Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mass fraction of Toluene (1) - Liquid mixture 1 | Mass fraction of Phenol (3) - Liquid mixture 1 | Mass fraction of Phenol (3) - Liquid mixture 2 | Mass fraction of Toluene (1) - Liquid mixture 2 |
298.15 | 0.9114 | 0.0814 | 0.3750 | 0.5200 |
298.15 | 0.9678 | 0.0300 | 0.4542 | 0.3741 |
298.15 | 0.9860 | 0.0134 | 0.4826 | 0.2835 |
313.15 | 0.9045 | 0.0878 | 0.3669 | 0.5287 |
313.15 | 0.9579 | 0.0392 | 0.4442 | 0.3833 |
313.15 | 0.9827 | 0.0164 | 0.4756 | 0.2922 |
338.15 | 0.8874 | 0.1036 | 0.3520 | 0.5421 |
338.15 | 0.9505 | 0.0465 | 0.4256 | 0.4053 |
338.15 | 0.9773 | 0.0215 | 0.4682 | 0.2996 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mass fraction of Toluene (1) - Liquid mixture 1 | Mass fraction of Phenol (3) - Liquid mixture 1 | Mass fraction of Phenol (3) - Liquid mixture 2 | Mass fraction of Toluene (1) - Liquid mixture 2 |
298.15 | 0.9114 | 0.0814 | 0.3750 | 0.5200 |
298.15 | 0.9678 | 0.0300 | 0.4542 | 0.3741 |
298.15 | 0.9860 | 0.0134 | 0.4826 | 0.2835 |
313.15 | 0.9045 | 0.0878 | 0.3669 | 0.5287 |
313.15 | 0.9579 | 0.0392 | 0.4442 | 0.3833 |
313.15 | 0.9827 | 0.0164 | 0.4756 | 0.2922 |
338.15 | 0.8874 | 0.1036 | 0.3520 | 0.5421 |
338.15 | 0.9505 | 0.0465 | 0.4256 | 0.4053 |
338.15 | 0.9773 | 0.0215 | 0.4682 | 0.2996 |