Operational conditions:
| Temperature, K - Liquid | Activity coefficient of Ethylbenzene (2) - Liquid |
|---|---|
| 333.20 | 8.63 |
| 348.20 | 8.21 |
| 363.20 | 7.86 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Ethylbenzene (2) - Liquid |
|---|---|
| 323.15 | 10.8636 |
| 333.15 | 10.2807 |
| 343.15 | 9.7303 |
| 353.15 | 9.1046 |
| 363.15 | 8.7188 |
| 373.10 | 8.3906 |
| 383.15 | 7.942 |
| 393.15 | 7.7208 |
Operational conditions:
| Temperature, K - Liquid | Activity coefficient of Ethylbenzene (2) - Liquid |
|---|---|
| 333.20 | 8.63 |
| 348.20 | 8.21 |
| 363.20 | 7.86 |
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Ethylbenzene (2) - Liquid |
|---|---|
| 323.15 | 10.8636 |
| 333.15 | 10.2807 |
| 343.15 | 9.7303 |
| 353.15 | 9.1046 |
| 363.15 | 8.7188 |
| 373.10 | 8.3906 |
| 383.15 | 7.942 |
| 393.15 | 7.7208 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Triethylene glycol (1) - Liquid mixture 1 |
|---|---|
| 366.55 | 0.0870 |
| 369.05 | 0.0970 |
| 371.55 | 0.1080 |
| 374.65 | 0.1230 |
| 377.15 | 0.1420 |
| 379.95 | 0.1680 |
| 382.15 | 0.2060 |
| 383.55 | 0.2330 |
| 384.05 | 0.2670 |
| 384.55 | 0.3130 |
| 384.25 | 0.3780 |
| 383.15 | 0.4760 |
| 381.15 | 0.5320 |
| 373.15 | 0.6030 |
| 356.15 | 0.6950 |
| 298.15 | 0.8200 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Triethylene glycol (1) - Liquid mixture 1 |
|---|---|
| 366.55 | 0.0870 |
| 369.05 | 0.0970 |
| 371.55 | 0.1080 |
| 374.65 | 0.1230 |
| 377.15 | 0.1420 |
| 379.95 | 0.1680 |
| 382.15 | 0.2060 |
| 383.55 | 0.2330 |
| 384.05 | 0.2670 |
| 384.55 | 0.3130 |
| 384.25 | 0.3780 |
| 383.15 | 0.4760 |
| 381.15 | 0.5320 |
| 373.15 | 0.6030 |
| 356.15 | 0.6950 |
| 298.15 | 0.8200 |