- Name
- PHENOL, 4-METHYL-
- InChI
- InChI=1S/C7H8O/c1-6-2-4-7(8)5-3-6/h2-5,8H,1H3
- InChI Key
- IWDCLRJOBJJRNH-UHFFFAOYSA-N
- Formula
- C7H8O
- SMILES
- Cc1ccc(O)cc1
- Mol. Weight (g/mol)
- 108.14
- CAS
- 106-44-5
- Name
- Water
- InChI
- InChI=1S/H2O/h1H2
- InChI Key
- XLYOFNOQVPJJNP-UHFFFAOYSA-N
- Formula
- H2O
- SMILES
- O
- Mol. Weight (g/mol)
- 18.02
- CAS
- 7732-18-5
Datasets
Mole fraction of PHENOL, 4-METHYL- (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of PHENOL, 4-METHYL- (1) - Liquid mixture 1 |
|---|---|
| 298.15 | 0.0036 |
| 303.15 | 0.0037 |
| 308.15 | 0.0038 |
| 313.15 | 0.0039 |
| 318.15 | 0.0040 |
Mole fraction of PHENOL, 4-METHYL- (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of PHENOL, 4-METHYL- (1) - Liquid mixture 2 |
|---|---|
| 298.15 | 0.4843 |
| 303.15 | 0.4720 |
| 308.15 | 0.4617 |
| 313.15 | 0.4518 |
| 318.15 | 0.4455 |
Mole fraction of PHENOL, 4-METHYL- (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 | Mole fraction of PHENOL, 4-METHYL- (1) - Liquid mixture 2 |
|---|---|
| 333.20 | 0.4674 |
| 343.20 | 0.4423 |
Mole fraction of PHENOL, 4-METHYL- (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 | Mole fraction of PHENOL, 4-METHYL- (1) - Liquid mixture 1 |
|---|---|
| 333.20 | 0.0048 |
| 343.20 | 0.0063 |
Mass fraction of PHENOL, 4-METHYL- (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 | Mass fraction of PHENOL, 4-METHYL- (1) - Liquid mixture 2 |
|---|---|
| 323.15 | 0.8247 |
| 298.15 | 0.8465 |
Mass fraction of PHENOL, 4-METHYL- (1) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 1 | Mass fraction of PHENOL, 4-METHYL- (1) - Liquid mixture 1 |
|---|---|
| 323.15 | 0.0249 |
| 298.15 | 0.0196 |
Mole fraction of PHENOL, 4-METHYL- (1) [ref]
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of PHENOL, 4-METHYL- (1) - Liquid mixture 1 |
|---|---|
| 283.15 | 0.0035 |
| 298.15 | 0.0037 |
| 313.15 | 0.0040 |
Mole fraction of Water (2) [ref]
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 2 |
|---|---|
| 283.15 | 0.4820 |
| 298.15 | 0.5202 |
| 313.15 | 0.5562 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 303.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of PHENOL, 4-METHYL- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.5480 | 1020.42 |
| 0.6243 | 1021.77 |
| 0.6758 | 1022.35 |
| 0.7400 | 1023.33 |
| 0.7976 | 1023.92 |
| 0.8897 | 1025.1 |
Sources
- Phase equilibria of phenolic compounds in water or ethanol
- Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibrium for extraction of o-cresol, m-cresol or p-cresol from aqueous solution with 2-pentanone
- (Liquid + liquid) extraction of phenols from aqueous solutions with cineole
- Extraction of o-, m- and p-cresol from aqueous solution with methyl isopropyl ketone: Equilibrium, correlations, and COSMO-RS predictions
- Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water