Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Acetic acid, phenylmethyl ester (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.3430 | 275.61 |
| 0.3620 | 276.70 |
| 0.3792 | 277.46 |
| 0.4232 | 278.97 |
| 0.4506 | 279.65 |
| 0.4755 | 280.10 |
| 0.5014 | 280.44 |
| 0.5268 | 280.58 |
| 0.5636 | 280.77 |
| 0.5761 | 280.80 |
| 0.5997 | 280.75 |
| 0.6251 | 280.77 |
| 0.6543 | 280.72 |
| 0.6822 | 280.61 |
| 0.7023 | 280.42 |
| 0.7167 | 280.27 |
| 0.7467 | 279.97 |
| 0.7656 | 279.27 |
| 0.7994 | 277.76 |
| 0.8201 | 276.50 |
| 0.8500 | 273.60 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Acetic acid, phenylmethyl ester (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.3430 | 275.61 |
| 0.3620 | 276.70 |
| 0.3792 | 277.46 |
| 0.4232 | 278.97 |
| 0.4506 | 279.65 |
| 0.4755 | 280.10 |
| 0.5014 | 280.44 |
| 0.5268 | 280.58 |
| 0.5636 | 280.77 |
| 0.5761 | 280.80 |
| 0.5997 | 280.75 |
| 0.6251 | 280.77 |
| 0.6543 | 280.72 |
| 0.6822 | 280.61 |
| 0.7023 | 280.42 |
| 0.7167 | 280.27 |
| 0.7467 | 279.97 |
| 0.7656 | 279.27 |
| 0.7994 | 277.76 |
| 0.8201 | 276.50 |
| 0.8500 | 273.60 |