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 |
---|---|
0.3480 | 280.00 |
0.3762 | 281.90 |
0.4014 | 283.20 |
0.4429 | 285.10 |
0.4452 | 285.10 |
0.4756 | 286.20 |
0.5098 | 287.00 |
0.5244 | 287.30 |
0.5582 | 287.80 |
0.5780 | 287.90 |
0.5898 | 288.00 |
0.6211 | 288.10 |
0.6501 | 288.30 |
0.6619 | 288.20 |
0.6909 | 288.20 |
0.7069 | 288.10 |
0.7088 | 288.10 |
0.7198 | 288.10 |
0.7213 | 288.10 |
0.7619 | 287.70 |
0.7887 | 287.10 |
0.7958 | 286.90 |
0.8243 | 285.60 |
0.8476 | 283.20 |
0.8721 | 280.20 |
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 |
---|---|
0.3480 | 280.00 |
0.3762 | 281.90 |
0.4014 | 283.20 |
0.4429 | 285.10 |
0.4452 | 285.10 |
0.4756 | 286.20 |
0.5098 | 287.00 |
0.5244 | 287.30 |
0.5582 | 287.80 |
0.5780 | 287.90 |
0.5898 | 288.00 |
0.6211 | 288.10 |
0.6501 | 288.30 |
0.6619 | 288.20 |
0.6909 | 288.20 |
0.7069 | 288.10 |
0.7088 | 288.10 |
0.7198 | 288.10 |
0.7213 | 288.10 |
0.7619 | 287.70 |
0.7887 | 287.10 |
0.7958 | 286.90 |
0.8243 | 285.60 |
0.8476 | 283.20 |
0.8721 | 280.20 |