Mixture of Naphthalene, decahydro-, cis- + Naphthalene, decahydro-, trans- + Cyclohexane, methyl-

Datasets

1. η - Viscosity, Pa*s (2)
2. ρ_l - Mass density, kg/m3 (2)

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Solvent: Mole fraction = 0.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane, methyl- (3) - Liquid	Viscosity, Pa*s - Liquid
293.15	1.0000	0.0007
293.15	0.9004	0.0008
293.15	0.8002	0.0010
293.15	0.6995	0.0011
293.15	0.5995	0.0012
293.15	0.4998	0.0014
293.15	0.3997	0.0016
293.15	0.3002	0.0017
293.15	0.2006	0.0020
293.15	0.1003	0.0022
293.15	0.0000	0.0025
298.15	1.0000	0.0007
298.15	0.9004	0.0008
298.15	0.8002	0.0009
298.15	0.6995	0.0010
298.15	0.5995	0.0011
298.15	0.4998	0.0013
298.15	0.3997	0.0014
298.15	0.3002	0.0016
298.15	0.2006	0.0018
298.15	0.1003	0.0020
298.15	0.0000	0.0023
303.15	1.0000	0.0006
303.15	0.9004	0.0007
303.15	0.8002	0.0008
303.15	0.6995	0.0009
303.15	0.5995	0.0010
303.15	0.4998	0.0012
303.15	0.3997	0.0013
303.15	0.3002	0.0015
303.15	0.2006	0.0016
303.15	0.1003	0.0018
303.15	0.0000	0.0021
308.15	1.0000	0.0006
308.15	0.9004	0.0007
308.15	0.8002	0.0008
308.15	0.6995	0.0009
308.15	0.5995	0.0010
308.15	0.4998	0.0011
308.15	0.3997	0.0012
308.15	0.3002	0.0014
308.15	0.2006	0.0015
308.15	0.1003	0.0017
308.15	0.0000	0.0019
313.15	1.0000	0.0006
313.15	0.9004	0.0007
313.15	0.8002	0.0007
313.15	0.6995	0.0008
313.15	0.5995	0.0009
313.15	0.4998	0.0010
313.15	0.3997	0.0011
313.15	0.3002	0.0013
313.15	0.2006	0.0014
313.15	0.1003	0.0016
313.15	0.0000	0.0017
318.15	1.0000	0.0005
318.15	0.9004	0.0006
318.15	0.8002	0.0007
318.15	0.6995	0.0008
318.15	0.5995	0.0009
318.15	0.4998	0.0009
318.15	0.3997	0.0011
318.15	0.3002	0.0012
318.15	0.2006	0.0013
318.15	0.1003	0.0014
318.15	0.0000	0.0016
323.15	1.0000	0.0005
323.15	0.9004	0.0006
323.15	0.8002	0.0007
323.15	0.6995	0.0007
323.15	0.5995	0.0008
323.15	0.4998	0.0009
323.15	0.3997	0.0010
323.15	0.3002	0.0011
323.15	0.2006	0.0012
323.15	0.1003	0.0013
323.15	0.0000	0.0015
328.15	1.0000	0.0005
328.15	0.9004	0.0006
328.15	0.8002	0.0006
328.15	0.6995	0.0007
328.15	0.5995	0.0008
328.15	0.4998	0.0008
328.15	0.3997	0.0009
328.15	0.3002	0.0010
328.15	0.2006	0.0011
328.15	0.1003	0.0012
328.15	0.0000	0.0014
333.15	1.0000	0.0005
333.15	0.9004	0.0005
333.15	0.8002	0.0006
333.15	0.6995	0.0006
333.15	0.5995	0.0007
333.15	0.4998	0.0008
333.15	0.3997	0.0009
333.15	0.3002	0.0010
333.15	0.2006	0.0011
333.15	0.1003	0.0012
333.15	0.0000	0.0013
338.15	1.0000	0.0005
338.15	0.9004	0.0005
338.15	0.8002	0.0006
338.15	0.6995	0.0006
338.15	0.5995	0.0007
338.15	0.4998	0.0007
338.15	0.3997	0.0008
338.15	0.3002	0.0009
338.15	0.2006	0.0010
338.15	0.1003	0.0011
338.15	0.0000	0.0012
343.15	1.0000	0.0004
343.15	0.9004	0.0005
343.15	0.8002	0.0005
343.15	0.6995	0.0006
343.15	0.5995	0.0006
343.15	0.4998	0.0007
343.15	0.3997	0.0008
343.15	0.3002	0.0009
343.15	0.2006	0.0009
343.15	0.1003	0.0010
343.15	0.0000	0.0011

Viscosity, Pa*s [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Solvent: Mole fraction = 0.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane, methyl- (3) - Liquid	Viscosity, Pa*s - Liquid
293.15	1.0000	0.0007
293.15	0.9004	0.0008
293.15	0.8002	0.0010
293.15	0.6995	0.0011
293.15	0.5995	0.0012
293.15	0.4998	0.0014
293.15	0.3997	0.0016
293.15	0.3002	0.0017
293.15	0.2006	0.0020
293.15	0.1003	0.0022
293.15	0.0000	0.0025
298.15	1.0000	0.0007
298.15	0.9004	0.0008
298.15	0.8002	0.0009
298.15	0.6995	0.0010
298.15	0.5995	0.0011
298.15	0.4998	0.0013
298.15	0.3997	0.0014
298.15	0.3002	0.0016
298.15	0.2006	0.0018
298.15	0.1003	0.0020
298.15	0.0000	0.0023
303.15	1.0000	0.0006
303.15	0.9004	0.0007
303.15	0.8002	0.0008
303.15	0.6995	0.0009
303.15	0.5995	0.0010
303.15	0.4998	0.0012
303.15	0.3997	0.0013
303.15	0.3002	0.0015
303.15	0.2006	0.0016
303.15	0.1003	0.0018
303.15	0.0000	0.0021
308.15	1.0000	0.0006
308.15	0.9004	0.0007
308.15	0.8002	0.0008
308.15	0.6995	0.0009
308.15	0.5995	0.0010
308.15	0.4998	0.0011
308.15	0.3997	0.0012
308.15	0.3002	0.0014
308.15	0.2006	0.0015
308.15	0.1003	0.0017
308.15	0.0000	0.0019
313.15	1.0000	0.0006
313.15	0.9004	0.0007
313.15	0.8002	0.0007
313.15	0.6995	0.0008
313.15	0.5995	0.0009
313.15	0.4998	0.0010
313.15	0.3997	0.0011
313.15	0.3002	0.0013
313.15	0.2006	0.0014
313.15	0.1003	0.0016
313.15	0.0000	0.0017
318.15	1.0000	0.0005
318.15	0.9004	0.0006
318.15	0.8002	0.0007
318.15	0.6995	0.0008
318.15	0.5995	0.0009
318.15	0.4998	0.0009
318.15	0.3997	0.0011
318.15	0.3002	0.0012
318.15	0.2006	0.0013
318.15	0.1003	0.0014
318.15	0.0000	0.0016
323.15	1.0000	0.0005
323.15	0.9004	0.0006
323.15	0.8002	0.0007
323.15	0.6995	0.0007
323.15	0.5995	0.0008
323.15	0.4998	0.0009
323.15	0.3997	0.0010
323.15	0.3002	0.0011
323.15	0.2006	0.0012
323.15	0.1003	0.0013
323.15	0.0000	0.0015
328.15	1.0000	0.0005
328.15	0.9004	0.0006
328.15	0.8002	0.0006
328.15	0.6995	0.0007
328.15	0.5995	0.0008
328.15	0.4998	0.0008
328.15	0.3997	0.0009
328.15	0.3002	0.0010
328.15	0.2006	0.0011
328.15	0.1003	0.0012
328.15	0.0000	0.0014
333.15	1.0000	0.0005
333.15	0.9004	0.0005
333.15	0.8002	0.0006
333.15	0.6995	0.0006
333.15	0.5995	0.0007
333.15	0.4998	0.0008
333.15	0.3997	0.0009
333.15	0.3002	0.0010
333.15	0.2006	0.0011
333.15	0.1003	0.0012
333.15	0.0000	0.0013
338.15	1.0000	0.0005
338.15	0.9004	0.0005
338.15	0.8002	0.0006
338.15	0.6995	0.0006
338.15	0.5995	0.0007
338.15	0.4998	0.0007
338.15	0.3997	0.0008
338.15	0.3002	0.0009
338.15	0.2006	0.0010
338.15	0.1003	0.0011
338.15	0.0000	0.0012
343.15	1.0000	0.0004
343.15	0.9004	0.0005
343.15	0.8002	0.0005
343.15	0.6995	0.0006
343.15	0.5995	0.0006
343.15	0.4998	0.0007
343.15	0.3997	0.0008
343.15	0.3002	0.0009
343.15	0.2006	0.0009
343.15	0.1003	0.0010
343.15	0.0000	0.0011

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Solvent: Mole fraction = 0.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane, methyl- (3) - Liquid	Mass density, kg/m3 - Liquid
293.15	1.0000	769.35
293.15	0.9004	783.13
293.15	0.8002	796.3
293.15	0.6995	808.89
293.15	0.5995	820.76
293.15	0.4998	831.88
293.15	0.3997	842.53
293.15	0.3002	852.66
293.15	0.2006	862.3
293.15	0.1003	871.55
293.15	0.0000	880.41
298.15	1.0000	765.0
298.15	0.9004	778.88
298.15	0.8002	792.12
298.15	0.6995	804.78
298.15	0.5995	816.7
298.15	0.4998	827.89
298.15	0.3997	838.59
298.15	0.3002	848.76
298.15	0.2006	858.46
298.15	0.1003	867.75
298.15	0.0000	876.64
303.15	1.0000	760.65
303.15	0.9004	774.61
303.15	0.8002	787.93
303.15	0.6995	800.66
303.15	0.5995	812.63
303.15	0.4998	823.88
303.15	0.3997	834.64
303.15	0.3002	844.85
303.15	0.2006	854.61
303.15	0.1003	863.94
303.15	0.0000	872.86
308.15	1.0000	756.3
308.15	0.9004	770.34
308.15	0.8002	783.73
308.15	0.6995	796.53
308.15	0.5995	808.57
308.15	0.4998	819.88
308.15	0.3997	830.68
308.15	0.3002	840.95
308.15	0.2006	850.75
308.15	0.1003	860.13
308.15	0.0000	869.1
313.15	1.0000	751.93
313.15	0.9004	766.05
313.15	0.8002	779.52
313.15	0.6995	792.39
313.15	0.5995	804.49
313.15	0.4998	815.86
313.15	0.3997	826.72
313.15	0.3002	837.04
313.15	0.2006	846.9
313.15	0.1003	856.32
313.15	0.0000	865.33
318.15	1.0000	747.56
318.15	0.9004	761.75
318.15	0.8002	775.3
318.15	0.6995	788.24
318.15	0.5995	800.41
318.15	0.4998	811.84
318.15	0.3997	822.75
318.15	0.3002	833.13
318.15	0.2006	843.04
318.15	0.1003	852.51
318.15	0.0000	861.56
323.15	1.0000	743.16
323.15	0.9004	757.44
323.15	0.8002	771.06
323.15	0.6995	784.08
323.15	0.5995	796.32
323.15	0.4998	807.81
323.15	0.3997	818.78
323.15	0.3002	829.22
323.15	0.2006	839.18
323.15	0.1003	848.7
323.15	0.0000	857.8
328.15	1.0000	738.74
328.15	0.9004	753.11
328.15	0.8002	766.81
328.15	0.6995	779.91
328.15	0.5995	792.21
328.15	0.4998	803.77
328.15	0.3997	814.81
328.15	0.3002	825.3
328.15	0.2006	835.31
328.15	0.1003	844.88
328.15	0.0000	854.02
333.15	1.0000	734.29
333.15	0.9004	748.76
333.15	0.8002	762.55
333.15	0.6995	775.73
333.15	0.5995	788.1
333.15	0.4998	799.73
333.15	0.3997	810.82
333.15	0.3002	821.37
333.15	0.2006	831.43
333.15	0.1003	841.06
333.15	0.0000	850.25
338.15	1.0000	729.82
338.15	0.9004	744.38
338.15	0.8002	758.26
338.15	0.6995	771.52
338.15	0.5995	783.97
338.15	0.4998	795.67
338.15	0.3997	806.83
338.15	0.3002	817.44
338.15	0.2006	827.55
338.15	0.1003	837.23
338.15	0.0000	846.47
343.15	1.0000	725.32
343.15	0.9004	739.98
343.15	0.8002	753.96
343.15	0.6995	767.31
343.15	0.5995	779.83
343.15	0.4998	791.61
343.15	0.3997	802.84
343.15	0.3002	813.5
343.15	0.2006	823.66
343.15	0.1003	833.39
343.15	0.0000	842.68

Mass density, kg/m3 [ref]

Operational conditions:

• Pressure, kPa = 100 (Liquid)
• Solvent: Mole fraction = 0.5 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Cyclohexane, methyl- (3) - Liquid	Mass density, kg/m3 - Liquid
293.15	1.0000	769.35
293.15	0.9004	783.13
293.15	0.8002	796.3
293.15	0.6995	808.89
293.15	0.5995	820.76
293.15	0.4998	831.88
293.15	0.3997	842.53
293.15	0.3002	852.66
293.15	0.2006	862.3
293.15	0.1003	871.55
293.15	0.0000	880.41
298.15	1.0000	765.0
298.15	0.9004	778.88
298.15	0.8002	792.12
298.15	0.6995	804.78
298.15	0.5995	816.7
298.15	0.4998	827.89
298.15	0.3997	838.59
298.15	0.3002	848.76
298.15	0.2006	858.46
298.15	0.1003	867.75
298.15	0.0000	876.64
303.15	1.0000	760.65
303.15	0.9004	774.61
303.15	0.8002	787.93
303.15	0.6995	800.66
303.15	0.5995	812.63
303.15	0.4998	823.88
303.15	0.3997	834.64
303.15	0.3002	844.85
303.15	0.2006	854.61
303.15	0.1003	863.94
303.15	0.0000	872.86
308.15	1.0000	756.3
308.15	0.9004	770.34
308.15	0.8002	783.73
308.15	0.6995	796.53
308.15	0.5995	808.57
308.15	0.4998	819.88
308.15	0.3997	830.68
308.15	0.3002	840.95
308.15	0.2006	850.75
308.15	0.1003	860.13
308.15	0.0000	869.1
313.15	1.0000	751.93
313.15	0.9004	766.05
313.15	0.8002	779.52
313.15	0.6995	792.39
313.15	0.5995	804.49
313.15	0.4998	815.86
313.15	0.3997	826.72
313.15	0.3002	837.04
313.15	0.2006	846.9
313.15	0.1003	856.32
313.15	0.0000	865.33
318.15	1.0000	747.56
318.15	0.9004	761.75
318.15	0.8002	775.3
318.15	0.6995	788.24
318.15	0.5995	800.41
318.15	0.4998	811.84
318.15	0.3997	822.75
318.15	0.3002	833.13
318.15	0.2006	843.04
318.15	0.1003	852.51
318.15	0.0000	861.56
323.15	1.0000	743.16
323.15	0.9004	757.44
323.15	0.8002	771.06
323.15	0.6995	784.08
323.15	0.5995	796.32
323.15	0.4998	807.81
323.15	0.3997	818.78
323.15	0.3002	829.22
323.15	0.2006	839.18
323.15	0.1003	848.7
323.15	0.0000	857.8
328.15	1.0000	738.74
328.15	0.9004	753.11
328.15	0.8002	766.81
328.15	0.6995	779.91
328.15	0.5995	792.21
328.15	0.4998	803.77
328.15	0.3997	814.81
328.15	0.3002	825.3
328.15	0.2006	835.31
328.15	0.1003	844.88
328.15	0.0000	854.02
333.15	1.0000	734.29
333.15	0.9004	748.76
333.15	0.8002	762.55
333.15	0.6995	775.73
333.15	0.5995	788.1
333.15	0.4998	799.73
333.15	0.3997	810.82
333.15	0.3002	821.37
333.15	0.2006	831.43
333.15	0.1003	841.06
333.15	0.0000	850.25
338.15	1.0000	729.82
338.15	0.9004	744.38
338.15	0.8002	758.26
338.15	0.6995	771.52
338.15	0.5995	783.97
338.15	0.4998	795.67
338.15	0.3997	806.83
338.15	0.3002	817.44
338.15	0.2006	827.55
338.15	0.1003	837.23
338.15	0.0000	846.47
343.15	1.0000	725.32
343.15	0.9004	739.98
343.15	0.8002	753.96
343.15	0.6995	767.31
343.15	0.5995	779.83
343.15	0.4998	791.61
343.15	0.3997	802.84
343.15	0.3002	813.5
343.15	0.2006	823.66
343.15	0.1003	833.39
343.15	0.0000	842.68

Sources

• Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K