Mixture of Octane + Phenol

Datasets

1. Upper consolute composition: mole fraction (2)
2. Upper consolute temperature, K (2)
3. Liquid-liquid equilibrium temperature, K (4)

Upper consolute composition: mole fraction of Phenol (2) [ref]

Upper consolute composition: mole fraction of Phenol (2) - Liquid mixture 1
0.5457

Upper consolute composition: mole fraction of Phenol (2) [ref]

Upper consolute composition: mole fraction of Phenol (2) - Liquid mixture 1
0.5457

Upper consolute temperature, K [ref]

Upper consolute temperature, K - Liquid mixture 1
329.54

Upper consolute temperature, K [ref]

Upper consolute temperature, K - Liquid mixture 1
329.54

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Mole fraction of Phenol (2) - Liquid mixture 1	Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.1486	306.67
0.1943	314.69
0.2960	323.33
0.3479	326.08
0.3990	327.46
0.4176	328.30
0.4935	329.33
0.5437	329.53
0.5457	329.54
0.5991	329.34
0.6493	328.72
0.6979	327.28
0.7451	325.22
0.7949	320.16
0.8191	316.55
0.8472	310.99
0.8622	306.18

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Mole fraction of Phenol (2) - Liquid mixture 1	Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.1232	301.85
0.1410	305.55
0.1534	307.90
0.1680	310.05
0.1859	312.55
0.2036	314.85
0.2186	316.45
0.2361	318.20
0.2564	319.85
0.2959	323.45
0.3073	324.30
0.3629	327.30
0.3879	328.05
0.4174	328.70
0.4530	329.20
0.4948	329.85
0.5256	330.00
0.5577	329.95
0.5908	329.80
0.6203	329.45
0.6501	329.05
0.6745	328.55
0.7022	327.65
0.7306	326.35
0.7493	325.45
0.7625	324.60
0.7808	322.35
0.8000	319.75
0.8201	317.10
0.8352	313.45
0.8481	310.25

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)

Mole fraction of Phenol (2) - Liquid mixture 1	Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.1486	306.67
0.1943	314.69
0.2960	323.33
0.3479	326.08
0.3990	327.46
0.4176	328.30
0.4935	329.33
0.5437	329.53
0.5457	329.54
0.5991	329.34
0.6493	328.72
0.6979	327.28
0.7451	325.22
0.7949	320.16
0.8191	316.55
0.8472	310.99
0.8622	306.18

Liquid-liquid equilibrium temperature, K [ref]

Operational condition: Pressure, kPa = 101 (Liquid mixture 1)

Mole fraction of Phenol (2) - Liquid mixture 1	Liquid-liquid equilibrium temperature, K - Liquid mixture 1
0.1232	301.85
0.1410	305.55
0.1534	307.90
0.1680	310.05
0.1859	312.55
0.2036	314.85
0.2186	316.45
0.2361	318.20
0.2564	319.85
0.2959	323.45
0.3073	324.30
0.3629	327.30
0.3879	328.05
0.4174	328.70
0.4530	329.20
0.4948	329.85
0.5256	330.00
0.5577	329.95
0.5908	329.80
0.6203	329.45
0.6501	329.05
0.6745	328.55
0.7022	327.65
0.7306	326.35
0.7493	325.45
0.7625	324.60
0.7808	322.35
0.8000	319.75
0.8201	317.10
0.8352	313.45
0.8481	310.25

Sources

• Measurement and Correlation of Mutual Solubilities for High Viscosity Binary Systems: Aniline + Methylcyclohexane, Phenol + Heptane, Phenol + Octane, and Glycerol + 1-Pentanol
• Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water