Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 2 | Mole fraction of Phenol (2) - Liquid mixture 2 | Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 1 | Mole fraction of Phenol (2) - Liquid mixture 1 |
333.20 | 0.6944 | 0.0482 | 0.0043 | 0.0001 |
333.20 | 0.6003 | 0.0948 | 0.0042 | 0.0002 |
333.20 | 0.5056 | 0.1578 | 0.0039 | 0.0006 |
333.20 | 0.4354 | 0.1968 | 0.0033 | 0.0013 |
333.20 | 0.3636 | 0.2454 | 0.0027 | 0.0020 |
333.20 | 0.3043 | 0.2785 | 0.0024 | 0.0029 |
333.20 | 0.2324 | 0.3134 | 0.0015 | 0.0043 |
333.20 | 0.1824 | 0.3352 | 0.0010 | 0.0050 |
343.20 | 0.6525 | 0.0510 | 0.0050 | 0.0001 |
343.20 | 0.5857 | 0.0984 | 0.0048 | 0.0003 |
343.20 | 0.5246 | 0.1374 | 0.0046 | 0.0005 |
343.20 | 0.4437 | 0.1977 | 0.0035 | 0.0017 |
343.20 | 0.2888 | 0.2865 | 0.0022 | 0.0037 |
343.20 | 0.2049 | 0.3106 | 0.0009 | 0.0064 |
343.20 | 0.1217 | 0.3215 | 0.0006 | 0.0068 |
343.20 | 0.0829 | 0.3125 | 0.0007 | 0.0080 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mass fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 1 | Mass fraction of Phenol (2) - Liquid mixture 1 | Mass fraction of Phenol (2) - Liquid mixture 2 | Mass fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 2 |
298.15 | 0.0321 | 0.0050 | 0.3367 | 0.5897 |
298.15 | 0.0403 | 0.0026 | 0.2236 | 0.7151 |
298.15 | 0.0434 | 0.0020 | 0.1951 | 0.7483 |
298.15 | 0.0489 | 0.0012 | 0.1422 | 0.8072 |
298.15 | 0.0506 | 0.0010 | 0.1212 | 0.8321 |
298.15 | 0.0529 | 0.0007 | 0.0939 | 0.8619 |
298.15 | 0.0563 | 0.0003 | 0.0530 | 0.9078 |
298.15 | 0.0619 | 0.0000 | 0.0000 | 0.9653 |
313.15 | 0.0293 | 0.0045 | 0.2895 | 0.6379 |
313.15 | 0.0330 | 0.0032 | 0.2354 | 0.6983 |
313.15 | 0.0375 | 0.0020 | 0.1672 | 0.7751 |
313.15 | 0.0397 | 0.0015 | 0.1341 | 0.8110 |
313.15 | 0.0419 | 0.0010 | 0.0983 | 0.8523 |
313.15 | 0.0448 | 0.0005 | 0.0524 | 0.9028 |
313.15 | 0.0467 | 0.0002 | 0.0295 | 0.9274 |
313.15 | 0.0496 | 0.0000 | 0.0000 | 0.9598 |
323.15 | 0.0270 | 0.0052 | 0.3091 | 0.6102 |
323.15 | 0.0333 | 0.0033 | 0.2160 | 0.7165 |
323.15 | 0.0364 | 0.0024 | 0.1744 | 0.7651 |
323.15 | 0.0396 | 0.0016 | 0.1244 | 0.8201 |
323.15 | 0.0419 | 0.0010 | 0.0856 | 0.8641 |
323.15 | 0.0433 | 0.0007 | 0.0622 | 0.8895 |
323.15 | 0.0453 | 0.0002 | 0.0223 | 0.9308 |
323.15 | 0.0478 | 0.0000 | 0.0000 | 0.9559 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 1)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 2 | Mole fraction of Phenol (2) - Liquid mixture 2 | Mole fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 1 | Mole fraction of Phenol (2) - Liquid mixture 1 |
333.20 | 0.6944 | 0.0482 | 0.0043 | 0.0001 |
333.20 | 0.6003 | 0.0948 | 0.0042 | 0.0002 |
333.20 | 0.5056 | 0.1578 | 0.0039 | 0.0006 |
333.20 | 0.4354 | 0.1968 | 0.0033 | 0.0013 |
333.20 | 0.3636 | 0.2454 | 0.0027 | 0.0020 |
333.20 | 0.3043 | 0.2785 | 0.0024 | 0.0029 |
333.20 | 0.2324 | 0.3134 | 0.0015 | 0.0043 |
333.20 | 0.1824 | 0.3352 | 0.0010 | 0.0050 |
343.20 | 0.6525 | 0.0510 | 0.0050 | 0.0001 |
343.20 | 0.5857 | 0.0984 | 0.0048 | 0.0003 |
343.20 | 0.5246 | 0.1374 | 0.0046 | 0.0005 |
343.20 | 0.4437 | 0.1977 | 0.0035 | 0.0017 |
343.20 | 0.2888 | 0.2865 | 0.0022 | 0.0037 |
343.20 | 0.2049 | 0.3106 | 0.0009 | 0.0064 |
343.20 | 0.1217 | 0.3215 | 0.0006 | 0.0068 |
343.20 | 0.0829 | 0.3125 | 0.0007 | 0.0080 |
Operational condition: Pressure, kPa = 100 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mass fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 1 | Mass fraction of Phenol (2) - Liquid mixture 1 | Mass fraction of Phenol (2) - Liquid mixture 2 | Mass fraction of 2-Butanone, 3-methyl- (1) - Liquid mixture 2 |
298.15 | 0.0321 | 0.0050 | 0.3367 | 0.5897 |
298.15 | 0.0403 | 0.0026 | 0.2236 | 0.7151 |
298.15 | 0.0434 | 0.0020 | 0.1951 | 0.7483 |
298.15 | 0.0489 | 0.0012 | 0.1422 | 0.8072 |
298.15 | 0.0506 | 0.0010 | 0.1212 | 0.8321 |
298.15 | 0.0529 | 0.0007 | 0.0939 | 0.8619 |
298.15 | 0.0563 | 0.0003 | 0.0530 | 0.9078 |
298.15 | 0.0619 | 0.0000 | 0.0000 | 0.9653 |
313.15 | 0.0293 | 0.0045 | 0.2895 | 0.6379 |
313.15 | 0.0330 | 0.0032 | 0.2354 | 0.6983 |
313.15 | 0.0375 | 0.0020 | 0.1672 | 0.7751 |
313.15 | 0.0397 | 0.0015 | 0.1341 | 0.8110 |
313.15 | 0.0419 | 0.0010 | 0.0983 | 0.8523 |
313.15 | 0.0448 | 0.0005 | 0.0524 | 0.9028 |
313.15 | 0.0467 | 0.0002 | 0.0295 | 0.9274 |
313.15 | 0.0496 | 0.0000 | 0.0000 | 0.9598 |
323.15 | 0.0270 | 0.0052 | 0.3091 | 0.6102 |
323.15 | 0.0333 | 0.0033 | 0.2160 | 0.7165 |
323.15 | 0.0364 | 0.0024 | 0.1744 | 0.7651 |
323.15 | 0.0396 | 0.0016 | 0.1244 | 0.8201 |
323.15 | 0.0419 | 0.0010 | 0.0856 | 0.8641 |
323.15 | 0.0433 | 0.0007 | 0.0622 | 0.8895 |
323.15 | 0.0453 | 0.0002 | 0.0223 | 0.9308 |
323.15 | 0.0478 | 0.0000 | 0.0000 | 0.9559 |