Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mass fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 1 | Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 | Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 | Mass fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 2 |
298.20 | 0.6395 | 0.3188 | 0.0022 | 0.0083 |
298.20 | 0.9853 | 0.0000 | 0.0000 | 0.0171 |
313.20 | 0.6287 | 0.3259 | 0.0022 | 0.0080 |
313.20 | 0.6631 | 0.2938 | 0.0019 | 0.0089 |
313.20 | 0.7139 | 0.2453 | 0.0015 | 0.0092 |
313.20 | 0.7390 | 0.2255 | 0.0012 | 0.0103 |
313.20 | 0.7658 | 0.2021 | 0.0010 | 0.0105 |
313.20 | 0.7938 | 0.1752 | 0.0008 | 0.0113 |
313.20 | 0.8127 | 0.1576 | 0.0006 | 0.0118 |
313.20 | 0.8338 | 0.1375 | 0.0005 | 0.0121 |
313.20 | 0.8532 | 0.1205 | 0.0004 | 0.0125 |
298.20 | 0.6564 | 0.3030 | 0.0018 | 0.0087 |
313.20 | 0.9827 | 0.0000 | 0.0000 | 0.0159 |
323.20 | 0.6702 | 0.2842 | 0.0021 | 0.0085 |
323.20 | 0.6973 | 0.2578 | 0.0016 | 0.0088 |
323.20 | 0.7252 | 0.2311 | 0.0013 | 0.0093 |
323.20 | 0.7496 | 0.2091 | 0.0011 | 0.0095 |
323.20 | 0.7716 | 0.1883 | 0.0009 | 0.0105 |
323.20 | 0.7967 | 0.1658 | 0.0007 | 0.0108 |
323.20 | 0.8167 | 0.1492 | 0.0006 | 0.0113 |
323.20 | 0.8296 | 0.1370 | 0.0005 | 0.0117 |
323.20 | 0.8542 | 0.1147 | 0.0004 | 0.0120 |
298.20 | 0.6884 | 0.2763 | 0.0015 | 0.0093 |
323.20 | 0.9807 | 0.0000 | 0.0000 | 0.0141 |
298.20 | 0.6975 | 0.2690 | 0.0014 | 0.0098 |
298.20 | 0.7251 | 0.2435 | 0.0011 | 0.0109 |
298.20 | 0.7319 | 0.2372 | 0.0010 | 0.0120 |
298.20 | 0.7378 | 0.2316 | 0.0009 | 0.0124 |
298.20 | 0.7624 | 0.2086 | 0.0008 | 0.0135 |
298.20 | 0.7771 | 0.1945 | 0.0007 | 0.0140 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 | Mole fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 1 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 | Mole fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 2 |
333.20 | 0.0001 | 0.0021 | 0.0518 | 0.8032 |
353.20 | 0.0003 | 0.0022 | 0.1581 | 0.5991 |
353.20 | 0.0004 | 0.0022 | 0.2174 | 0.5197 |
353.20 | 0.0007 | 0.0021 | 0.2770 | 0.3916 |
353.20 | 0.0011 | 0.0021 | 0.3005 | 0.3426 |
353.20 | 0.0019 | 0.0020 | 0.3291 | 0.2791 |
353.20 | 0.0026 | 0.0018 | 0.3488 | 0.2371 |
333.20 | 0.0001 | 0.0021 | 0.0871 | 0.7295 |
333.20 | 0.0002 | 0.0020 | 0.1744 | 0.5813 |
333.20 | 0.0003 | 0.0020 | 0.2279 | 0.4921 |
333.20 | 0.0005 | 0.0018 | 0.2903 | 0.3883 |
333.20 | 0.0008 | 0.0015 | 0.3190 | 0.3321 |
333.20 | 0.0016 | 0.0013 | 0.3653 | 0.2529 |
333.20 | 0.0020 | 0.0011 | 0.3966 | 0.1965 |
353.20 | 0.0001 | 0.0023 | 0.0466 | 0.8029 |
353.20 | 0.0001 | 0.0022 | 0.0855 | 0.7327 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mass fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 1 | Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 | Mass fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 | Mass fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 2 |
298.20 | 0.6395 | 0.3188 | 0.0022 | 0.0083 |
298.20 | 0.9853 | 0.0000 | 0.0000 | 0.0171 |
313.20 | 0.6287 | 0.3259 | 0.0022 | 0.0080 |
313.20 | 0.6631 | 0.2938 | 0.0019 | 0.0089 |
313.20 | 0.7139 | 0.2453 | 0.0015 | 0.0092 |
313.20 | 0.7390 | 0.2255 | 0.0012 | 0.0103 |
313.20 | 0.7658 | 0.2021 | 0.0010 | 0.0105 |
313.20 | 0.7938 | 0.1752 | 0.0008 | 0.0113 |
313.20 | 0.8127 | 0.1576 | 0.0006 | 0.0118 |
313.20 | 0.8338 | 0.1375 | 0.0005 | 0.0121 |
313.20 | 0.8532 | 0.1205 | 0.0004 | 0.0125 |
298.20 | 0.6564 | 0.3030 | 0.0018 | 0.0087 |
313.20 | 0.9827 | 0.0000 | 0.0000 | 0.0159 |
323.20 | 0.6702 | 0.2842 | 0.0021 | 0.0085 |
323.20 | 0.6973 | 0.2578 | 0.0016 | 0.0088 |
323.20 | 0.7252 | 0.2311 | 0.0013 | 0.0093 |
323.20 | 0.7496 | 0.2091 | 0.0011 | 0.0095 |
323.20 | 0.7716 | 0.1883 | 0.0009 | 0.0105 |
323.20 | 0.7967 | 0.1658 | 0.0007 | 0.0108 |
323.20 | 0.8167 | 0.1492 | 0.0006 | 0.0113 |
323.20 | 0.8296 | 0.1370 | 0.0005 | 0.0117 |
323.20 | 0.8542 | 0.1147 | 0.0004 | 0.0120 |
298.20 | 0.6884 | 0.2763 | 0.0015 | 0.0093 |
323.20 | 0.9807 | 0.0000 | 0.0000 | 0.0141 |
298.20 | 0.6975 | 0.2690 | 0.0014 | 0.0098 |
298.20 | 0.7251 | 0.2435 | 0.0011 | 0.0109 |
298.20 | 0.7319 | 0.2372 | 0.0010 | 0.0120 |
298.20 | 0.7378 | 0.2316 | 0.0009 | 0.0124 |
298.20 | 0.7624 | 0.2086 | 0.0008 | 0.0135 |
298.20 | 0.7771 | 0.1945 | 0.0007 | 0.0140 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 | Mole fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 1 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 | Mole fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 2 |
333.20 | 0.0001 | 0.0021 | 0.0518 | 0.8032 |
353.20 | 0.0003 | 0.0022 | 0.1581 | 0.5991 |
353.20 | 0.0004 | 0.0022 | 0.2174 | 0.5197 |
353.20 | 0.0007 | 0.0021 | 0.2770 | 0.3916 |
353.20 | 0.0011 | 0.0021 | 0.3005 | 0.3426 |
353.20 | 0.0019 | 0.0020 | 0.3291 | 0.2791 |
353.20 | 0.0026 | 0.0018 | 0.3488 | 0.2371 |
333.20 | 0.0001 | 0.0021 | 0.0871 | 0.7295 |
333.20 | 0.0002 | 0.0020 | 0.1744 | 0.5813 |
333.20 | 0.0003 | 0.0020 | 0.2279 | 0.4921 |
333.20 | 0.0005 | 0.0018 | 0.2903 | 0.3883 |
333.20 | 0.0008 | 0.0015 | 0.3190 | 0.3321 |
333.20 | 0.0016 | 0.0013 | 0.3653 | 0.2529 |
333.20 | 0.0020 | 0.0011 | 0.3966 | 0.1965 |
353.20 | 0.0001 | 0.0023 | 0.0466 | 0.8029 |
353.20 | 0.0001 | 0.0022 | 0.0855 | 0.7327 |