Mixture of Cyclohexane + Methyl Alcohol

Datasets

1. Mole fraction (4)
2. η - Viscosity, Pa*s (2)
3. Liquid-liquid equilibrium temperature, K (4)
4. ρ_l - Mass density, kg/m3 (2)
5. Vapor Liquid Equilibrium at Constant Pressure
6. Vapor Liquid Equilibrium at Constant Temperature (2)

Mole fraction of Cyclohexane (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Temperature, K - Liquid mixture 2	Mole fraction of Cyclohexane (1) - Liquid mixture 2
278.15	0.1040
283.15	0.1250
288.15	0.1350
293.15	0.1580
298.15	0.1770
303.15	0.1900
308.15	0.2180
313.15	0.2610
316.15	0.3010

Mole fraction of Cyclohexane (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Cyclohexane (1) - Liquid mixture 1
278.15	0.9420
283.15	0.9390
288.15	0.9220
293.15	0.8920
298.15	0.8760
303.15	0.8410
308.15	0.8120
313.15	0.7580
316.15	0.7020

Mole fraction of Cyclohexane (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Temperature, K - Liquid mixture 2	Mole fraction of Cyclohexane (1) - Liquid mixture 2
278.15	0.1040
283.15	0.1250
288.15	0.1350
293.15	0.1580
298.15	0.1770
303.15	0.1900
308.15	0.2180
313.15	0.2610
316.15	0.3010

Mole fraction of Cyclohexane (1) [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Temperature, K - Liquid mixture 1	Mole fraction of Cyclohexane (1) - Liquid mixture 1
278.15	0.9420
283.15	0.9390
288.15	0.9220
293.15	0.8920
298.15	0.8760
303.15	0.8410
308.15	0.8120
313.15	0.7580
316.15	0.7020

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Viscosity, Pa*s - Liquid
321.15	1.0000	0.0004
321.15	0.9590	0.0004
321.15	0.9130	0.0004
321.15	0.8600	0.0004
321.15	0.8300	0.0004
321.15	0.7980	0.0004
321.15	0.7620	0.0005
321.15	0.7240	0.0005
321.15	0.6370	0.0005
321.15	0.5270	0.0006
321.15	0.5000	0.0006
321.15	0.4670	0.0006
321.15	0.3960	0.0005
321.15	0.2260	0.0005
321.15	0.1210	0.0006
321.15	0.0000	0.0006
322.15	1.0000	0.0004
322.15	0.9590	0.0004
322.15	0.9130	0.0004
322.15	0.8600	0.0004
322.15	0.8300	0.0004
322.15	0.7980	0.0004
322.15	0.7620	0.0005
322.15	0.7240	0.0005
322.15	0.6370	0.0005
322.15	0.5270	0.0005
322.15	0.5000	0.0006
322.15	0.4670	0.0006
322.15	0.3960	0.0005
322.15	0.2260	0.0005
322.15	0.1210	0.0005
322.15	0.0000	0.0006
323.15	1.0000	0.0004
323.15	0.9590	0.0004
323.15	0.9130	0.0004
323.15	0.8600	0.0004
323.15	0.8300	0.0004
323.15	0.7980	0.0004
323.15	0.7620	0.0004
323.15	0.7240	0.0005
323.15	0.6370	0.0005
323.15	0.5270	0.0005
323.15	0.5000	0.0005
323.15	0.4670	0.0005
323.15	0.3960	0.0005
323.15	0.2260	0.0005
323.15	0.1210	0.0005
323.15	0.0000	0.0006
325.15	1.0000	0.0004
325.15	0.9590	0.0004
325.15	0.9130	0.0004
325.15	0.8600	0.0004
325.15	0.8300	0.0004
325.15	0.7980	0.0004
325.15	0.7620	0.0004
325.15	0.7240	0.0004
325.15	0.6370	0.0005
325.15	0.5270	0.0005
325.15	0.5000	0.0005
325.15	0.4670	0.0005
325.15	0.3960	0.0005
325.15	0.2260	0.0005
325.15	0.1210	0.0005
325.15	0.0000	0.0006

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Viscosity, Pa*s - Liquid
321.15	1.0000	0.0004
321.15	0.9590	0.0004
321.15	0.9130	0.0004
321.15	0.8600	0.0004
321.15	0.8300	0.0004
321.15	0.7980	0.0004
321.15	0.7620	0.0005
321.15	0.7240	0.0005
321.15	0.6370	0.0005
321.15	0.5270	0.0006
321.15	0.5000	0.0006
321.15	0.4670	0.0006
321.15	0.3960	0.0005
321.15	0.2260	0.0005
321.15	0.1210	0.0006
321.15	0.0000	0.0006
322.15	1.0000	0.0004
322.15	0.9590	0.0004
322.15	0.9130	0.0004
322.15	0.8600	0.0004
322.15	0.8300	0.0004
322.15	0.7980	0.0004
322.15	0.7620	0.0005
322.15	0.7240	0.0005
322.15	0.6370	0.0005
322.15	0.5270	0.0005
322.15	0.5000	0.0006
322.15	0.4670	0.0006
322.15	0.3960	0.0005
322.15	0.2260	0.0005
322.15	0.1210	0.0005
322.15	0.0000	0.0006
323.15	1.0000	0.0004
323.15	0.9590	0.0004
323.15	0.9130	0.0004
323.15	0.8600	0.0004
323.15	0.8300	0.0004
323.15	0.7980	0.0004
323.15	0.7620	0.0004
323.15	0.7240	0.0005
323.15	0.6370	0.0005
323.15	0.5270	0.0005
323.15	0.5000	0.0005
323.15	0.4670	0.0005
323.15	0.3960	0.0005
323.15	0.2260	0.0005
323.15	0.1210	0.0005
323.15	0.0000	0.0006
325.15	1.0000	0.0004
325.15	0.9590	0.0004
325.15	0.9130	0.0004
325.15	0.8600	0.0004
325.15	0.8300	0.0004
325.15	0.7980	0.0004
325.15	0.7620	0.0004
325.15	0.7240	0.0004
325.15	0.6370	0.0005
325.15	0.5270	0.0005
325.15	0.5000	0.0005
325.15	0.4670	0.0005
325.15	0.3960	0.0005
325.15	0.2260	0.0005
325.15	0.1210	0.0005
325.15	0.0000	0.0006

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid mixture 1)

Mole fraction of Methyl Alcohol (2) - Liquid mixture 1	Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.8597	287.98
0.8299	296.99
0.8240	298.43
0.8140	300.86
0.8060	302.34
0.7975	304.48
0.7804	307.36
0.7624	310.58
0.7438	312.45
0.7242	314.76
0.7040	316.25
0.6824	317.48
0.6600	318.15
0.6365	318.72
0.5858	318.85
0.5527	319.10
0.5295	319.21
0.5175	319.60
0.4993	319.35
0.4927	319.23
0.4799	319.46
0.4668	319.29
0.4534	319.56
0.4396	319.60
0.4255	319.23
0.4111	319.45
0.3963	319.14
0.3812	319.42
0.3498	318.50
0.3167	317.06
0.2637	315.06
0.2259	313.17
0.2220	312.38
0.2062	310.27
0.1859	309.17
0.1713	307.34
0.1650	304.57
0.1435	302.81
0.1295	300.85
0.1214	298.36
0.1108	297.15

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Mole fraction of Methyl Alcohol (2) - Liquid mixture 1	Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.1471	308.36
0.2503	317.36
0.3018	319.24
0.3553	320.86
0.4040	322.22
0.4578	321.53
0.5082	321.64
0.5582	321.36
0.6008	321.30
0.7015	319.09
0.8019	306.28

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid mixture 1)

Mole fraction of Methyl Alcohol (2) - Liquid mixture 1	Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.8597	287.98
0.8299	296.99
0.8240	298.43
0.8140	300.86
0.8060	302.34
0.7975	304.48
0.7804	307.36
0.7624	310.58
0.7438	312.45
0.7242	314.76
0.7040	316.25
0.6824	317.48
0.6600	318.15
0.6365	318.72
0.5858	318.85
0.5527	319.10
0.5295	319.21
0.5175	319.60
0.4993	319.35
0.4927	319.23
0.4799	319.46
0.4668	319.29
0.4534	319.56
0.4396	319.60
0.4255	319.23
0.4111	319.45
0.3963	319.14
0.3812	319.42
0.3498	318.50
0.3167	317.06
0.2637	315.06
0.2259	313.17
0.2220	312.38
0.2062	310.27
0.1859	309.17
0.1713	307.34
0.1650	304.57
0.1435	302.81
0.1295	300.85
0.1214	298.36
0.1108	297.15

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 100 (Liquid mixture 1)

Mole fraction of Methyl Alcohol (2) - Liquid mixture 1	Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.1471	308.36
0.2503	317.36
0.3018	319.24
0.3553	320.86
0.4040	322.22
0.4578	321.53
0.5082	321.64
0.5582	321.36
0.6008	321.30
0.7015	319.09
0.8019	306.28

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
321.15	1.0000	765.18
321.15	0.9590	760.9
321.15	0.9130	756.79
321.15	0.8600	753.62
321.15	0.8300	752.41
321.15	0.7980	752.02
321.15	0.7620	751.22
321.15	0.7240	750.76
321.15	0.6370	749.61
321.15	0.5270	749.02
321.15	0.5000	748.58
321.15	0.4670	748.53
321.15	0.3960	748.75
321.15	0.2260	748.95
321.15	0.1210	749.62
321.15	0.0000	751.7
322.15	1.0000	764.21
322.15	0.9590	759.92
322.15	0.9130	755.8
322.15	0.8600	752.62
322.15	0.8300	751.4
322.15	0.7980	751.0
322.15	0.7620	750.2
322.15	0.7240	749.74
322.15	0.6370	748.55
322.15	0.5270	747.95
322.15	0.5000	747.54
322.15	0.4670	747.49
322.15	0.3960	747.73
322.15	0.2260	747.92
322.15	0.1210	748.62
322.15	0.0000	750.73
323.15	1.0000	763.24
323.15	0.9590	758.94
323.15	0.9130	754.81
323.15	0.8600	751.61
323.15	0.8300	750.37
323.15	0.7980	749.69
323.15	0.7620	748.78
323.15	0.7240	748.73
323.15	0.6370	747.51
323.15	0.5270	746.89
323.15	0.5000	746.49
323.15	0.4670	746.44
323.15	0.3960	746.71
323.15	0.2260	746.88
323.15	0.1210	747.61
323.15	0.0000	749.76
325.15	1.0000	761.42
325.15	0.9590	757.17
325.15	0.9130	753.05
325.15	0.8600	749.82
325.15	0.8300	748.52
325.15	0.7980	748.08
325.15	0.7620	747.25
325.15	0.7240	746.82
325.15	0.6370	745.15
325.15	0.5270	744.84
325.15	0.5000	745.11
325.15	0.4670	744.47
325.15	0.3960	744.54
325.15	0.2260	744.79
325.15	0.1210	745.68
325.15	0.0000	747.95

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101.32 (Liquid)

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Methyl Alcohol (2) - Liquid	Mass density, kg/m3 - Liquid
321.15	1.0000	765.18
321.15	0.9590	760.9
321.15	0.9130	756.79
321.15	0.8600	753.62
321.15	0.8300	752.41
321.15	0.7980	752.02
321.15	0.7620	751.22
321.15	0.7240	750.76
321.15	0.6370	749.61
321.15	0.5270	749.02
321.15	0.5000	748.58
321.15	0.4670	748.53
321.15	0.3960	748.75
321.15	0.2260	748.95
321.15	0.1210	749.62
321.15	0.0000	751.7
322.15	1.0000	764.21
322.15	0.9590	759.92
322.15	0.9130	755.8
322.15	0.8600	752.62
322.15	0.8300	751.4
322.15	0.7980	751.0
322.15	0.7620	750.2
322.15	0.7240	749.74
322.15	0.6370	748.55
322.15	0.5270	747.95
322.15	0.5000	747.54
322.15	0.4670	747.49
322.15	0.3960	747.73
322.15	0.2260	747.92
322.15	0.1210	748.62
322.15	0.0000	750.73
323.15	1.0000	763.24
323.15	0.9590	758.94
323.15	0.9130	754.81
323.15	0.8600	751.61
323.15	0.8300	750.37
323.15	0.7980	749.69
323.15	0.7620	748.78
323.15	0.7240	748.73
323.15	0.6370	747.51
323.15	0.5270	746.89
323.15	0.5000	746.49
323.15	0.4670	746.44
323.15	0.3960	746.71
323.15	0.2260	746.88
323.15	0.1210	747.61
323.15	0.0000	749.76
325.15	1.0000	761.42
325.15	0.9590	757.17
325.15	0.9130	753.05
325.15	0.8600	749.82
325.15	0.8300	748.52
325.15	0.7980	748.08
325.15	0.7620	747.25
325.15	0.7240	746.82
325.15	0.6370	745.15
325.15	0.5270	744.84
325.15	0.5000	745.11
325.15	0.4670	744.47
325.15	0.3960	744.54
325.15	0.2260	744.79
325.15	0.1210	745.68
325.15	0.0000	747.95

Vapor Liquid Equilibrium at Constant Pressure [ref]

Operational condition: Pressure, kPa = 101.33 (VLE)

Fixed	Measured
T [K] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid	y1[mol/mol] of Methyl Alcohol (2) - Vapour
353.9	0.0000	0.0000
330.2	0.0370	0.5640
327.6	0.1860	0.5900
327.48	0.3000	0.5940
327.47	0.3820	0.5950
327.46	0.4850	0.5970
327.43	0.5900	0.6040
327.57	0.8110	0.6390
329.08	0.9140	0.7060
332.81	0.9720	0.8190
337.8	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 308.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid	y1[mol/mol] of Methyl Alcohol (2) - Vapour
19.625	0.0000	0.0000
43.33	0.0940	0.5680
44.396	0.8000	0.5860
42.57	0.9040	0.6270
36.784	0.9620	0.7520
27.198	1.0000	1.0000

Vapor Liquid Equilibrium at Constant Temperature [ref]

Operational condition: Temperature, K = 318.15 (VLE)

Fixed	Measured
P [kPa] - VLE	x1[mol/mol] of Methyl Alcohol (2) - Liquid	y1[mol/mol] of Methyl Alcohol (2) - Vapour
29.464	0.0000	0.0000
66.101	0.0730	0.5550
69.234	0.2070	0.5900
69.154	0.6800	0.5980
68.034	0.8030	0.6130
64.888	0.9030	0.6580
56.329	0.9650	0.7720
43.463	1.0000	1.0000

Sources

• Dortmund Data Bank Vapor-Liquid Equilibrium Data
• Thermodynamic properties of cyclohexane methanol liquid mixture from shear viscosity measurements
• Liquid-Liquid Coexistence Curves for Binary Systems: Methanol + Cyclohexane and + Several Isomers of Hexane
• Liquid-Liquid Equilibrium of (Cyclohexane + 2,2,2-Trifluoroethanol) and (Cyclohexane + Methanol) from (278.15 to 318.15) K