Mixture of Cyclohexanemethanol + Dodecane

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)
3. T_fus - Solid-liquid equilibrium temperature, K (2)

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dodecane (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.1014	0.0184
293.15	0.1991	0.0098
293.15	0.2990	0.0062
293.15	0.3997	0.0043
293.15	0.4992	0.0032
293.15	0.6005	0.0025
293.15	0.7008	0.0021
293.15	0.7986	0.0018
293.15	0.8996	0.0016
298.15	0.1014	0.0146
298.15	0.1991	0.0080
298.15	0.2990	0.0052
298.15	0.3997	0.0037
298.15	0.4992	0.0028
298.15	0.6005	0.0023
298.15	0.7008	0.0019
298.15	0.7986	0.0016
298.15	0.8996	0.0014
303.15	0.1014	0.0117
303.15	0.1991	0.0066
303.15	0.2990	0.0044
303.15	0.3997	0.0032
303.15	0.4992	0.0025
303.15	0.6005	0.0020
303.15	0.7008	0.0017
303.15	0.7986	0.0015
303.15	0.8996	0.0013
308.15	0.1014	0.0096
308.15	0.1991	0.0055
308.15	0.2990	0.0038
308.15	0.3997	0.0028
308.15	0.4992	0.0022
308.15	0.6005	0.0018
308.15	0.7008	0.0015
308.15	0.7986	0.0014
308.15	0.8996	0.0012
313.15	0.1014	0.0079
313.15	0.1991	0.0047
313.15	0.2990	0.0033
313.15	0.3997	0.0025
313.15	0.4992	0.0020
313.15	0.6005	0.0016
313.15	0.7008	0.0014
313.15	0.7986	0.0012
313.15	0.8996	0.0011
318.15	0.1014	0.0066
318.15	0.1991	0.0040
318.15	0.2990	0.0029
318.15	0.3997	0.0022
318.15	0.4992	0.0018
318.15	0.6005	0.0015
318.15	0.7008	0.0013
318.15	0.7986	0.0011
318.15	0.8996	0.0010
323.15	0.1014	0.0055
323.15	0.1991	0.0034
323.15	0.2990	0.0025
323.15	0.3997	0.0019
323.15	0.4992	0.0016
323.15	0.6005	0.0013
323.15	0.7008	0.0012
323.15	0.7986	0.0010
323.15	0.8996	0.0010
328.15	0.1014	0.0047
328.15	0.1991	0.0030
328.15	0.2990	0.0022
328.15	0.3997	0.0017
328.15	0.4992	0.0014
328.15	0.6005	0.0012
328.15	0.7008	0.0011
328.15	0.7986	0.0010
328.15	0.8996	0.0009
333.15	0.1014	0.0040
333.15	0.1991	0.0026
333.15	0.2990	0.0020
333.15	0.3997	0.0016
333.15	0.4992	0.0013
333.15	0.6005	0.0011
333.15	0.7008	0.0010
333.15	0.7986	0.0009
333.15	0.8996	0.0008

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dodecane (2) - Liquid	Viscosity, Pa*s - Liquid
293.15	0.1014	0.0184
293.15	0.1991	0.0098
293.15	0.2990	0.0062
293.15	0.3997	0.0043
293.15	0.4992	0.0032
293.15	0.6005	0.0025
293.15	0.7008	0.0021
293.15	0.7986	0.0018
293.15	0.8996	0.0016
298.15	0.1014	0.0146
298.15	0.1991	0.0080
298.15	0.2990	0.0052
298.15	0.3997	0.0037
298.15	0.4992	0.0028
298.15	0.6005	0.0023
298.15	0.7008	0.0019
298.15	0.7986	0.0016
298.15	0.8996	0.0014
303.15	0.1014	0.0117
303.15	0.1991	0.0066
303.15	0.2990	0.0044
303.15	0.3997	0.0032
303.15	0.4992	0.0025
303.15	0.6005	0.0020
303.15	0.7008	0.0017
303.15	0.7986	0.0015
303.15	0.8996	0.0013
308.15	0.1014	0.0096
308.15	0.1991	0.0055
308.15	0.2990	0.0038
308.15	0.3997	0.0028
308.15	0.4992	0.0022
308.15	0.6005	0.0018
308.15	0.7008	0.0015
308.15	0.7986	0.0014
308.15	0.8996	0.0012
313.15	0.1014	0.0079
313.15	0.1991	0.0047
313.15	0.2990	0.0033
313.15	0.3997	0.0025
313.15	0.4992	0.0020
313.15	0.6005	0.0016
313.15	0.7008	0.0014
313.15	0.7986	0.0012
313.15	0.8996	0.0011
318.15	0.1014	0.0066
318.15	0.1991	0.0040
318.15	0.2990	0.0029
318.15	0.3997	0.0022
318.15	0.4992	0.0018
318.15	0.6005	0.0015
318.15	0.7008	0.0013
318.15	0.7986	0.0011
318.15	0.8996	0.0010
323.15	0.1014	0.0055
323.15	0.1991	0.0034
323.15	0.2990	0.0025
323.15	0.3997	0.0019
323.15	0.4992	0.0016
323.15	0.6005	0.0013
323.15	0.7008	0.0012
323.15	0.7986	0.0010
323.15	0.8996	0.0010
328.15	0.1014	0.0047
328.15	0.1991	0.0030
328.15	0.2990	0.0022
328.15	0.3997	0.0017
328.15	0.4992	0.0014
328.15	0.6005	0.0012
328.15	0.7008	0.0011
328.15	0.7986	0.0010
328.15	0.8996	0.0009
333.15	0.1014	0.0040
333.15	0.1991	0.0026
333.15	0.2990	0.0020
333.15	0.3997	0.0016
333.15	0.4992	0.0013
333.15	0.6005	0.0011
333.15	0.7008	0.0010
333.15	0.7986	0.0009
333.15	0.8996	0.0008

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dodecane (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.1014	898.17
293.15	0.1991	872.04
293.15	0.2990	849.06
293.15	0.3997	828.81
293.15	0.4992	811.3
293.15	0.6005	795.57
293.15	0.7008	781.83
293.15	0.7986	769.9
293.15	0.8996	758.73
298.15	0.1014	894.59
298.15	0.1991	868.46
298.15	0.2990	845.44
298.15	0.3997	825.18
298.15	0.4992	807.71
298.15	0.6005	791.92
298.15	0.7008	778.16
298.15	0.7986	766.22
298.15	0.8996	755.05
303.15	0.1014	890.99
303.15	0.1991	864.86
303.15	0.2990	841.79
303.15	0.3997	821.5
303.15	0.4992	804.02
303.15	0.6005	788.23
303.15	0.7008	774.47
303.15	0.7986	762.53
303.15	0.8996	751.37
308.15	0.1014	887.35
308.15	0.1991	861.23
308.15	0.2990	838.08
308.15	0.3997	817.79
308.15	0.4992	800.32
308.15	0.6005	784.52
308.15	0.7008	770.76
308.15	0.7986	758.82
308.15	0.8996	747.67
313.15	0.1014	883.69
313.15	0.1991	857.57
313.15	0.2990	834.37
313.15	0.3997	814.07
313.15	0.4992	796.59
313.15	0.6005	780.79
313.15	0.7008	767.03
313.15	0.7986	755.09
313.15	0.8996	743.96
318.15	0.1014	879.99
318.15	0.1991	853.91
318.15	0.2990	830.77
318.15	0.3997	810.31
318.15	0.4992	792.83
318.15	0.6005	777.04
318.15	0.7008	763.28
318.15	0.7986	751.35
318.15	0.8996	740.24
323.15	0.1014	876.25
323.15	0.1991	850.16
323.15	0.2990	827.01
323.15	0.3997	806.53
323.15	0.4992	789.05
323.15	0.6005	773.26
323.15	0.7008	759.51
323.15	0.7986	747.58
323.15	0.8996	736.5
328.15	0.1014	872.47
328.15	0.1991	846.36
328.15	0.2990	823.2
328.15	0.3997	802.71
328.15	0.4992	785.24
328.15	0.6005	769.45
328.15	0.7008	755.71
328.15	0.7986	743.79
328.15	0.8996	732.74
333.15	0.1014	868.64
333.15	0.1991	842.52
333.15	0.2990	819.35
333.15	0.3997	798.87
333.15	0.4992	781.41
333.15	0.6005	765.62
333.15	0.7008	751.89
333.15	0.7986	739.98
333.15	0.8996	728.97

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Dodecane (2) - Liquid	Mass density, kg/m3 - Liquid
293.15	0.1014	898.17
293.15	0.1991	872.04
293.15	0.2990	849.06
293.15	0.3997	828.81
293.15	0.4992	811.3
293.15	0.6005	795.57
293.15	0.7008	781.83
293.15	0.7986	769.9
293.15	0.8996	758.73
298.15	0.1014	894.59
298.15	0.1991	868.46
298.15	0.2990	845.44
298.15	0.3997	825.18
298.15	0.4992	807.71
298.15	0.6005	791.92
298.15	0.7008	778.16
298.15	0.7986	766.22
298.15	0.8996	755.05
303.15	0.1014	890.99
303.15	0.1991	864.86
303.15	0.2990	841.79
303.15	0.3997	821.5
303.15	0.4992	804.02
303.15	0.6005	788.23
303.15	0.7008	774.47
303.15	0.7986	762.53
303.15	0.8996	751.37
308.15	0.1014	887.35
308.15	0.1991	861.23
308.15	0.2990	838.08
308.15	0.3997	817.79
308.15	0.4992	800.32
308.15	0.6005	784.52
308.15	0.7008	770.76
308.15	0.7986	758.82
308.15	0.8996	747.67
313.15	0.1014	883.69
313.15	0.1991	857.57
313.15	0.2990	834.37
313.15	0.3997	814.07
313.15	0.4992	796.59
313.15	0.6005	780.79
313.15	0.7008	767.03
313.15	0.7986	755.09
313.15	0.8996	743.96
318.15	0.1014	879.99
318.15	0.1991	853.91
318.15	0.2990	830.77
318.15	0.3997	810.31
318.15	0.4992	792.83
318.15	0.6005	777.04
318.15	0.7008	763.28
318.15	0.7986	751.35
318.15	0.8996	740.24
323.15	0.1014	876.25
323.15	0.1991	850.16
323.15	0.2990	827.01
323.15	0.3997	806.53
323.15	0.4992	789.05
323.15	0.6005	773.26
323.15	0.7008	759.51
323.15	0.7986	747.58
323.15	0.8996	736.5
328.15	0.1014	872.47
328.15	0.1991	846.36
328.15	0.2990	823.2
328.15	0.3997	802.71
328.15	0.4992	785.24
328.15	0.6005	769.45
328.15	0.7008	755.71
328.15	0.7986	743.79
328.15	0.8996	732.74
333.15	0.1014	868.64
333.15	0.1991	842.52
333.15	0.2990	819.35
333.15	0.3997	798.87
333.15	0.4992	781.41
333.15	0.6005	765.62
333.15	0.7008	751.89
333.15	0.7986	739.98
333.15	0.8996	728.97

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Dodecane (2) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.1014	256.05
0.1991	259.85
0.2990	261.65
0.3997	262.15
0.4992	262.55
0.6005	262.95
0.7008	263.15
0.7986	263.55
0.8996	264.15
1.0000	264.95

Solid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Mole fraction of Dodecane (2) - Liquid	Solid-liquid equilibrium temperature, K - Liquid
0.1014	256.05
0.1991	259.85
0.2990	261.65
0.3997	262.15
0.4992	262.55
0.6005	262.95
0.7008	263.15
0.7986	263.55
0.8996	264.15
1.0000	264.95

Sources

• Density, Viscosity, and Freezing Point for Four Binary Systems of n-Dodecane or Methylcyclohexane Mixed with 1-Heptanol or Cyclohexylmethanol