Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Mole fraction of 2-Butanone, 4-phenyl- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2262 | 285.80 |
0.2421 | 287.30 |
0.2911 | 291.60 |
0.3173 | 293.40 |
0.3346 | 294.70 |
0.3524 | 295.50 |
0.3731 | 296.40 |
0.3958 | 297.40 |
0.4479 | 299.00 |
0.4610 | 299.30 |
0.5040 | 300.00 |
0.5259 | 300.10 |
0.5511 | 300.10 |
0.5826 | 300.00 |
0.5949 | 300.00 |
0.6374 | 299.90 |
0.6873 | 299.80 |
0.7021 | 299.70 |
0.7183 | 299.50 |
0.7218 | 299.40 |
0.7475 | 298.90 |
0.7740 | 297.10 |
0.7958 | 295.60 |
0.8233 | 293.60 |
0.8566 | 289.90 |
0.8629 | 289.00 |
0.8920 | 285.70 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 1)
Mole fraction of 2-Butanone, 4-phenyl- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2262 | 285.80 |
0.2421 | 287.30 |
0.2911 | 291.60 |
0.3173 | 293.40 |
0.3346 | 294.70 |
0.3524 | 295.50 |
0.3731 | 296.40 |
0.3958 | 297.40 |
0.4479 | 299.00 |
0.4610 | 299.30 |
0.5040 | 300.00 |
0.5259 | 300.10 |
0.5511 | 300.10 |
0.5826 | 300.00 |
0.5949 | 300.00 |
0.6374 | 299.90 |
0.6873 | 299.80 |
0.7021 | 299.70 |
0.7183 | 299.50 |
0.7218 | 299.40 |
0.7475 | 298.90 |
0.7740 | 297.10 |
0.7958 | 295.60 |
0.8233 | 293.60 |
0.8566 | 289.90 |
0.8629 | 289.00 |
0.8920 | 285.70 |