Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mass fraction of 2-Hexanone (2) - Liquid mixture 2 | Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 | Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 | Mass fraction of 2-Hexanone (2) - Liquid mixture 1 |
298.20 | 0.9773 | 0.0000 | 0.0000 | 0.0158 |
298.20 | 0.8342 | 0.1316 | 0.0004 | 0.0118 |
298.20 | 0.7884 | 0.1734 | 0.0006 | 0.0106 |
298.20 | 0.7673 | 0.1929 | 0.0007 | 0.0101 |
298.20 | 0.7503 | 0.2084 | 0.0008 | 0.0098 |
298.20 | 0.7152 | 0.2404 | 0.0010 | 0.0092 |
298.20 | 0.6761 | 0.2768 | 0.0014 | 0.0085 |
298.20 | 0.6114 | 0.3371 | 0.0022 | 0.0072 |
298.20 | 0.5827 | 0.3638 | 0.0026 | 0.0066 |
313.20 | 0.9732 | 0.0000 | 0.0000 | 0.0120 |
313.20 | 0.8324 | 0.1262 | 0.0004 | 0.0093 |
313.20 | 0.7855 | 0.1683 | 0.0007 | 0.0084 |
313.20 | 0.7570 | 0.1939 | 0.0008 | 0.0079 |
313.20 | 0.7280 | 0.2201 | 0.0010 | 0.0075 |
313.20 | 0.6941 | 0.2506 | 0.0014 | 0.0069 |
313.20 | 0.6746 | 0.2681 | 0.0015 | 0.0065 |
313.20 | 0.6467 | 0.2936 | 0.0019 | 0.0061 |
313.20 | 0.5832 | 0.3515 | 0.0027 | 0.0051 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Hexanone (2) - Liquid mixture 2 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 | Mole fraction of 2-Hexanone (2) - Liquid mixture 1 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 |
333.20 | 0.6774 | 0.0912 | 0.0018 | 0.0001 |
333.20 | 0.6219 | 0.1232 | 0.0018 | 0.0002 |
333.20 | 0.5721 | 0.1514 | 0.0017 | 0.0002 |
333.20 | 0.5269 | 0.1787 | 0.0017 | 0.0003 |
333.20 | 0.4850 | 0.2049 | 0.0016 | 0.0004 |
333.20 | 0.4364 | 0.2344 | 0.0016 | 0.0005 |
333.20 | 0.3999 | 0.2564 | 0.0015 | 0.0006 |
333.20 | 0.3272 | 0.3015 | 0.0013 | 0.0009 |
353.20 | 0.6624 | 0.0834 | 0.0019 | 0.0001 |
353.20 | 0.6050 | 0.1162 | 0.0018 | 0.0002 |
353.20 | 0.5748 | 0.1333 | 0.0018 | 0.0002 |
353.20 | 0.5036 | 0.1761 | 0.0017 | 0.0004 |
353.20 | 0.4612 | 0.1999 | 0.0017 | 0.0005 |
353.20 | 0.4149 | 0.2290 | 0.0016 | 0.0007 |
353.20 | 0.3597 | 0.2548 | 0.0015 | 0.0009 |
353.20 | 0.3011 | 0.2895 | 0.0013 | 0.0011 |
333.20 | 0.8530 | 0.0000 | 0.0020 | 0.0000 |
353.20 | 0.8360 | 0.0000 | 0.0020 | 0.0000 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mass fraction of 2-Hexanone (2) - Liquid mixture 2 | Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 | Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 | Mass fraction of 2-Hexanone (2) - Liquid mixture 1 |
298.20 | 0.9773 | 0.0000 | 0.0000 | 0.0158 |
298.20 | 0.8342 | 0.1316 | 0.0004 | 0.0118 |
298.20 | 0.7884 | 0.1734 | 0.0006 | 0.0106 |
298.20 | 0.7673 | 0.1929 | 0.0007 | 0.0101 |
298.20 | 0.7503 | 0.2084 | 0.0008 | 0.0098 |
298.20 | 0.7152 | 0.2404 | 0.0010 | 0.0092 |
298.20 | 0.6761 | 0.2768 | 0.0014 | 0.0085 |
298.20 | 0.6114 | 0.3371 | 0.0022 | 0.0072 |
298.20 | 0.5827 | 0.3638 | 0.0026 | 0.0066 |
313.20 | 0.9732 | 0.0000 | 0.0000 | 0.0120 |
313.20 | 0.8324 | 0.1262 | 0.0004 | 0.0093 |
313.20 | 0.7855 | 0.1683 | 0.0007 | 0.0084 |
313.20 | 0.7570 | 0.1939 | 0.0008 | 0.0079 |
313.20 | 0.7280 | 0.2201 | 0.0010 | 0.0075 |
313.20 | 0.6941 | 0.2506 | 0.0014 | 0.0069 |
313.20 | 0.6746 | 0.2681 | 0.0015 | 0.0065 |
313.20 | 0.6467 | 0.2936 | 0.0019 | 0.0061 |
313.20 | 0.5832 | 0.3515 | 0.0027 | 0.0051 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Hexanone (2) - Liquid mixture 2 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 | Mole fraction of 2-Hexanone (2) - Liquid mixture 1 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 |
333.20 | 0.6774 | 0.0912 | 0.0018 | 0.0001 |
333.20 | 0.6219 | 0.1232 | 0.0018 | 0.0002 |
333.20 | 0.5721 | 0.1514 | 0.0017 | 0.0002 |
333.20 | 0.5269 | 0.1787 | 0.0017 | 0.0003 |
333.20 | 0.4850 | 0.2049 | 0.0016 | 0.0004 |
333.20 | 0.4364 | 0.2344 | 0.0016 | 0.0005 |
333.20 | 0.3999 | 0.2564 | 0.0015 | 0.0006 |
333.20 | 0.3272 | 0.3015 | 0.0013 | 0.0009 |
353.20 | 0.6624 | 0.0834 | 0.0019 | 0.0001 |
353.20 | 0.6050 | 0.1162 | 0.0018 | 0.0002 |
353.20 | 0.5748 | 0.1333 | 0.0018 | 0.0002 |
353.20 | 0.5036 | 0.1761 | 0.0017 | 0.0004 |
353.20 | 0.4612 | 0.1999 | 0.0017 | 0.0005 |
353.20 | 0.4149 | 0.2290 | 0.0016 | 0.0007 |
353.20 | 0.3597 | 0.2548 | 0.0015 | 0.0009 |
353.20 | 0.3011 | 0.2895 | 0.0013 | 0.0011 |
333.20 | 0.8530 | 0.0000 | 0.0020 | 0.0000 |
353.20 | 0.8360 | 0.0000 | 0.0020 | 0.0000 |