4
0.7444 308.15 842.9
0.8611 298.15 833.3
0.8611 303.15 829.4
0.8611 308.15 826.0
1.0000 298.15 815.4
1.0000 303.15 811.5
1.0000 308.15 808.3

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Propylene Glycol (1) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0000 818.749
293.15 0.1014 831.496
293.15 0.1998 845.231
293.15 0.2999 860.667
293.15 0.4003 877.818
293.15 0.4939 895.533
293.15 0.5996 917.945
293.15 0.6965 941.028
293.15 0.7989 968.795
293.15 0.9005 1000.458
293.15 1.0000 1036.209
298.15 0.0000 815.188
298.15 0.1014 827.881
298.15 0.1998 841.574
298.15 0.2999 856.979
298.15 0.4003 874.105
298.15 0.4939 891.801
298.15 0.5996 914.203
298.15 0.6965 937.285
298.15 0.7989 965.064
298.15 0.9005 996.753
298.15 1.0000 1032.548
303.15 0.0000 811.6
303.15 0.1014 824.235
303.15 0.1998 837.887
303.15 0.2999 853.262
303.15 0.4003 870.363
303.15 0.4939 888.041
303.15 0.5996 910.432
303.15 0.6965 933.51
303.15 0.7989 961.302
303.15 0.9005 993.003
303.15 1.0000 1028.837
308.15 0.0000 807.984
308.15 0.1014 820.566
308.15 0.1998 834.178
308.15 0.2999 849.521
308.15 0.4003 866.596
308.15 0.4939 884.256
308.15 0.5996 906.63
308.15 0.6965 929.702
308.15 0.7989 957.503
308.15 0.9005 989.222
308.15 1.0000 1025.088
313.15 0.0000 804.339
313.15 0.1014 816.869
313.15 0.1998 830.44
313.15 0.2999 845.751
313.15 0.4003 862.8
313.15 0.4939 880.441
313.15 0.5996 902.801
313.15 0.6965 925.868
313.15 0.7989 953.677
313.15 0.9005 985.406
313.15 1.0000 1021.309
318.15 0.0000 800.657
318.15 0.1014 813.142
318.15 0.1998 826.676
318.15 0.2999 841.952
318.15 0.4003 858.977
318.15 0.4939 876.599
318.15 0.5996 898.941
318.15 0.6965 922.002
318.15 0.7989 949.81
318.15 0.9005 981.555
318.15 1.0000 1017.488

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Mole fraction of 1-Hexanol (2) - Liquid Temperature, K - Liquid Mass density, kg/m3 - Liquid
0.0000 298.15 1033.1
0.0000 303.15 1029.9
0.0000 308.15 1025.4
0.0771 298.15 1004.5
0.0771 303.15 1000.9
0.0771 308.15 996.1
0.1213 298.15 989.9
0.1213 303.15 986.2
0.1213 308.15 981.6
0.2425 298.15 953.6
0.2425 303.15 949.9
0.2425 308.15 945.8
0.3311 298.15 930.7
0.3311 303.15 927.0
0.3311 308.15 923.1
0.5225 298.15 888.7
0.5225 303.15 884.9
0.5225 308.15 881.3
0.5377 298.15 885.7
0.5377 303.15 881.9
0.5377 308.15 878.2
0.6309 298.15 868.9
0.6309 303.15 865.1
0.6309 308.15 861.5
0.7444 298.15 850.3
0.7444 303.15 846.4
0.7444 308.15 842.9
0.8611 298.15 833.3
0.8611 303.15 829.4
0.8611 308.15 826.0
1.0000 298.15 815.4
1.0000 303.15 811.5
1.0000 308.15 808.3

Sources