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 |