Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Mole fraction of Benzaldehyde (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.4279 | 286.71 |
0.4590 | 289.85 |
0.4839 | 291.95 |
0.5180 | 294.23 |
0.5257 | 294.70 |
0.5485 | 295.64 |
0.5653 | 296.49 |
0.5807 | 296.87 |
0.5927 | 297.18 |
0.6005 | 297.09 |
0.6035 | 297.27 |
0.6061 | 297.24 |
0.6165 | 297.45 |
0.6376 | 297.75 |
0.6556 | 297.94 |
0.6783 | 298.08 |
0.6910 | 298.08 |
0.7155 | 298.11 |
0.7489 | 297.94 |
0.7543 | 297.97 |
0.7640 | 297.99 |
0.7926 | 297.73 |
0.8488 | 295.67 |
0.8509 | 295.70 |
0.8528 | 295.53 |
0.8720 | 293.27 |
0.8851 | 290.58 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Mole fraction of Benzaldehyde (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.4279 | 286.71 |
0.4590 | 289.85 |
0.4839 | 291.95 |
0.5180 | 294.23 |
0.5257 | 294.70 |
0.5485 | 295.64 |
0.5653 | 296.49 |
0.5807 | 296.87 |
0.5927 | 297.18 |
0.6005 | 297.09 |
0.6035 | 297.27 |
0.6061 | 297.24 |
0.6165 | 297.45 |
0.6376 | 297.75 |
0.6556 | 297.94 |
0.6783 | 298.08 |
0.6910 | 298.08 |
0.7155 | 298.11 |
0.7489 | 297.94 |
0.7543 | 297.97 |
0.7640 | 297.99 |
0.7926 | 297.73 |
0.8488 | 295.67 |
0.8509 | 295.70 |
0.8528 | 295.53 |
0.8720 | 293.27 |
0.8851 | 290.58 |