Mixture of 1-Octanol + Cyclohexane

Datasets

1. Mole fraction (2)
2. η - Viscosity, Pa*s (2)
3. ρ_l - Mass density, kg/m3 (4)
4. T_boil - Boiling temperature at pressure P, K (2)

Mole fraction of 1-Octanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of 1-Octanol (1) - Liquid	Mole fraction of 1-Octanol (1) - Gas
0.0100	0.0005
0.0133	0.0007
0.0195	0.0008
0.0288	0.0010
0.0352	0.0012
0.0365	0.0012
0.0440	0.0013
0.0565	0.0014
0.0576	0.0015

Mole fraction of 1-Octanol (1) [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of 1-Octanol (1) - Liquid	Mole fraction of 1-Octanol (1) - Gas
0.0100	0.0005
0.0133	0.0007
0.0195	0.0008
0.0288	0.0010
0.0352	0.0012
0.0365	0.0012
0.0440	0.0013
0.0565	0.0014
0.0576	0.0015

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Octanol (1) - Liquid	Viscosity, Pa*s - Liquid
0.2008	0.0012
0.3755	0.0018
0.5205	0.0024
0.6054	0.0028
0.7044	0.0035
0.7758	0.0040
0.8541	0.0046
0.9010	0.0051
0.9553	0.0057

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Octanol (1) - Liquid	Viscosity, Pa*s - Liquid
0.2008	0.0012
0.3755	0.0018
0.5205	0.0024
0.6054	0.0028
0.7044	0.0035
0.7758	0.0040
0.8541	0.0046
0.9010	0.0051
0.9553	0.0057

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	821.4
0.0815	818.3
0.1602	815.1
0.2408	811.7
0.3494	806.9
0.4398	802.7
0.5605	796.8
0.6496	792.4
0.7404	787.8
0.8495	782.0
0.9400	777.0
1.0000	773.6

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Octanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.2008	780.75
0.3755	789.9
0.5205	796.98
0.6054	800.89
0.7044	805.34
0.7758	808.38
0.8541	811.63
0.9010	813.56
0.9553	815.75

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 298.15 (Liquid)
• Pressure, kPa = 100 (Liquid)

Mole fraction of Cyclohexane (2) - Liquid	Mass density, kg/m3 - Liquid
0.0000	821.4
0.0815	818.3
0.1602	815.1
0.2408	811.7
0.3494	806.9
0.4398	802.7
0.5605	796.8
0.6496	792.4
0.7404	787.8
0.8495	782.0
0.9400	777.0
1.0000	773.6

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101 (Liquid)

Mole fraction of 1-Octanol (1) - Liquid	Mass density, kg/m3 - Liquid
0.2008	780.75
0.3755	789.9
0.5205	796.98
0.6054	800.89
0.7044	805.34
0.7758	808.38
0.8541	811.63
0.9010	813.56
0.9553	815.75

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of 1-Octanol (1) - Liquid	Boiling temperature at pressure P, K - Gas
0.0100	354.10
0.0133	354.10
0.0195	354.20
0.0288	354.40
0.0352	354.50
0.0365	354.60
0.0440	354.70
0.0565	354.80
0.0576	354.90

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 101.3 (Gas)

Mole fraction of 1-Octanol (1) - Liquid	Boiling temperature at pressure P, K - Gas
0.0100	354.10
0.0133	354.10
0.0195	354.20
0.0288	354.40
0.0352	354.50
0.0365	354.60
0.0440	354.70
0.0565	354.80
0.0576	354.90

Sources

• Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
• Evaluation of (vapor + liquid) equilibria for the binary systems (1-octanol + cyclohexane) and (1-octanol + n-hexane), at low alcohol compositions
• Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model