- Name
- Toluene
- InChI
- InChI=1S/C7H8/c1-7-5-3-2-4-6-7/h2-6H,1H3
- InChI Key
- YXFVVABEGXRONW-UHFFFAOYSA-N
- Formula
- C7H8
- SMILES
- Cc1ccccc1
- Mol. Weight (g/mol)
- 92.14
- CAS
- 108-88-3
- Name
- Triethylene glycol
- InChI
- InChI=1S/C6H14O4/c7-1-3-9-5-6-10-4-2-8/h7-8H,1-6H2
- InChI Key
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N
- Formula
- C6H14O4
- SMILES
- OCCOCCOCCO
- Mol. Weight (g/mol)
- 150.17
- CAS
- 112-27-6
Datasets
Activity coefficient of Toluene (1) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Toluene (1) - Liquid |
|---|---|
| 333.20 | 5.88 |
| 348.20 | 5.73 |
| 363.20 | 5.55 |
Activity coefficient of Toluene (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Toluene (1) - Liquid |
|---|---|
| 323.15 | 7.1078 |
| 333.15 | 6.7965 |
| 343.15 | 6.5103 |
| 353.15 | 6.2512 |
| 363.15 | 5.9922 |
| 373.10 | 5.8481 |
| 383.15 | 5.5627 |
| 393.15 | 5.512 |
Activity coefficient of Toluene (1) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Toluene (1) - Liquid |
|---|---|
| 333.20 | 5.88 |
| 348.20 | 5.73 |
| 363.20 | 5.55 |
Activity coefficient of Toluene (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Toluene (1) - Liquid |
|---|---|
| 323.15 | 7.1078 |
| 333.15 | 6.7965 |
| 343.15 | 6.5103 |
| 353.15 | 6.2512 |
| 363.15 | 5.9922 |
| 373.10 | 5.8481 |
| 383.15 | 5.5627 |
| 393.15 | 5.512 |
Mole fraction of Triethylene glycol (2) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Triethylene glycol (2) - Liquid mixture 1 |
|---|---|
| 343.15 | 0.0760 |
| 348.05 | 0.0950 |
| 353.35 | 0.1240 |
| 355.75 | 0.1470 |
| 357.75 | 0.1810 |
| 358.29 | 0.2040 |
| 358.45 | 0.2340 |
| 358.75 | 0.2740 |
| 358.05 | 0.3320 |
| 357.85 | 0.3620 |
| 356.85 | 0.3980 |
| 354.65 | 0.4430 |
| 352.65 | 0.4690 |
| 350.15 | 0.4980 |
| 344.45 | 0.5320 |
| 336.95 | 0.5700 |
| 324.35 | 0.6140 |
| 298.15 | 0.6650 |
Mole fraction of Toluene (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Toluene (1) - Liquid mixture 1 |
|---|---|
| 279.00 | 0.3084 |
| 293.00 | 0.3296 |
| 302.00 | 0.3478 |
| 312.80 | 0.3589 |
| 321.20 | 0.3814 |
| 331.50 | 0.4195 |
| 344.20 | 0.4637 |
| 345.40 | 0.4850 |
Mole fraction of Triethylene glycol (2) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mole fraction of Triethylene glycol (2) - Liquid mixture 2 |
|---|---|
| 279.00 | 0.0107 |
| 293.00 | 0.0186 |
| 302.00 | 0.0226 |
| 312.80 | 0.0316 |
| 321.20 | 0.0416 |
| 331.50 | 0.0566 |
| 344.20 | 0.0837 |
| 345.40 | 0.0866 |
Mole fraction of Triethylene glycol (2) [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Triethylene glycol (2) - Liquid mixture 1 |
|---|---|
| 343.15 | 0.0760 |
| 348.05 | 0.0950 |
| 353.35 | 0.1240 |
| 355.75 | 0.1470 |
| 357.75 | 0.1810 |
| 358.29 | 0.2040 |
| 358.45 | 0.2340 |
| 358.75 | 0.2740 |
| 358.05 | 0.3320 |
| 357.85 | 0.3620 |
| 356.85 | 0.3980 |
| 354.65 | 0.4430 |
| 352.65 | 0.4690 |
| 350.15 | 0.4980 |
| 344.45 | 0.5320 |
| 336.95 | 0.5700 |
| 324.35 | 0.6140 |
| 298.15 | 0.6650 |
Mole fraction of Toluene (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Toluene (1) - Liquid mixture 1 |
|---|---|
| 279.00 | 0.3084 |
| 293.00 | 0.3296 |
| 302.00 | 0.3478 |
| 312.80 | 0.3589 |
| 321.20 | 0.3814 |
| 331.50 | 0.4195 |
| 344.20 | 0.4637 |
| 345.40 | 0.4850 |
Mole fraction of Triethylene glycol (2) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mole fraction of Triethylene glycol (2) - Liquid mixture 2 |
|---|---|
| 279.00 | 0.0107 |
| 293.00 | 0.0186 |
| 302.00 | 0.0226 |
| 312.80 | 0.0316 |
| 321.20 | 0.0416 |
| 331.50 | 0.0566 |
| 344.20 | 0.0837 |
| 345.40 | 0.0866 |
Sources
- Liquid-liquid phase diagrams of poly(ethylene glycol) and aromatic hydrocarbons
- Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
- Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
- Liquid-Liquid Equilibria for Binary and Ternary Systems Containing Glycols, Aromatic Hydrocarbons, and Water: Experimental Measurements and Modeling with the CPA EoS