Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzaldehyde (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.3627 | 279.16 |
| 0.3852 | 280.03 |
| 0.4281 | 281.75 |
| 0.4302 | 281.82 |
| 0.4509 | 282.40 |
| 0.5040 | 283.92 |
| 0.5253 | 283.97 |
| 0.5542 | 284.65 |
| 0.5586 | 284.60 |
| 0.5841 | 284.79 |
| 0.5946 | 284.70 |
| 0.5981 | 284.72 |
| 0.6099 | 284.67 |
| 0.6299 | 284.61 |
| 0.6328 | 284.79 |
| 0.6555 | 284.77 |
| 0.6683 | 284.70 |
| 0.6811 | 284.74 |
| 0.6943 | 284.62 |
| 0.7173 | 284.32 |
| 0.7364 | 284.14 |
| 0.7394 | 284.26 |
| 0.7577 | 284.01 |
| 0.7759 | 283.29 |
| 0.7863 | 282.86 |
| 0.8071 | 281.61 |
| 0.8248 | 280.13 |
| 0.8297 | 279.83 |
| 0.8362 | 279.10 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
| Mole fraction of Benzaldehyde (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
|---|---|
| 0.3627 | 279.16 |
| 0.3852 | 280.03 |
| 0.4281 | 281.75 |
| 0.4302 | 281.82 |
| 0.4509 | 282.40 |
| 0.5040 | 283.92 |
| 0.5253 | 283.97 |
| 0.5542 | 284.65 |
| 0.5586 | 284.60 |
| 0.5841 | 284.79 |
| 0.5946 | 284.70 |
| 0.5981 | 284.72 |
| 0.6099 | 284.67 |
| 0.6299 | 284.61 |
| 0.6328 | 284.79 |
| 0.6555 | 284.77 |
| 0.6683 | 284.70 |
| 0.6811 | 284.74 |
| 0.6943 | 284.62 |
| 0.7173 | 284.32 |
| 0.7364 | 284.14 |
| 0.7394 | 284.26 |
| 0.7577 | 284.01 |
| 0.7759 | 283.29 |
| 0.7863 | 282.86 |
| 0.8071 | 281.61 |
| 0.8248 | 280.13 |
| 0.8297 | 279.83 |
| 0.8362 | 279.10 |