Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Mole fraction of 1,1'-Biphenyl, 4,4'-dibromo- (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2000 | 453.15 |
0.2500 | 461.15 |
0.3000 | 471.15 |
0.3500 | 483.15 |
0.4000 | 493.15 |
0.4500 | 497.15 |
0.5000 | 503.15 |
0.5500 | 505.15 |
0.5750 | 505.15 |
0.6500 | 505.15 |
0.6750 | 504.15 |
0.7750 | 497.15 |
0.8500 | 491.15 |
0.9000 | 475.15 |
0.9200 | 466.15 |
0.9300 | 459.15 |
0.9400 | 453.15 |
0.9500 | 448.15 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Mole fraction of 1,1'-Biphenyl, 4,4'-dibromo- (2) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
---|---|
0.2000 | 453.15 |
0.2500 | 461.15 |
0.3000 | 471.15 |
0.3500 | 483.15 |
0.4000 | 493.15 |
0.4500 | 497.15 |
0.5000 | 503.15 |
0.5500 | 505.15 |
0.5750 | 505.15 |
0.6500 | 505.15 |
0.6750 | 504.15 |
0.7750 | 497.15 |
0.8500 | 491.15 |
0.9000 | 475.15 |
0.9200 | 466.15 |
0.9300 | 459.15 |
0.9400 | 453.15 |
0.9500 | 448.15 |
Operational condition: Pressure, kPa = 101 (Liquid)
Mole fraction of Butanedinitrile (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0500 | 439.15 |
0.1000 | 439.15 |
0.1500 | 438.15 |
Operational condition: Pressure, kPa = 101 (Liquid)
Mole fraction of Butanedinitrile (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.9600 | 423.15 |
0.9700 | 414.15 |
0.9800 | 398.15 |
0.9900 | 383.15 |
0.9950 | 357.15 |
0.9960 | 355.15 |
0.9970 | 348.15 |
0.9990 | 331.15 |
0.9996 | 329.15 |
0.9997 | 327.65 |
0.9999 | 328.65 |
Operational condition: Pressure, kPa = 101 (Liquid)
Mole fraction of Butanedinitrile (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.0500 | 439.15 |
0.1000 | 439.15 |
0.1500 | 438.15 |
Operational condition: Pressure, kPa = 101 (Liquid)
Mole fraction of Butanedinitrile (1) - Liquid | Solid-liquid equilibrium temperature, K - Liquid |
---|---|
0.9600 | 423.15 |
0.9700 | 414.15 |
0.9800 | 398.15 |
0.9900 | 383.15 |
0.9950 | 357.15 |
0.9960 | 355.15 |
0.9970 | 348.15 |
0.9990 | 331.15 |
0.9996 | 329.15 |
0.9997 | 327.65 |
0.9999 | 328.65 |