Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Fixed | Measured | |||||
---|---|---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Ethanol (2) - Liquid mixture 1 | Mole fraction of Ethanol (2) - Liquid mixture 2 | Mole fraction of Ethanol (2) - Gas | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Water (3) - Gas |
346.75 | 0.0000 | 0.0000 | 0.0000 | 0.4344 | 0.9583 | 0.3606 |
346.35 | 0.0123 | 0.0049 | 0.0129 | 0.4606 | 0.9502 | 0.3636 |
345.95 | 0.0291 | 0.0120 | 0.0309 | 0.5182 | 0.9337 | 0.3666 |
345.25 | 0.0365 | 0.0168 | 0.0399 | 0.5483 | 0.9115 | 0.3612 |
344.75 | 0.0447 | 0.0248 | 0.0533 | 0.6365 | 0.8917 | 0.3615 |
344.35 | 0.0439 | 0.0332 | 0.0602 | 0.7205 | 0.8398 | 0.3614 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||||
---|---|---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone (1) - Liquid mixture 2 | Mole fraction of Ethanol (2) - Liquid mixture 2 | Mole fraction of 2-Butanone (1) - Liquid mixture 1 | Mole fraction of Ethanol (2) - Liquid mixture 1 | Mole fraction of 2-Butanone (1) - Gas | Mole fraction of Ethanol (2) - Gas |
346.65 | 0.0480 | 0.0000 | 0.5864 | 0.0000 | 0.6473 | 0.0000 |
346.79 | 0.0450 | 0.0000 | 0.5850 | 0.0000 | 0.6490 | 0.0000 |
346.70 | 0.0443 | 0.0000 | 0.5837 | 0.0000 | 0.6513 | 0.0000 |
346.68 | 0.0462 | 0.0041 | 0.5790 | 0.0060 | 0.6463 | 0.0045 |
346.67 | 0.0472 | 0.0053 | 0.5692 | 0.0100 | 0.6449 | 0.0060 |
346.65 | 0.0480 | 0.0071 | 0.5689 | 0.0114 | 0.6434 | 0.0080 |
346.63 | 0.0480 | 0.0092 | 0.5612 | 0.0124 | 0.6395 | 0.0128 |
346.61 | 0.0492 | 0.0097 | 0.5583 | 0.0136 | 0.6381 | 0.0141 |
346.59 | 0.0510 | 0.0101 | 0.5481 | 0.0155 | 0.6375 | 0.0156 |
346.56 | 0.0537 | 0.0119 | 0.5390 | 0.0183 | 0.6371 | 0.0175 |
346.54 | 0.0562 | 0.0134 | 0.5348 | 0.0191 | 0.6358 | 0.0185 |
346.51 | 0.0594 | 0.0151 | 0.5330 | 0.0195 | 0.6324 | 0.0213 |
346.48 | 0.0608 | 0.0158 | 0.5315 | 0.0206 | 0.6300 | 0.0235 |
346.45 | 0.0632 | 0.0168 | 0.5281 | 0.0207 | 0.6271 | 0.0261 |
346.42 | 0.0666 | 0.0191 | 0.5108 | 0.0241 | 0.6165 | 0.0414 |
346.38 | 0.0680 | 0.0201 | 0.4994 | 0.0263 | 0.6128 | 0.0430 |
346.35 | 0.0695 | 0.0206 | 0.4883 | 0.0296 | 0.6000 | 0.0567 |
346.31 | 0.0728 | 0.0239 | 0.4733 | 0.0315 | 0.5973 | 0.0596 |
346.26 | 0.0761 | 0.0247 | 0.4478 | 0.0357 | 0.5892 | 0.0685 |
346.19 | 0.0838 | 0.0280 | 0.4226 | 0.0389 | 0.5830 | 0.0761 |
346.12 | 0.0872 | 0.0297 | 0.4033 | 0.0401 | 0.5723 | 0.0892 |
345.65 | 0.0908 | 0.0305 | 0.3669 | 0.0421 | 0.5551 | 0.1082 |
Operational condition: Pressure, kPa = 101.325 (Liquid mixture 1)
Fixed | Measured | |||||
---|---|---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of Ethanol (2) - Liquid mixture 1 | Mole fraction of Ethanol (2) - Liquid mixture 2 | Mole fraction of Ethanol (2) - Gas | Mole fraction of Water (3) - Liquid mixture 1 | Mole fraction of Water (3) - Liquid mixture 2 | Mole fraction of Water (3) - Gas |
346.75 | 0.0000 | 0.0000 | 0.0000 | 0.4344 | 0.9583 | 0.3606 |
346.35 | 0.0123 | 0.0049 | 0.0129 | 0.4606 | 0.9502 | 0.3636 |
345.95 | 0.0291 | 0.0120 | 0.0309 | 0.5182 | 0.9337 | 0.3666 |
345.25 | 0.0365 | 0.0168 | 0.0399 | 0.5483 | 0.9115 | 0.3612 |
344.75 | 0.0447 | 0.0248 | 0.0533 | 0.6365 | 0.8917 | 0.3615 |
344.35 | 0.0439 | 0.0332 | 0.0602 | 0.7205 | 0.8398 | 0.3614 |
Operational condition: Pressure, kPa = 101.3 (Liquid mixture 2)
Fixed | Measured | |||||
---|---|---|---|---|---|---|
Temperature, K - Liquid mixture 1 | Mole fraction of 2-Butanone (1) - Liquid mixture 2 | Mole fraction of Ethanol (2) - Liquid mixture 2 | Mole fraction of 2-Butanone (1) - Liquid mixture 1 | Mole fraction of Ethanol (2) - Liquid mixture 1 | Mole fraction of 2-Butanone (1) - Gas | Mole fraction of Ethanol (2) - Gas |
346.65 | 0.0480 | 0.0000 | 0.5864 | 0.0000 | 0.6473 | 0.0000 |
346.79 | 0.0450 | 0.0000 | 0.5850 | 0.0000 | 0.6490 | 0.0000 |
346.70 | 0.0443 | 0.0000 | 0.5837 | 0.0000 | 0.6513 | 0.0000 |
346.68 | 0.0462 | 0.0041 | 0.5790 | 0.0060 | 0.6463 | 0.0045 |
346.67 | 0.0472 | 0.0053 | 0.5692 | 0.0100 | 0.6449 | 0.0060 |
346.65 | 0.0480 | 0.0071 | 0.5689 | 0.0114 | 0.6434 | 0.0080 |
346.63 | 0.0480 | 0.0092 | 0.5612 | 0.0124 | 0.6395 | 0.0128 |
346.61 | 0.0492 | 0.0097 | 0.5583 | 0.0136 | 0.6381 | 0.0141 |
346.59 | 0.0510 | 0.0101 | 0.5481 | 0.0155 | 0.6375 | 0.0156 |
346.56 | 0.0537 | 0.0119 | 0.5390 | 0.0183 | 0.6371 | 0.0175 |
346.54 | 0.0562 | 0.0134 | 0.5348 | 0.0191 | 0.6358 | 0.0185 |
346.51 | 0.0594 | 0.0151 | 0.5330 | 0.0195 | 0.6324 | 0.0213 |
346.48 | 0.0608 | 0.0158 | 0.5315 | 0.0206 | 0.6300 | 0.0235 |
346.45 | 0.0632 | 0.0168 | 0.5281 | 0.0207 | 0.6271 | 0.0261 |
346.42 | 0.0666 | 0.0191 | 0.5108 | 0.0241 | 0.6165 | 0.0414 |
346.38 | 0.0680 | 0.0201 | 0.4994 | 0.0263 | 0.6128 | 0.0430 |
346.35 | 0.0695 | 0.0206 | 0.4883 | 0.0296 | 0.6000 | 0.0567 |
346.31 | 0.0728 | 0.0239 | 0.4733 | 0.0315 | 0.5973 | 0.0596 |
346.26 | 0.0761 | 0.0247 | 0.4478 | 0.0357 | 0.5892 | 0.0685 |
346.19 | 0.0838 | 0.0280 | 0.4226 | 0.0389 | 0.5830 | 0.0761 |
346.12 | 0.0872 | 0.0297 | 0.4033 | 0.0401 | 0.5723 | 0.0892 |
345.65 | 0.0908 | 0.0305 | 0.3669 | 0.0421 | 0.5551 | 0.1082 |