Mixture of Heptane + Phenol

Excel

Heptane

Name
Heptane
InChI
InChI=1S/C7H16/c1-3-5-7-6-4-2/h3-7H2,1-2H3
InChI Key
IMNFDUFMRHMDMM-UHFFFAOYSA-N
Formula
C7H16
SMILES
CCCCCCC
Mol. Weight (g/mol)
100.20
CAS
142-82-5

Phenol

Name
Phenol
InChI
InChI=1S/C6H6O/c7-6-4-2-1-3-5-6/h1-5,7H
InChI Key
ISWSIDIOOBJBQZ-UHFFFAOYSA-N
Formula
C6H6O
SMILES
Oc1ccccc1
Mol. Weight (g/mol)
94.11
CAS
108-95-2
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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
0.5188

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

Upper consolute composition: mole fraction of Phenol (2) - Liquid mixture 1
0.5188

Upper consolute temperature, K [ref]

Upper consolute temperature, K - Liquid mixture 1
327.30

Upper consolute temperature, K [ref]

Upper consolute temperature, K - Liquid mixture 1
327.30

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
0.1372 305.95
0.1429 307.05
0.1693 311.28
0.1737 311.93
0.1946 314.27
0.1981 314.50
0.2043 315.67
0.2127 316.61
0.2512 319.58
0.2949 321.99
0.3442 324.27
0.3773 324.99
0.4142 325.92
0.4222 326.05
0.4497 326.58
0.4698 326.90
0.5188 327.30
0.5563 327.01
0.6051 326.63
0.6417 325.07
0.6712 324.04
0.7010 323.01
0.7465 319.54
0.7700 317.33
0.7783 315.01
0.7998 311.26
0.8297 305.63

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
0.1414 305.35
0.1551 308.05
0.1734 310.35
0.1987 314.21
0.2651 320.11
0.3236 323.05
0.3842 324.80
0.4038 325.12
0.4261 325.35
0.4481 325.50
0.4663 325.66
0.4726 325.75
0.4885 325.85
0.5220 325.94
0.5375 325.90
0.5532 325.75
0.5653 325.65
0.5796 325.55
0.5933 325.47
0.6113 325.25
0.6270 325.05
0.6506 324.70
0.6702 324.15
0.6949 323.05
0.7184 321.35
0.7465 318.75
0.7841 314.35
0.8001 311.55

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
0.1372 305.95
0.1429 307.05
0.1693 311.28
0.1737 311.93
0.1946 314.27
0.1981 314.50
0.2043 315.67
0.2127 316.61
0.2512 319.58
0.2949 321.99
0.3442 324.27
0.3773 324.99
0.4142 325.92
0.4222 326.05
0.4497 326.58
0.4698 326.90
0.5188 327.30
0.5563 327.01
0.6051 326.63
0.6417 325.07
0.6712 324.04
0.7010 323.01
0.7465 319.54
0.7700 317.33
0.7783 315.01
0.7998 311.26
0.8297 305.63

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
0.1414 305.35
0.1551 308.05
0.1734 310.35
0.1987 314.21
0.2651 320.11
0.3236 323.05
0.3842 324.80
0.4038 325.12
0.4261 325.35
0.4481 325.50
0.4663 325.66
0.4726 325.75
0.4885 325.85
0.5220 325.94
0.5375 325.90
0.5532 325.75
0.5653 325.65
0.5796 325.55
0.5933 325.47
0.6113 325.25
0.6270 325.05
0.6506 324.70
0.6702 324.15
0.6949 323.05
0.7184 321.35
0.7465 318.75
0.7841 314.35
0.8001 311.55

Sources