Operational conditions:
| Fixed | Measured | ||
|---|---|---|---|
| Mole fraction of Butane, 2-methyl- (2) - Liquid mixture 1 | Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid mixture 1 | Mole fraction of Butane, 2-methyl- (2) - Liquid mixture 2 | Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid mixture 2 |
| 0.9996 | 0.0000 | 0.0000 | 0.0000 |
| 0.9861 | 0.0130 | 0.0000 | 0.0165 |
| 0.9619 | 0.0344 | 0.0000 | 0.0287 |
| 0.9455 | 0.0483 | 0.0000 | 0.0298 |
| 0.9034 | 0.0781 | 0.0000 | 0.0346 |
| 0.8668 | 0.1120 | 0.0000 | 0.0383 |
| 0.8062 | 0.1610 | 0.0000 | 0.0419 |
| 0.7432 | 0.2060 | 0.0000 | 0.0434 |
| 0.7112 | 0.2360 | 0.0000 | 0.0486 |
| 0.7068 | 0.2360 | 0.0000 | 0.0455 |
| 0.6440 | 0.2890 | 0.0000 | 0.0490 |
| 0.5934 | 0.3170 | 0.0000 | 0.0501 |
| 0.5410 | 0.3480 | 0.0001 | 0.0528 |
| 0.4640 | 0.3810 | 0.0001 | 0.0548 |
| 0.4160 | 0.4030 | 0.0001 | 0.0577 |
| 0.3610 | 0.4150 | 0.0001 | 0.0581 |
| 0.2970 | 0.4330 | 0.0002 | 0.0605 |
| 0.2730 | 0.4320 | 0.0002 | 0.0608 |
| 0.2200 | 0.4310 | 0.0002 | 0.0639 |
| 0.2170 | 0.4320 | 0.0002 | 0.0648 |
| 0.1520 | 0.4150 | 0.0004 | 0.0693 |
| 0.1020 | 0.3840 | 0.0006 | 0.0769 |
| 0.0440 | 0.3000 | 0.0018 | 0.0926 |
Operational conditions:
| Fixed | Measured | ||
|---|---|---|---|
| Mole fraction of Butane, 2-methyl- (2) - Liquid mixture 1 | Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid mixture 1 | Mole fraction of Butane, 2-methyl- (2) - Liquid mixture 2 | Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid mixture 2 |
| 0.9996 | 0.0000 | 0.0000 | 0.0000 |
| 0.9861 | 0.0130 | 0.0000 | 0.0165 |
| 0.9619 | 0.0344 | 0.0000 | 0.0287 |
| 0.9455 | 0.0483 | 0.0000 | 0.0298 |
| 0.9034 | 0.0781 | 0.0000 | 0.0346 |
| 0.8668 | 0.1120 | 0.0000 | 0.0383 |
| 0.8062 | 0.1610 | 0.0000 | 0.0419 |
| 0.7432 | 0.2060 | 0.0000 | 0.0434 |
| 0.7112 | 0.2360 | 0.0000 | 0.0486 |
| 0.7068 | 0.2360 | 0.0000 | 0.0455 |
| 0.6440 | 0.2890 | 0.0000 | 0.0490 |
| 0.5934 | 0.3170 | 0.0000 | 0.0501 |
| 0.5410 | 0.3480 | 0.0001 | 0.0528 |
| 0.4640 | 0.3810 | 0.0001 | 0.0548 |
| 0.4160 | 0.4030 | 0.0001 | 0.0577 |
| 0.3610 | 0.4150 | 0.0001 | 0.0581 |
| 0.2970 | 0.4330 | 0.0002 | 0.0605 |
| 0.2730 | 0.4320 | 0.0002 | 0.0608 |
| 0.2200 | 0.4310 | 0.0002 | 0.0639 |
| 0.2170 | 0.4320 | 0.0002 | 0.0648 |
| 0.1520 | 0.4150 | 0.0004 | 0.0693 |
| 0.1020 | 0.3840 | 0.0006 | 0.0769 |
| 0.0440 | 0.3000 | 0.0018 | 0.0926 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Butane, 2-methyl- (2) - Liquid mixture 1 | Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
| 0.0747 | 0.3441 | 293.15 |
| 0.1064 | 0.3794 | 293.15 |
| 0.1892 | 0.4218 | 293.15 |
| 0.2420 | 0.4267 | 293.15 |
| 0.2975 | 0.4252 | 293.15 |
| 0.3048 | 0.4247 | 293.15 |
| 0.4186 | 0.3936 | 293.15 |
| 0.5363 | 0.3418 | 293.15 |
| 0.6115 | 0.3018 | 293.15 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Butane, 2-methyl- (2) - Liquid mixture 1 | Mole fraction of 2-Propanol, 2-methyl- (1) - Liquid mixture 1 | Liquid-liquid equilibrium temperature, K - Liquid mixture 1 |
| 0.0747 | 0.3441 | 293.15 |
| 0.1064 | 0.3794 | 293.15 |
| 0.1892 | 0.4218 | 293.15 |
| 0.2420 | 0.4267 | 293.15 |
| 0.2975 | 0.4252 | 293.15 |
| 0.3048 | 0.4247 | 293.15 |
| 0.4186 | 0.3936 | 293.15 |
| 0.5363 | 0.3418 | 293.15 |
| 0.6115 | 0.3018 | 293.15 |