Datasets
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Azeotropic composition: mole fraction (3)
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Tboil(P) - Boiling temperature at pressure P, K
Azeotropic composition: mole fraction of 2-Butene, 2,3-dimethyl- (1)
[ref]
| Temperature, K - Liquid |
Azeotropic composition: mole fraction of 2-Butene, 2,3-dimethyl- (1) - Liquid |
| 345.10 |
0.8950 |
Azeotropic composition: mole fraction of 2-Butene, 2,3-dimethyl- (1)
[ref]
| Pressure, kPa - Liquid |
Azeotropic composition: mole fraction of 2-Butene, 2,3-dimethyl- (1) - Liquid |
| 101.80 |
0.8950 |
Mole fraction of 2-Butene, 2,3-dimethyl- (1)
[ref]
| Fixed |
Measured |
| Mole fraction of 2-Butene, 2,3-dimethyl- (1) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 2-Butene, 2,3-dimethyl- (1) - Gas |
| 0.0000 |
102.10 |
0.0000 |
| 0.0103 |
101.20 |
0.0611 |
| 0.0150 |
101.20 |
0.0868 |
| 0.0224 |
101.20 |
0.1223 |
| 0.0375 |
101.20 |
0.1991 |
| 0.0544 |
101.20 |
0.2598 |
| 0.0680 |
101.30 |
0.3014 |
| 0.0900 |
101.40 |
0.3750 |
| 0.1146 |
101.30 |
0.4277 |
| 0.1348 |
101.30 |
0.4740 |
| 0.1590 |
101.30 |
0.5114 |
| 0.2123 |
101.30 |
0.5858 |
| 0.2407 |
101.30 |
0.6125 |
| 0.2908 |
101.30 |
0.6561 |
| 0.3263 |
101.70 |
0.6784 |
| 0.3917 |
101.70 |
0.7184 |
| 0.4652 |
101.70 |
0.7521 |
| 0.5390 |
101.70 |
0.7769 |
| 0.6887 |
101.70 |
0.8009 |
| 0.7448 |
101.70 |
0.8402 |
| 0.7885 |
101.70 |
0.8548 |
| 0.8375 |
101.80 |
0.8695 |
| 0.8764 |
101.80 |
0.8859 |
| 0.9189 |
102.10 |
0.9065 |
| 0.9706 |
102.10 |
0.9536 |
| 0.9860 |
102.10 |
0.9757 |
| 1.0000 |
102.10 |
1.0000 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of 2-Butene, 2,3-dimethyl- (1) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 0.0000 |
102.10 |
372.61 |
| 0.0103 |
101.20 |
371.05 |
| 0.0150 |
101.20 |
370.44 |
| 0.0224 |
101.20 |
369.56 |
| 0.0375 |
101.20 |
367.95 |
| 0.0544 |
101.20 |
366.25 |
| 0.0680 |
101.30 |
365.06 |
| 0.0900 |
101.40 |
362.95 |
| 0.1146 |
101.30 |
361.23 |
| 0.1348 |
101.30 |
359.74 |
| 0.1590 |
101.30 |
358.28 |
| 0.2123 |
101.30 |
355.52 |
| 0.2407 |
101.30 |
354.24 |
| 0.2908 |
101.30 |
352.41 |
| 0.3263 |
101.70 |
351.51 |
| 0.3917 |
101.70 |
349.90 |
| 0.4652 |
101.70 |
348.49 |
| 0.5390 |
101.70 |
347.44 |
| 0.6887 |
101.70 |
346.54 |
| 0.7448 |
101.70 |
345.92 |
| 0.7885 |
101.70 |
345.54 |
| 0.8375 |
101.80 |
345.24 |
| 0.8764 |
101.80 |
345.11 |
| 0.9189 |
102.10 |
345.24 |
| 0.9706 |
102.10 |
345.76 |
| 0.9860 |
102.10 |
346.09 |
| 1.0000 |
102.10 |
346.49 |
Sources
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