Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mass fraction of 2-Butanone, 3-methyl- (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-methyl- (2) - Liquid mixture 2 |
298.20 | 0.9653 | 0.0000 | 0.0000 | 0.0619 |
313.20 | 0.9598 | 0.0000 | 0.0000 | 0.0496 |
313.20 | 0.8521 | 0.1010 | 0.0003 | 0.0376 |
313.20 | 0.7716 | 0.1756 | 0.0006 | 0.0292 |
313.20 | 0.6857 | 0.2567 | 0.0011 | 0.0246 |
313.20 | 0.6340 | 0.3035 | 0.0015 | 0.0212 |
313.20 | 0.5686 | 0.3633 | 0.0024 | 0.0172 |
313.20 | 0.5123 | 0.4163 | 0.0034 | 0.0142 |
313.20 | 0.4715 | 0.4538 | 0.0043 | 0.0125 |
313.20 | 0.4303 | 0.4918 | 0.0053 | 0.0104 |
298.20 | 0.8497 | 0.1062 | 0.0003 | 0.0471 |
298.20 | 0.7689 | 0.1817 | 0.0006 | 0.0373 |
298.20 | 0.6961 | 0.2497 | 0.0009 | 0.0307 |
298.20 | 0.6543 | 0.2882 | 0.0012 | 0.0268 |
298.20 | 0.5905 | 0.3472 | 0.0020 | 0.0227 |
298.20 | 0.5386 | 0.3956 | 0.0029 | 0.0189 |
298.20 | 0.4878 | 0.4431 | 0.0038 | 0.0158 |
298.20 | 0.4392 | 0.4877 | 0.0050 | 0.0123 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone, 3-methyl- (2) - Liquid mixture 2 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 | Mole fraction of 2-Butanone, 3-methyl- (2) - Liquid mixture 1 |
333.20 | 0.8307 | 0.0000 | 0.0000 | 0.0088 |
333.20 | 0.7389 | 0.0805 | 0.0001 | 0.0067 |
333.20 | 0.6502 | 0.1248 | 0.0002 | 0.0058 |
333.20 | 0.5737 | 0.1653 | 0.0003 | 0.0047 |
333.20 | 0.4900 | 0.2113 | 0.0007 | 0.0041 |
333.20 | 0.4480 | 0.2381 | 0.0009 | 0.0033 |
333.20 | 0.4103 | 0.2609 | 0.0012 | 0.0028 |
333.20 | 0.3527 | 0.2951 | 0.0014 | 0.0022 |
333.20 | 0.2917 | 0.3227 | 0.0015 | 0.0019 |
333.20 | 0.0000 | 0.4866 | 0.0053 | 0.0000 |
343.20 | 0.8115 | 0.0000 | 0.0000 | 0.0074 |
343.20 | 0.7617 | 0.0597 | 0.0001 | 0.0059 |
343.20 | 0.6601 | 0.1057 | 0.0003 | 0.0050 |
343.20 | 0.5829 | 0.1412 | 0.0004 | 0.0048 |
343.20 | 0.4941 | 0.1888 | 0.0006 | 0.0043 |
343.20 | 0.4387 | 0.2073 | 0.0008 | 0.0035 |
343.20 | 0.3594 | 0.2514 | 0.0011 | 0.0029 |
343.20 | 0.3384 | 0.2667 | 0.0012 | 0.0023 |
343.20 | 0.2613 | 0.3071 | 0.0014 | 0.0015 |
343.20 | 0.0000 | 0.4614 | 0.0059 | 0.0000 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 2 | Mass fraction of 2-Butanone, 3-methyl- (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-methyl- (2) - Liquid mixture 2 |
298.20 | 0.9653 | 0.0000 | 0.0000 | 0.0619 |
313.20 | 0.9598 | 0.0000 | 0.0000 | 0.0496 |
313.20 | 0.8521 | 0.1010 | 0.0003 | 0.0376 |
313.20 | 0.7716 | 0.1756 | 0.0006 | 0.0292 |
313.20 | 0.6857 | 0.2567 | 0.0011 | 0.0246 |
313.20 | 0.6340 | 0.3035 | 0.0015 | 0.0212 |
313.20 | 0.5686 | 0.3633 | 0.0024 | 0.0172 |
313.20 | 0.5123 | 0.4163 | 0.0034 | 0.0142 |
313.20 | 0.4715 | 0.4538 | 0.0043 | 0.0125 |
313.20 | 0.4303 | 0.4918 | 0.0053 | 0.0104 |
298.20 | 0.8497 | 0.1062 | 0.0003 | 0.0471 |
298.20 | 0.7689 | 0.1817 | 0.0006 | 0.0373 |
298.20 | 0.6961 | 0.2497 | 0.0009 | 0.0307 |
298.20 | 0.6543 | 0.2882 | 0.0012 | 0.0268 |
298.20 | 0.5905 | 0.3472 | 0.0020 | 0.0227 |
298.20 | 0.5386 | 0.3956 | 0.0029 | 0.0189 |
298.20 | 0.4878 | 0.4431 | 0.0038 | 0.0158 |
298.20 | 0.4392 | 0.4877 | 0.0050 | 0.0123 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||
---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone, 3-methyl- (2) - Liquid mixture 2 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 2 | Mole fraction of Phenol, 2-methyl- (1) - Liquid mixture 1 | Mole fraction of 2-Butanone, 3-methyl- (2) - Liquid mixture 1 |
333.20 | 0.8307 | 0.0000 | 0.0000 | 0.0088 |
333.20 | 0.7389 | 0.0805 | 0.0001 | 0.0067 |
333.20 | 0.6502 | 0.1248 | 0.0002 | 0.0058 |
333.20 | 0.5737 | 0.1653 | 0.0003 | 0.0047 |
333.20 | 0.4900 | 0.2113 | 0.0007 | 0.0041 |
333.20 | 0.4480 | 0.2381 | 0.0009 | 0.0033 |
333.20 | 0.4103 | 0.2609 | 0.0012 | 0.0028 |
333.20 | 0.3527 | 0.2951 | 0.0014 | 0.0022 |
333.20 | 0.2917 | 0.3227 | 0.0015 | 0.0019 |
333.20 | 0.0000 | 0.4866 | 0.0053 | 0.0000 |
343.20 | 0.8115 | 0.0000 | 0.0000 | 0.0074 |
343.20 | 0.7617 | 0.0597 | 0.0001 | 0.0059 |
343.20 | 0.6601 | 0.1057 | 0.0003 | 0.0050 |
343.20 | 0.5829 | 0.1412 | 0.0004 | 0.0048 |
343.20 | 0.4941 | 0.1888 | 0.0006 | 0.0043 |
343.20 | 0.4387 | 0.2073 | 0.0008 | 0.0035 |
343.20 | 0.3594 | 0.2514 | 0.0011 | 0.0029 |
343.20 | 0.3384 | 0.2667 | 0.0012 | 0.0023 |
343.20 | 0.2613 | 0.3071 | 0.0014 | 0.0015 |
343.20 | 0.0000 | 0.4614 | 0.0059 | 0.0000 |