Mixture of Octane + Eucalyptol

Excel

Octane

Name
Octane
InChI
InChI=1S/C8H18/c1-3-5-7-8-6-4-2/h3-8H2,1-2H3
InChI Key
TVMXDCGIABBOFY-UHFFFAOYSA-N
Formula
C8H18
SMILES
CCCCCCCC
Mol. Weight (g/mol)
114.23
CAS
111-65-9

Eucalyptol

Name
Eucalyptol
InChI
InChI=1S/C10H18O/c1-9(2)8-4-6-10(3,11-9)7-5-8/h8H,4-7H2,1-3H3
InChI Key
WEEGYLXZBRQIMU-UHFFFAOYSA-N
Formula
C10H18O
SMILES
CC12CCC(CC1)C(C)(C)O2
Mol. Weight (g/mol)
154.25
CAS
470-82-6
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Datasets

  1. Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
  2. η - Viscosity, Pa*s (2)
  3. ρl - Mass density, kg/m3 (2)
  4. csound,fluid - Speed of Sound, m/s (2)

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Eucalyptol (2) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
278.15 0.0000 246.17
278.15 0.1046 246.20
278.15 0.1990 246.45
278.15 0.2987 246.89
278.15 0.4008 247.59
278.15 0.4955 248.46
278.15 0.5939 249.62
278.15 0.6971 250.95
278.15 0.7985 252.64
278.15 0.8939 254.30
278.15 1.0000 256.14
298.15 0.0000 253.89
298.15 0.1046 254.53
298.15 0.1990 255.32
298.15 0.2987 256.22
298.15 0.4008 257.36
298.15 0.4955 258.59
298.15 0.5939 260.07
298.15 0.6971 261.75
298.15 0.7985 263.66
298.15 0.8939 265.57
298.15 1.0000 267.69
318.15 0.0000 262.16
318.15 0.1046 263.19
318.15 0.1990 264.31
318.15 0.2987 265.53
318.15 0.4008 267.00
318.15 0.4955 268.51
318.15 0.5939 270.26
318.15 0.6971 272.14
318.15 0.7985 274.24
318.15 0.8939 276.39
318.15 1.0000 278.65
338.15 0.0000 270.96
338.15 0.1046 272.35
338.15 0.1990 273.81
338.15 0.2987 275.37
338.15 0.4008 277.18
338.15 0.4955 278.93
338.15 0.5939 280.96
338.15 0.6971 283.13
338.15 0.7985 285.45
338.15 0.8939 287.81
338.15 1.0000 290.33

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Eucalyptol (2) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
278.15 0.0000 246.17
278.15 0.1046 246.20
278.15 0.1990 246.45
278.15 0.2987 246.89
278.15 0.4008 247.59
278.15 0.4955 248.46
278.15 0.5939 249.62
278.15 0.6971 250.95
278.15 0.7985 252.64
278.15 0.8939 254.30
278.15 1.0000 256.14
298.15 0.0000 253.89
298.15 0.1046 254.53
298.15 0.1990 255.32
298.15 0.2987 256.22
298.15 0.4008 257.36
298.15 0.4955 258.59
298.15 0.5939 260.07
298.15 0.6971 261.75
298.15 0.7985 263.66
298.15 0.8939 265.57
298.15 1.0000 267.69
318.15 0.0000 262.16
318.15 0.1046 263.19
318.15 0.1990 264.31
318.15 0.2987 265.53
318.15 0.4008 267.00
318.15 0.4955 268.51
318.15 0.5939 270.26
318.15 0.6971 272.14
318.15 0.7985 274.24
318.15 0.8939 276.39
318.15 1.0000 278.65
338.15 0.0000 270.96
338.15 0.1046 272.35
338.15 0.1990 273.81
338.15 0.2987 275.37
338.15 0.4008 277.18
338.15 0.4955 278.93
338.15 0.5939 280.96
338.15 0.6971 283.13
338.15 0.7985 285.45
338.15 0.8939 287.81
338.15 1.0000 290.33

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Eucalyptol (2) - Liquid Viscosity, Pa*s - Liquid
278.15 0.0000 0.0007
278.15 0.1046 0.0008
278.15 0.1990 0.0009
278.15 0.2987 0.0010
278.15 0.4008 0.0012
278.15 0.4955 0.0014
278.15 0.5939 0.0016
278.15 0.6971 0.0020
278.15 0.7985 0.0025
278.15 0.8939 0.0031
278.15 1.0000 0.0042
298.15 0.0000 0.0005
298.15 0.1046 0.0006
298.15 0.1990 0.0007
298.15 0.2987 0.0008
298.15 0.4008 0.0009
298.15 0.4955 0.0010
298.15 0.5939 0.0011
298.15 0.6971 0.0014
298.15 0.7985 0.0016
298.15 0.8939 0.0020
298.15 1.0000 0.0026
318.15 0.0000 0.0004
318.15 0.1046 0.0005
318.15 0.1990 0.0005
318.15 0.2987 0.0006
318.15 0.4008 0.0007
318.15 0.4955 0.0007
318.15 0.5939 0.0008
318.15 0.6971 0.0010
318.15 0.7985 0.0012
318.15 0.8939 0.0014
318.15 1.0000 0.0017
338.15 0.0000 0.0004
338.15 0.1046 0.0004
338.15 0.1990 0.0004
338.15 0.2987 0.0005
338.15 0.4008 0.0005
338.15 0.4955 0.0006
338.15 0.5939 0.0007
338.15 0.6971 0.0008
338.15 0.7985 0.0009
338.15 0.8939 0.0010
338.15 1.0000 0.0013

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Eucalyptol (2) - Liquid Viscosity, Pa*s - Liquid
278.15 0.0000 0.0007
278.15 0.1046 0.0008
278.15 0.1990 0.0009
278.15 0.2987 0.0010
278.15 0.4008 0.0012
278.15 0.4955 0.0014
278.15 0.5939 0.0016
278.15 0.6971 0.0020
278.15 0.7985 0.0025
278.15 0.8939 0.0031
278.15 1.0000 0.0042
298.15 0.0000 0.0005
298.15 0.1046 0.0006
298.15 0.1990 0.0007
298.15 0.2987 0.0008
298.15 0.4008 0.0009
298.15 0.4955 0.0010
298.15 0.5939 0.0011
298.15 0.6971 0.0014
298.15 0.7985 0.0016
298.15 0.8939 0.0020
298.15 1.0000 0.0026
318.15 0.0000 0.0004
318.15 0.1046 0.0005
318.15 0.1990 0.0005
318.15 0.2987 0.0006
318.15 0.4008 0.0007
318.15 0.4955 0.0007
318.15 0.5939 0.0008
318.15 0.6971 0.0010
318.15 0.7985 0.0012
318.15 0.8939 0.0014
318.15 1.0000 0.0017
338.15 0.0000 0.0004
338.15 0.1046 0.0004
338.15 0.1990 0.0004
338.15 0.2987 0.0005
338.15 0.4008 0.0005
338.15 0.4955 0.0006
338.15 0.5939 0.0007
338.15 0.6971 0.0008
338.15 0.7985 0.0009
338.15 0.8939 0.0010
338.15 1.0000 0.0013

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Eucalyptol (2) - Liquid Mass density, kg/m3 - Liquid
278.15 0.0000 714.55
278.15 0.1046 738.47
278.15 0.1990 759.76
278.15 0.2987 782.16
278.15 0.4008 805.03
278.15 0.4955 826.13
278.15 0.5939 847.98
278.15 0.6971 870.82
278.15 0.7985 893.16
278.15 0.8939 914.06
278.15 1.0000 937.25
298.15 0.0000 698.51
298.15 0.1046 722.35
298.15 0.1990 743.56
298.15 0.2987 765.86
298.15 0.4008 788.62
298.15 0.4955 809.62
298.15 0.5939 831.35
298.15 0.6971 854.05
298.15 0.7985 876.24
298.15 0.8939 897.03
298.15 1.0000 920.04
318.15 0.0000 682.19
318.15 0.1046 705.93
318.15 0.1990 727.08
318.15 0.2987 749.32
318.15 0.4008 772.01
318.15 0.4955 792.93
318.15 0.5939 814.56
318.15 0.6971 837.17
318.15 0.7985 859.26
318.15 0.8939 879.92
318.15 1.0000 902.84
338.15 0.0000 665.43
338.15 0.1046 689.16
338.15 0.1990 710.27
338.15 0.2987 732.46
338.15 0.4008 755.1
338.15 0.4955 775.96
338.15 0.5939 797.55
338.15 0.6971 820.1
338.15 0.7985 842.12
338.15 0.8939 862.72
338.15 1.0000 885.57

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Eucalyptol (2) - Liquid Mass density, kg/m3 - Liquid
278.15 0.0000 714.55
278.15 0.1046 738.47
278.15 0.1990 759.76
278.15 0.2987 782.16
278.15 0.4008 805.03
278.15 0.4955 826.13
278.15 0.5939 847.98
278.15 0.6971 870.82
278.15 0.7985 893.16
278.15 0.8939 914.06
278.15 1.0000 937.25
298.15 0.0000 698.51
298.15 0.1046 722.35
298.15 0.1990 743.56
298.15 0.2987 765.86
298.15 0.4008 788.62
298.15 0.4955 809.62
298.15 0.5939 831.35
298.15 0.6971 854.05
298.15 0.7985 876.24
298.15 0.8939 897.03
298.15 1.0000 920.04
318.15 0.0000 682.19
318.15 0.1046 705.93
318.15 0.1990 727.08
318.15 0.2987 749.32
318.15 0.4008 772.01
318.15 0.4955 792.93
318.15 0.5939 814.56
318.15 0.6971 837.17
318.15 0.7985 859.26
318.15 0.8939 879.92
318.15 1.0000 902.84
338.15 0.0000 665.43
338.15 0.1046 689.16
338.15 0.1990 710.27
338.15 0.2987 732.46
338.15 0.4008 755.1
338.15 0.4955 775.96
338.15 0.5939 797.55
338.15 0.6971 820.1
338.15 0.7985 842.12
338.15 0.8939 862.72
338.15 1.0000 885.57

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Eucalyptol (2) - Liquid Speed of sound, m/s - Liquid
278.15 0.0000 1256.65
278.15 0.1046 1263.76
278.15 0.1990 1270.81
278.15 0.2987 1279.14
278.15 0.4008 1288.48
278.15 0.4955 1297.82
278.15 0.5939 1308.36
278.15 0.6971 1320.12
278.15 0.7985 1332.5
278.15 0.8939 1344.94
278.15 1.0000 1359.61
298.15 0.0000 1172.69
298.15 0.1046 1180.9
298.15 0.1990 1188.55
298.15 0.2987 1197.5
298.15 0.4008 1207.27
298.15 0.4955 1216.87
298.15 0.5939 1227.66
298.15 0.6971 1239.84
298.15 0.7985 1252.37
298.15 0.8939 1264.88
298.15 1.0000 1278.39
318.15 0.0000 1090.71
318.15 0.1046 1099.65
318.15 0.1990 1108.14
318.15 0.2987 1117.88
318.15 0.4008 1128.3
318.15 0.4955 1138.35
318.15 0.5939 1149.5
318.15 0.6971 1162.28
318.15 0.7985 1175.57
318.15 0.8939 1188.32
318.15 1.0000 1200.99
338.15 0.0000 1010.72
338.15 0.1046 1020.2
338.15 0.1990 1029.62
338.15 0.2987 1040.27
338.15 0.4008 1051.6
338.15 0.4955 1062.26
338.15 0.5939 1073.84
338.15 0.6971 1087.43
338.15 0.7985 1101.37
338.15 0.8939 1114.47
338.15 1.0000 1126.65

Speed of sound, m/s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Eucalyptol (2) - Liquid Speed of sound, m/s - Liquid
278.15 0.0000 1256.65
278.15 0.1046 1263.76
278.15 0.1990 1270.81
278.15 0.2987 1279.14
278.15 0.4008 1288.48
278.15 0.4955 1297.82
278.15 0.5939 1308.36
278.15 0.6971 1320.12
278.15 0.7985 1332.5
278.15 0.8939 1344.94
278.15 1.0000 1359.61
298.15 0.0000 1172.69
298.15 0.1046 1180.9
298.15 0.1990 1188.55
298.15 0.2987 1197.5
298.15 0.4008 1207.27
298.15 0.4955 1216.87
298.15 0.5939 1227.66
298.15 0.6971 1239.84
298.15 0.7985 1252.37
298.15 0.8939 1264.88
298.15 1.0000 1278.39
318.15 0.0000 1090.71
318.15 0.1046 1099.65
318.15 0.1990 1108.14
318.15 0.2987 1117.88
318.15 0.4008 1128.3
318.15 0.4955 1138.35
318.15 0.5939 1149.5
318.15 0.6971 1162.28
318.15 0.7985 1175.57
318.15 0.8939 1188.32
318.15 1.0000 1200.99
338.15 0.0000 1010.72
338.15 0.1046 1020.2
338.15 0.1990 1029.62
338.15 0.2987 1040.27
338.15 0.4008 1051.6
338.15 0.4955 1062.26
338.15 0.5939 1073.84
338.15 0.6971 1087.43
338.15 0.7985 1101.37
338.15 0.8939 1114.47
338.15 1.0000 1126.65

Sources