Mixture of Decane + Eucalyptol

Datasets

1. C_p,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
2. η - Viscosity, Pa*s (2)
3. ρ_l - Mass density, kg/m3 (2)
4. c_sound,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	305.94
278.15	0.1066	299.16
278.15	0.2007	293.50
278.15	0.2965	287.99
278.15	0.4063	282.04
278.15	0.5005	277.25
278.15	0.5959	272.59
278.15	0.7007	267.96
278.15	0.7989	263.81
278.15	0.8956	259.87
278.15	1.0000	256.14
298.15	0.0000	314.40
298.15	0.1066	308.32
298.15	0.2007	303.12
298.15	0.2965	298.17
298.15	0.4063	292.62
298.15	0.5005	288.12
298.15	0.5959	283.78
298.15	0.7007	279.20
298.15	0.7989	275.24
298.15	0.8956	271.44
298.15	1.0000	267.69
318.15	0.0000	323.94
318.15	0.1066	318.26
318.15	0.2007	313.35
318.15	0.2965	308.63
318.15	0.4063	303.32
318.15	0.5005	298.96
318.15	0.5959	294.70
318.15	0.7007	290.19
318.15	0.7989	286.17
318.15	0.8956	282.47
318.15	1.0000	278.65
338.15	0.0000	334.32
338.15	0.1066	328.92
338.15	0.2007	324.19
338.15	0.2965	319.65
338.15	0.4063	314.60
338.15	0.5005	310.38
338.15	0.5959	306.21
338.15	0.7007	301.78
338.15	0.7989	297.82
338.15	0.8956	294.23
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	305.94
278.15	0.1066	299.16
278.15	0.2007	293.50
278.15	0.2965	287.99
278.15	0.4063	282.04
278.15	0.5005	277.25
278.15	0.5959	272.59
278.15	0.7007	267.96
278.15	0.7989	263.81
278.15	0.8956	259.87
278.15	1.0000	256.14
298.15	0.0000	314.40
298.15	0.1066	308.32
298.15	0.2007	303.12
298.15	0.2965	298.17
298.15	0.4063	292.62
298.15	0.5005	288.12
298.15	0.5959	283.78
298.15	0.7007	279.20
298.15	0.7989	275.24
298.15	0.8956	271.44
298.15	1.0000	267.69
318.15	0.0000	323.94
318.15	0.1066	318.26
318.15	0.2007	313.35
318.15	0.2965	308.63
318.15	0.4063	303.32
318.15	0.5005	298.96
318.15	0.5959	294.70
318.15	0.7007	290.19
318.15	0.7989	286.17
318.15	0.8956	282.47
318.15	1.0000	278.65
338.15	0.0000	334.32
338.15	0.1066	328.92
338.15	0.2007	324.19
338.15	0.2965	319.65
338.15	0.4063	314.60
338.15	0.5005	310.38
338.15	0.5959	306.21
338.15	0.7007	301.78
338.15	0.7989	297.82
338.15	0.8956	294.23
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	0.0012
278.15	0.1066	0.0013
278.15	0.2007	0.0014
278.15	0.2965	0.0015
278.15	0.4063	0.0017
278.15	0.5005	0.0018
278.15	0.5959	0.0021
278.15	0.7007	0.0024
278.15	0.7989	0.0029
278.15	0.8956	0.0034
278.15	1.0000	0.0042
298.15	0.0000	0.0009
298.15	0.1066	0.0009
298.15	0.2007	0.0010
298.15	0.2965	0.0011
298.15	0.4063	0.0012
298.15	0.5005	0.0013
298.15	0.5959	0.0014
298.15	0.7007	0.0016
298.15	0.7989	0.0019
298.15	0.8956	0.0022
298.15	1.0000	0.0026
318.15	0.0000	0.0007
318.15	0.1066	0.0007
318.15	0.2007	0.0008
318.15	0.2965	0.0008
318.15	0.4063	0.0009
318.15	0.5005	0.0009
318.15	0.5959	0.0010
318.15	0.7007	0.0011
318.15	0.7989	0.0013
318.15	0.8956	0.0015
318.15	1.0000	0.0017
338.15	0.0000	0.0005
338.15	0.1066	0.0006
338.15	0.2007	0.0006
338.15	0.2965	0.0006
338.15	0.4063	0.0007
338.15	0.5005	0.0007
338.15	0.5959	0.0008
338.15	0.7007	0.0009
338.15	0.7989	0.0010
338.15	0.8956	0.0011
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	0.0012
278.15	0.1066	0.0013
278.15	0.2007	0.0014
278.15	0.2965	0.0015
278.15	0.4063	0.0017
278.15	0.5005	0.0018
278.15	0.5959	0.0021
278.15	0.7007	0.0024
278.15	0.7989	0.0029
278.15	0.8956	0.0034
278.15	1.0000	0.0042
298.15	0.0000	0.0009
298.15	0.1066	0.0009
298.15	0.2007	0.0010
298.15	0.2965	0.0011
298.15	0.4063	0.0012
298.15	0.5005	0.0013
298.15	0.5959	0.0014
298.15	0.7007	0.0016
298.15	0.7989	0.0019
298.15	0.8956	0.0022
298.15	1.0000	0.0026
318.15	0.0000	0.0007
318.15	0.1066	0.0007
318.15	0.2007	0.0008
318.15	0.2965	0.0008
318.15	0.4063	0.0009
318.15	0.5005	0.0009
318.15	0.5959	0.0010
318.15	0.7007	0.0011
318.15	0.7989	0.0013
318.15	0.8956	0.0015
318.15	1.0000	0.0017
338.15	0.0000	0.0005
338.15	0.1066	0.0006
338.15	0.2007	0.0006
338.15	0.2965	0.0006
338.15	0.4063	0.0007
338.15	0.5005	0.0007
338.15	0.5959	0.0008
338.15	0.7007	0.0009
338.15	0.7989	0.0010
338.15	0.8956	0.0011
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	741.18
278.15	0.1066	758.86
278.15	0.2007	775.04
278.15	0.2965	792.05
278.15	0.4063	812.26
278.15	0.5005	830.26
278.15	0.5959	849.15
278.15	0.7007	870.67
278.15	0.7989	891.66
278.15	0.8956	913.12
278.15	1.0000	937.25
298.15	0.0000	726.11
298.15	0.1066	743.66
298.15	0.2007	759.71
298.15	0.2965	776.57
298.15	0.4063	796.58
298.15	0.5005	814.39
298.15	0.5959	833.07
298.15	0.7007	854.34
298.15	0.7989	875.07
298.15	0.8956	896.24
298.15	1.0000	920.04
318.15	0.0000	710.89
318.15	0.1066	728.29
318.15	0.2007	744.21
318.15	0.2965	760.92
318.15	0.4063	780.75
318.15	0.5005	798.4
318.15	0.5959	816.88
318.15	0.7007	837.92
318.15	0.7989	858.42
318.15	0.8956	879.33
318.15	1.0000	902.84
338.15	0.0000	695.42
338.15	0.1066	712.7
338.15	0.2007	728.49
338.15	0.2965	745.06
338.15	0.4063	764.73
338.15	0.5005	782.2
338.15	0.5959	800.51
338.15	0.7007	821.36
338.15	0.7989	841.62
338.15	0.8956	862.32
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	741.18
278.15	0.1066	758.86
278.15	0.2007	775.04
278.15	0.2965	792.05
278.15	0.4063	812.26
278.15	0.5005	830.26
278.15	0.5959	849.15
278.15	0.7007	870.67
278.15	0.7989	891.66
278.15	0.8956	913.12
278.15	1.0000	937.25
298.15	0.0000	726.11
298.15	0.1066	743.66
298.15	0.2007	759.71
298.15	0.2965	776.57
298.15	0.4063	796.58
298.15	0.5005	814.39
298.15	0.5959	833.07
298.15	0.7007	854.34
298.15	0.7989	875.07
298.15	0.8956	896.24
298.15	1.0000	920.04
318.15	0.0000	710.89
318.15	0.1066	728.29
318.15	0.2007	744.21
318.15	0.2965	760.92
318.15	0.4063	780.75
318.15	0.5005	798.4
318.15	0.5959	816.88
318.15	0.7007	837.92
318.15	0.7989	858.42
318.15	0.8956	879.33
318.15	1.0000	902.84
338.15	0.0000	695.42
338.15	0.1066	712.7
338.15	0.2007	728.49
338.15	0.2965	745.06
338.15	0.4063	764.73
338.15	0.5005	782.2
338.15	0.5959	800.51
338.15	0.7007	821.36
338.15	0.7989	841.62
338.15	0.8956	862.32
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	1315.03
278.15	0.1066	1315.48
278.15	0.2007	1316.57
278.15	0.2965	1318.25
278.15	0.4063	1321.18
278.15	0.5005	1324.7
278.15	0.5959	1328.99
278.15	0.7007	1334.99
278.15	0.7989	1341.75
278.15	0.8956	1349.46
278.15	1.0000	1359.61
298.15	0.0000	1234.74
298.15	0.1066	1235.6
298.15	0.2007	1237.05
298.15	0.2965	1239.08
298.15	0.4063	1242.26
298.15	0.5005	1245.7
298.15	0.5959	1249.97
298.15	0.7007	1255.63
298.15	0.7989	1261.91
298.15	0.8956	1269.3
298.15	1.0000	1278.39
318.15	0.0000	1156.56
318.15	0.1066	1157.5
318.15	0.2007	1159.52
318.15	0.2965	1162.02
318.15	0.4063	1165.49
318.15	0.5005	1169.11
318.15	0.5959	1173.38
318.15	0.7007	1178.99
318.15	0.7989	1184.93
318.15	0.8956	1192.3
318.15	1.0000	1200.99
338.15	0.0000	1080.51
338.15	0.1066	1081.85
338.15	0.2007	1083.94
338.15	0.2965	1087.11
338.15	0.4063	1091.2
338.15	0.5005	1094.9
338.15	0.5959	1099.34
338.15	0.7007	1105.28
338.15	0.7989	1111.29
338.15	0.8956	1118.52
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	1315.03
278.15	0.1066	1315.48
278.15	0.2007	1316.57
278.15	0.2965	1318.25
278.15	0.4063	1321.18
278.15	0.5005	1324.7
278.15	0.5959	1328.99
278.15	0.7007	1334.99
278.15	0.7989	1341.75
278.15	0.8956	1349.46
278.15	1.0000	1359.61
298.15	0.0000	1234.74
298.15	0.1066	1235.6
298.15	0.2007	1237.05
298.15	0.2965	1239.08
298.15	0.4063	1242.26
298.15	0.5005	1245.7
298.15	0.5959	1249.97
298.15	0.7007	1255.63
298.15	0.7989	1261.91
298.15	0.8956	1269.3
298.15	1.0000	1278.39
318.15	0.0000	1156.56
318.15	0.1066	1157.5
318.15	0.2007	1159.52
318.15	0.2965	1162.02
318.15	0.4063	1165.49
318.15	0.5005	1169.11
318.15	0.5959	1173.38
318.15	0.7007	1178.99
318.15	0.7989	1184.93
318.15	0.8956	1192.3
318.15	1.0000	1200.99
338.15	0.0000	1080.51
338.15	0.1066	1081.85
338.15	0.2007	1083.94
338.15	0.2965	1087.11
338.15	0.4063	1091.2
338.15	0.5005	1094.9
338.15	0.5959	1099.34
338.15	0.7007	1105.28
338.15	0.7989	1111.29
338.15	0.8956	1118.52
338.15	1.0000	1126.65

Sources

• Preferential solvation and mixing behaviour of the essential oil 1,8-cineole with short-chain hydrocarbons