Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
---|---|
298.15 | 0.0041 |
303.15 | 0.0042 |
308.15 | 0.0044 |
313.15 | 0.0044 |
318.15 | 0.0046 |
323.15 | 0.0049 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 |
---|---|
298.15 | 0.5209 |
303.15 | 0.5087 |
308.15 | 0.4998 |
313.15 | 0.4859 |
318.15 | 0.4692 |
323.15 | 0.4573 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 | Mass fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 |
---|---|
323.15 | 0.8441 |
298.15 | 0.8647 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 | Mass fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
---|---|
323.15 | 0.0272 |
298.15 | 0.0237 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 |
---|---|
333.20 | 0.4690 |
343.20 | 0.4509 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
---|---|
333.20 | 0.0051 |
343.20 | 0.0062 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
---|---|
298.15 | 0.0041 |
303.15 | 0.0042 |
308.15 | 0.0044 |
313.15 | 0.0044 |
318.15 | 0.0046 |
323.15 | 0.0049 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 |
---|---|
298.15 | 0.5209 |
303.15 | 0.5087 |
308.15 | 0.4998 |
313.15 | 0.4859 |
318.15 | 0.4692 |
323.15 | 0.4573 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 | Mass fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 |
---|---|
323.15 | 0.8441 |
298.15 | 0.8647 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 | Mass fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
---|---|
323.15 | 0.0272 |
298.15 | 0.0237 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 |
---|---|
333.20 | 0.4690 |
343.20 | 0.4509 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
---|---|
333.20 | 0.0051 |
343.20 | 0.0062 |
Operational conditions:
Mole fraction of Phenol, 3-methyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.5470 | 1020.94 |
0.5754 | 1021.37 |
0.6312 | 1022.09 |
0.6558 | 1022.4 |
0.7040 | 1022.95 |
0.7933 | 1023.97 |
0.7997 | 1024.04 |
0.8215 | 1024.36 |
0.8450 | 1024.52 |
0.8635 | 1024.3 |
0.8759 | 1024.67 |
0.8839 | 1024.94 |
0.9231 | 1025.3 |
0.9426 | 1025.49 |
0.9703 | 1025.78 |
Operational conditions:
Mole fraction of Phenol, 3-methyl- (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.5470 | 1020.94 |
0.5754 | 1021.37 |
0.6312 | 1022.09 |
0.6558 | 1022.4 |
0.7040 | 1022.95 |
0.7933 | 1023.97 |
0.7997 | 1024.04 |
0.8215 | 1024.36 |
0.8450 | 1024.52 |
0.8635 | 1024.3 |
0.8759 | 1024.67 |
0.8839 | 1024.94 |
0.9231 | 1025.3 |
0.9426 | 1025.49 |
0.9703 | 1025.78 |