Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mass fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 2 | Mass fraction of Phenol, 3-methyl- (2) - Liquid mixture 2 | Mass fraction of Phenol, 3-methyl- (2) - Liquid mixture 1 | Mass fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 1 |
298.20 | 0.0619 | 0.0000 | 0.0000 | 0.9653 |
313.20 | 0.0099 | 0.0051 | 0.5290 | 0.3878 |
298.20 | 0.0447 | 0.0003 | 0.1125 | 0.8436 |
298.20 | 0.0370 | 0.0006 | 0.1924 | 0.7585 |
298.20 | 0.0305 | 0.0009 | 0.2588 | 0.6878 |
298.20 | 0.0272 | 0.0012 | 0.2995 | 0.6435 |
298.20 | 0.0234 | 0.0019 | 0.3640 | 0.5731 |
298.20 | 0.0193 | 0.0028 | 0.4275 | 0.5065 |
298.20 | 0.0166 | 0.0035 | 0.4658 | 0.4645 |
298.20 | 0.0124 | 0.0043 | 0.5026 | 0.4243 |
313.20 | 0.0496 | 0.0000 | 0.0000 | 0.9598 |
313.20 | 0.0361 | 0.0003 | 0.1079 | 0.8441 |
313.20 | 0.0282 | 0.0007 | 0.1921 | 0.7526 |
313.20 | 0.0247 | 0.0011 | 0.2565 | 0.6837 |
313.20 | 0.0219 | 0.0018 | 0.3310 | 0.6029 |
313.20 | 0.0166 | 0.0024 | 0.3792 | 0.5504 |
313.20 | 0.0148 | 0.0033 | 0.4367 | 0.4884 |
313.20 | 0.0119 | 0.0040 | 0.4769 | 0.4441 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 2 | Mole fraction of Phenol, 3-methyl- (2) - Liquid mixture 2 | Mole fraction of Phenol, 3-methyl- (2) - Liquid mixture 1 | Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 1 |
333.20 | 0.8307 | 0.0000 | 0.0000 | 0.0088 |
333.20 | 0.7410 | 0.0803 | 0.0001 | 0.0067 |
333.20 | 0.6463 | 0.1337 | 0.0002 | 0.0059 |
333.20 | 0.5739 | 0.1710 | 0.0003 | 0.0050 |
333.20 | 0.5104 | 0.2199 | 0.0004 | 0.0040 |
333.20 | 0.4433 | 0.2569 | 0.0006 | 0.0036 |
333.20 | 0.4078 | 0.2736 | 0.0009 | 0.0030 |
333.20 | 0.3581 | 0.2962 | 0.0013 | 0.0025 |
333.20 | 0.2830 | 0.3358 | 0.0015 | 0.0021 |
333.20 | 0.0000 | 0.4690 | 0.0051 | 0.0000 |
343.20 | 0.8115 | 0.0000 | 0.0000 | 0.0074 |
343.20 | 0.7702 | 0.0525 | 0.0001 | 0.0062 |
343.20 | 0.6839 | 0.0943 | 0.0003 | 0.0058 |
343.20 | 0.5958 | 0.1451 | 0.0005 | 0.0053 |
343.20 | 0.4925 | 0.2201 | 0.0007 | 0.0041 |
343.20 | 0.4048 | 0.2641 | 0.0010 | 0.0031 |
343.20 | 0.3627 | 0.2855 | 0.0012 | 0.0025 |
343.20 | 0.2895 | 0.3186 | 0.0013 | 0.0019 |
343.20 | 0.2379 | 0.3476 | 0.0016 | 0.0014 |
343.20 | 0.0000 | 0.4509 | 0.0062 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mass fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 2 | Mass fraction of Phenol, 3-methyl- (2) - Liquid mixture 2 | Mass fraction of Phenol, 3-methyl- (2) - Liquid mixture 1 | Mass fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 1 |
298.20 | 0.0619 | 0.0000 | 0.0000 | 0.9653 |
313.20 | 0.0099 | 0.0051 | 0.5290 | 0.3878 |
298.20 | 0.0447 | 0.0003 | 0.1125 | 0.8436 |
298.20 | 0.0370 | 0.0006 | 0.1924 | 0.7585 |
298.20 | 0.0305 | 0.0009 | 0.2588 | 0.6878 |
298.20 | 0.0272 | 0.0012 | 0.2995 | 0.6435 |
298.20 | 0.0234 | 0.0019 | 0.3640 | 0.5731 |
298.20 | 0.0193 | 0.0028 | 0.4275 | 0.5065 |
298.20 | 0.0166 | 0.0035 | 0.4658 | 0.4645 |
298.20 | 0.0124 | 0.0043 | 0.5026 | 0.4243 |
313.20 | 0.0496 | 0.0000 | 0.0000 | 0.9598 |
313.20 | 0.0361 | 0.0003 | 0.1079 | 0.8441 |
313.20 | 0.0282 | 0.0007 | 0.1921 | 0.7526 |
313.20 | 0.0247 | 0.0011 | 0.2565 | 0.6837 |
313.20 | 0.0219 | 0.0018 | 0.3310 | 0.6029 |
313.20 | 0.0166 | 0.0024 | 0.3792 | 0.5504 |
313.20 | 0.0148 | 0.0033 | 0.4367 | 0.4884 |
313.20 | 0.0119 | 0.0040 | 0.4769 | 0.4441 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 2 | Mole fraction of Phenol, 3-methyl- (2) - Liquid mixture 2 | Mole fraction of Phenol, 3-methyl- (2) - Liquid mixture 1 | Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 1 |
333.20 | 0.8307 | 0.0000 | 0.0000 | 0.0088 |
333.20 | 0.7410 | 0.0803 | 0.0001 | 0.0067 |
333.20 | 0.6463 | 0.1337 | 0.0002 | 0.0059 |
333.20 | 0.5739 | 0.1710 | 0.0003 | 0.0050 |
333.20 | 0.5104 | 0.2199 | 0.0004 | 0.0040 |
333.20 | 0.4433 | 0.2569 | 0.0006 | 0.0036 |
333.20 | 0.4078 | 0.2736 | 0.0009 | 0.0030 |
333.20 | 0.3581 | 0.2962 | 0.0013 | 0.0025 |
333.20 | 0.2830 | 0.3358 | 0.0015 | 0.0021 |
333.20 | 0.0000 | 0.4690 | 0.0051 | 0.0000 |
343.20 | 0.8115 | 0.0000 | 0.0000 | 0.0074 |
343.20 | 0.7702 | 0.0525 | 0.0001 | 0.0062 |
343.20 | 0.6839 | 0.0943 | 0.0003 | 0.0058 |
343.20 | 0.5958 | 0.1451 | 0.0005 | 0.0053 |
343.20 | 0.4925 | 0.2201 | 0.0007 | 0.0041 |
343.20 | 0.4048 | 0.2641 | 0.0010 | 0.0031 |
343.20 | 0.3627 | 0.2855 | 0.0012 | 0.0025 |
343.20 | 0.2895 | 0.3186 | 0.0013 | 0.0019 |
343.20 | 0.2379 | 0.3476 | 0.0016 | 0.0014 |
343.20 | 0.0000 | 0.4509 | 0.0062 | 0.0000 |