- Name
- Benzene
- InChI
- InChI=1S/C6H6/c1-2-4-6-5-3-1/h1-6H
- InChI Key
- UHOVQNZJYSORNB-UHFFFAOYSA-N
- Formula
- C6H6
- SMILES
- c1ccccc1
- Mol. Weight (g/mol)
- 78.11
- CAS
- 71-43-2
- 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
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Datasets
Activity coefficient of Benzene (1) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Benzene (1) - Liquid |
|---|---|
| 333.20 | 3.91 |
| 348.20 | 3.86 |
| 363.20 | 3.36 |
Activity coefficient of Benzene (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Benzene (1) - Liquid |
|---|---|
| 323.15 | 4.6238 |
| 333.15 | 4.3759 |
| 343.15 | 4.2634 |
| 353.15 | 4.1021 |
| 363.15 | 3.9713 |
| 373.10 | 3.9159 |
| 383.15 | 3.8227 |
| 393.15 | 3.755 |
Activity coefficient of Benzene (1) [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Benzene (1) - Liquid |
|---|---|
| 333.20 | 3.91 |
| 348.20 | 3.86 |
| 363.20 | 3.36 |
Activity coefficient of Benzene (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Benzene (1) - Liquid |
|---|---|
| 323.15 | 4.6238 |
| 333.15 | 4.3759 |
| 343.15 | 4.2634 |
| 353.15 | 4.1021 |
| 363.15 | 3.9713 |
| 373.10 | 3.9159 |
| 383.15 | 3.8227 |
| 393.15 | 3.755 |
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 |
|---|---|
| 295.05 | 0.1080 |
| 297.85 | 0.1320 |
| 299.45 | 0.1480 |
| 300.35 | 0.1570 |
| 301.35 | 0.1680 |
| 302.05 | 0.1810 |
| 302.45 | 0.1950 |
| 302.95 | 0.2130 |
| 303.05 | 0.2200 |
| 303.05 | 0.2290 |
| 303.05 | 0.2370 |
| 302.85 | 0.2470 |
| 302.15 | 0.2580 |
| 301.75 | 0.2690 |
| 301.45 | 0.2810 |
| 300.95 | 0.2950 |
| 300.35 | 0.3100 |
| 299.95 | 0.3270 |
| 299.85 | 0.3360 |
| 299.15 | 0.3460 |
| 298.25 | 0.3560 |
| 297.75 | 0.3660 |
| 297.25 | 0.3780 |
| 296.85 | 0.3900 |
| 296.25 | 0.4030 |
| 295.65 | 0.4170 |
| 294.75 | 0.4310 |
| 293.85 | 0.4470 |
| 292.05 | 0.4640 |
| 289.65 | 0.4830 |
| 286.65 | 0.5030 |
| 279.65 | 0.5250 |
Mole fraction of Benzene (1) [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid mixture 1 | Pressure, kPa - Liquid mixture 1 | Mole fraction of Benzene (1) - Liquid mixture 1 |
| 298.20 | 101.00 | 0.0230 |
Mole fraction of Benzene (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Benzene (1) - Liquid mixture 1 |
|---|---|
| 279.60 | 0.6342 |
| 281.60 | 0.6438 |
| 283.00 | 0.6488 |
| 284.30 | 0.6593 |
| 287.60 | 0.6732 |
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 |
|---|---|
| 279.60 | 0.0706 |
| 281.60 | 0.0722 |
| 283.00 | 0.0770 |
| 284.30 | 0.0804 |
| 287.60 | 0.1095 |
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 |
|---|---|
| 295.05 | 0.1080 |
| 297.85 | 0.1320 |
| 299.45 | 0.1480 |
| 300.35 | 0.1570 |
| 301.35 | 0.1680 |
| 302.05 | 0.1810 |
| 302.45 | 0.1950 |
| 302.95 | 0.2130 |
| 303.05 | 0.2200 |
| 303.05 | 0.2290 |
| 303.05 | 0.2370 |
| 302.85 | 0.2470 |
| 302.15 | 0.2580 |
| 301.75 | 0.2690 |
| 301.45 | 0.2810 |
| 300.95 | 0.2950 |
| 300.35 | 0.3100 |
| 299.95 | 0.3270 |
| 299.85 | 0.3360 |
| 299.15 | 0.3460 |
| 298.25 | 0.3560 |
| 297.75 | 0.3660 |
| 297.25 | 0.3780 |
| 296.85 | 0.3900 |
| 296.25 | 0.4030 |
| 295.65 | 0.4170 |
| 294.75 | 0.4310 |
| 293.85 | 0.4470 |
| 292.05 | 0.4640 |
| 289.65 | 0.4830 |
| 286.65 | 0.5030 |
| 279.65 | 0.5250 |
Mole fraction of Benzene (1) [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid mixture 1 | Pressure, kPa - Liquid mixture 1 | Mole fraction of Benzene (1) - Liquid mixture 1 |
| 298.20 | 101.00 | 0.0230 |
Mole fraction of Benzene (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Benzene (1) - Liquid mixture 1 |
|---|---|
| 279.60 | 0.6342 |
| 281.60 | 0.6438 |
| 283.00 | 0.6488 |
| 284.30 | 0.6593 |
| 287.60 | 0.6732 |
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 |
|---|---|
| 279.60 | 0.0706 |
| 281.60 | 0.0722 |
| 283.00 | 0.0770 |
| 284.30 | 0.0804 |
| 287.60 | 0.1095 |
Sources
- Liquid-liquid phase diagrams of poly(ethylene glycol) and aromatic hydrocarbons
- Effective extraction of benzene and thiophene by novel deep eutectic solvents from hexane / aromatic mixture at different temperatures
- 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