Mixture of 1-Butanamine, N,N-dimethyl- + n-Hexane
Datasets
-
Tboil - Boiling temperature at pressure P, K (2)
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid |
Mole fraction of 1-Butanamine, N,N-dimethyl- (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 29.84 |
0.1158 |
309.00 |
| 29.84 |
0.2271 |
310.70 |
| 29.84 |
0.4386 |
314.50 |
| 29.84 |
0.6374 |
319.10 |
| 29.84 |
0.8241 |
324.40 |
| 29.84 |
0.9117 |
327.50 |
| 49.84 |
0.1158 |
322.50 |
| 49.84 |
0.2271 |
324.20 |
| 49.84 |
0.4386 |
328.30 |
| 49.84 |
0.6374 |
332.90 |
| 49.84 |
0.8241 |
338.30 |
| 49.84 |
0.9117 |
341.50 |
| 69.83 |
0.1158 |
332.10 |
| 69.83 |
0.2271 |
333.90 |
| 69.83 |
0.4386 |
338.20 |
| 69.83 |
0.6374 |
342.90 |
| 69.83 |
0.8241 |
348.40 |
| 69.83 |
0.9117 |
351.80 |
| 89.83 |
0.1158 |
339.80 |
| 89.83 |
0.2271 |
341.60 |
| 89.83 |
0.4386 |
346.00 |
| 89.83 |
0.6374 |
350.90 |
| 89.83 |
0.8241 |
356.40 |
| 89.83 |
0.9117 |
359.70 |
| 99.83 |
0.1158 |
343.10 |
| 99.83 |
0.2271 |
345.00 |
| 99.83 |
0.4386 |
349.40 |
| 99.83 |
0.6374 |
354.40 |
| 99.83 |
0.8241 |
359.90 |
| 99.83 |
0.9117 |
363.20 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid |
Mole fraction of 1-Butanamine, N,N-dimethyl- (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 29.84 |
0.1158 |
309.00 |
| 29.84 |
0.2271 |
310.70 |
| 29.84 |
0.4386 |
314.50 |
| 29.84 |
0.6374 |
319.10 |
| 29.84 |
0.8241 |
324.40 |
| 29.84 |
0.9117 |
327.50 |
| 49.84 |
0.1158 |
322.50 |
| 49.84 |
0.2271 |
324.20 |
| 49.84 |
0.4386 |
328.30 |
| 49.84 |
0.6374 |
332.90 |
| 49.84 |
0.8241 |
338.30 |
| 49.84 |
0.9117 |
341.50 |
| 69.83 |
0.1158 |
332.10 |
| 69.83 |
0.2271 |
333.90 |
| 69.83 |
0.4386 |
338.20 |
| 69.83 |
0.6374 |
342.90 |
| 69.83 |
0.8241 |
348.40 |
| 69.83 |
0.9117 |
351.80 |
| 89.83 |
0.1158 |
339.80 |
| 89.83 |
0.2271 |
341.60 |
| 89.83 |
0.4386 |
346.00 |
| 89.83 |
0.6374 |
350.90 |
| 89.83 |
0.8241 |
356.40 |
| 89.83 |
0.9117 |
359.70 |
| 99.83 |
0.1158 |
343.10 |
| 99.83 |
0.2271 |
345.00 |
| 99.83 |
0.4386 |
349.40 |
| 99.83 |
0.6374 |
354.40 |
| 99.83 |
0.8241 |
359.90 |
| 99.83 |
0.9117 |
363.20 |
Sources