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, 3-methyl- (1) - Liquid mixture 1 | Mass fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 | Mass fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 2 |
298.20 | 0.6407 | 0.3172 | 0.0024 | 0.0079 |
298.20 | 0.9853 | 0.0000 | 0.0000 | 0.0171 |
313.20 | 0.6372 | 0.3185 | 0.0025 | 0.0077 |
313.20 | 0.6969 | 0.2617 | 0.0019 | 0.0075 |
313.20 | 0.7320 | 0.2329 | 0.0015 | 0.0100 |
313.20 | 0.7625 | 0.2041 | 0.0012 | 0.0101 |
313.20 | 0.7961 | 0.1722 | 0.0010 | 0.0104 |
313.20 | 0.8267 | 0.1427 | 0.0007 | 0.0109 |
313.20 | 0.8400 | 0.1298 | 0.0006 | 0.0113 |
313.20 | 0.8690 | 0.1022 | 0.0005 | 0.0116 |
313.20 | 0.8942 | 0.0782 | 0.0003 | 0.0121 |
298.20 | 0.6613 | 0.2994 | 0.0020 | 0.0084 |
313.20 | 0.9827 | 0.0000 | 0.0000 | 0.0159 |
323.20 | 0.6352 | 0.3167 | 0.0027 | 0.0071 |
323.20 | 0.6914 | 0.2615 | 0.0021 | 0.0089 |
323.20 | 0.7389 | 0.2147 | 0.0016 | 0.0098 |
323.20 | 0.7531 | 0.2009 | 0.0013 | 0.0102 |
323.20 | 0.7810 | 0.1765 | 0.0011 | 0.0105 |
323.20 | 0.8016 | 0.1586 | 0.0009 | 0.0106 |
323.20 | 0.8172 | 0.1473 | 0.0008 | 0.0108 |
323.20 | 0.8375 | 0.1292 | 0.0006 | 0.0109 |
323.20 | 0.8590 | 0.1082 | 0.0005 | 0.0114 |
298.20 | 0.6989 | 0.2659 | 0.0015 | 0.0109 |
323.20 | 0.9807 | 0.0000 | 0.0000 | 0.0141 |
298.20 | 0.7299 | 0.2389 | 0.0014 | 0.0113 |
298.20 | 0.7479 | 0.2173 | 0.0011 | 0.0120 |
298.20 | 0.7564 | 0.2094 | 0.0010 | 0.0124 |
298.20 | 0.7663 | 0.2006 | 0.0009 | 0.0130 |
298.20 | 0.7823 | 0.1864 | 0.0008 | 0.0133 |
298.20 | 0.7988 | 0.1729 | 0.0006 | 0.0145 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 2 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 | Mole fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
333.20 | 0.8184 | 0.0507 | 0.0022 | 0.0001 |
333.20 | 0.6120 | 0.1775 | 0.0022 | 0.0002 |
333.20 | 0.5254 | 0.2282 | 0.0021 | 0.0003 |
333.20 | 0.4483 | 0.2704 | 0.0021 | 0.0005 |
333.20 | 0.3836 | 0.3014 | 0.0020 | 0.0007 |
333.20 | 0.3302 | 0.3369 | 0.0019 | 0.0010 |
333.20 | 0.2332 | 0.3840 | 0.0018 | 0.0017 |
353.20 | 0.8092 | 0.0399 | 0.0022 | 0.0001 |
353.20 | 0.7027 | 0.1045 | 0.0022 | 0.0001 |
353.20 | 0.6009 | 0.1551 | 0.0022 | 0.0003 |
353.20 | 0.5197 | 0.2095 | 0.0021 | 0.0004 |
353.20 | 0.4047 | 0.2634 | 0.0020 | 0.0007 |
353.20 | 0.3416 | 0.2911 | 0.0019 | 0.0011 |
353.20 | 0.2814 | 0.3155 | 0.0019 | 0.0018 |
353.20 | 0.2399 | 0.3366 | 0.0017 | 0.0026 |
333.20 | 0.7079 | 0.1133 | 0.0022 | 0.0001 |
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, 3-methyl- (1) - Liquid mixture 1 | Mass fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 | Mass fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 2 |
298.20 | 0.6407 | 0.3172 | 0.0024 | 0.0079 |
298.20 | 0.9853 | 0.0000 | 0.0000 | 0.0171 |
313.20 | 0.6372 | 0.3185 | 0.0025 | 0.0077 |
313.20 | 0.6969 | 0.2617 | 0.0019 | 0.0075 |
313.20 | 0.7320 | 0.2329 | 0.0015 | 0.0100 |
313.20 | 0.7625 | 0.2041 | 0.0012 | 0.0101 |
313.20 | 0.7961 | 0.1722 | 0.0010 | 0.0104 |
313.20 | 0.8267 | 0.1427 | 0.0007 | 0.0109 |
313.20 | 0.8400 | 0.1298 | 0.0006 | 0.0113 |
313.20 | 0.8690 | 0.1022 | 0.0005 | 0.0116 |
313.20 | 0.8942 | 0.0782 | 0.0003 | 0.0121 |
298.20 | 0.6613 | 0.2994 | 0.0020 | 0.0084 |
313.20 | 0.9827 | 0.0000 | 0.0000 | 0.0159 |
323.20 | 0.6352 | 0.3167 | 0.0027 | 0.0071 |
323.20 | 0.6914 | 0.2615 | 0.0021 | 0.0089 |
323.20 | 0.7389 | 0.2147 | 0.0016 | 0.0098 |
323.20 | 0.7531 | 0.2009 | 0.0013 | 0.0102 |
323.20 | 0.7810 | 0.1765 | 0.0011 | 0.0105 |
323.20 | 0.8016 | 0.1586 | 0.0009 | 0.0106 |
323.20 | 0.8172 | 0.1473 | 0.0008 | 0.0108 |
323.20 | 0.8375 | 0.1292 | 0.0006 | 0.0109 |
323.20 | 0.8590 | 0.1082 | 0.0005 | 0.0114 |
298.20 | 0.6989 | 0.2659 | 0.0015 | 0.0109 |
323.20 | 0.9807 | 0.0000 | 0.0000 | 0.0141 |
298.20 | 0.7299 | 0.2389 | 0.0014 | 0.0113 |
298.20 | 0.7479 | 0.2173 | 0.0011 | 0.0120 |
298.20 | 0.7564 | 0.2094 | 0.0010 | 0.0124 |
298.20 | 0.7663 | 0.2006 | 0.0009 | 0.0130 |
298.20 | 0.7823 | 0.1864 | 0.0008 | 0.0133 |
298.20 | 0.7988 | 0.1729 | 0.0006 | 0.0145 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 2 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 2 | Mole fraction of 2-Butanone, 3,3-dimethyl- (2) - Liquid mixture 1 | Mole fraction of Phenol, 3-methyl- (1) - Liquid mixture 1 |
333.20 | 0.8184 | 0.0507 | 0.0022 | 0.0001 |
333.20 | 0.6120 | 0.1775 | 0.0022 | 0.0002 |
333.20 | 0.5254 | 0.2282 | 0.0021 | 0.0003 |
333.20 | 0.4483 | 0.2704 | 0.0021 | 0.0005 |
333.20 | 0.3836 | 0.3014 | 0.0020 | 0.0007 |
333.20 | 0.3302 | 0.3369 | 0.0019 | 0.0010 |
333.20 | 0.2332 | 0.3840 | 0.0018 | 0.0017 |
353.20 | 0.8092 | 0.0399 | 0.0022 | 0.0001 |
353.20 | 0.7027 | 0.1045 | 0.0022 | 0.0001 |
353.20 | 0.6009 | 0.1551 | 0.0022 | 0.0003 |
353.20 | 0.5197 | 0.2095 | 0.0021 | 0.0004 |
353.20 | 0.4047 | 0.2634 | 0.0020 | 0.0007 |
353.20 | 0.3416 | 0.2911 | 0.0019 | 0.0011 |
353.20 | 0.2814 | 0.3155 | 0.0019 | 0.0018 |
353.20 | 0.2399 | 0.3366 | 0.0017 | 0.0026 |
333.20 | 0.7079 | 0.1133 | 0.0022 | 0.0001 |