Mixture of 1-Methoxy-2-propyl acetate + Water
Datasets
-
Tboil - Boiling temperature at pressure P, K (2)
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 26.70 |
0.0480 |
366.00 |
| 26.70 |
0.0980 |
358.22 |
| 26.70 |
0.2000 |
347.96 |
| 26.70 |
0.2980 |
343.19 |
| 26.70 |
0.3980 |
339.47 |
| 26.70 |
0.4990 |
336.93 |
| 26.70 |
0.5990 |
336.54 |
| 26.70 |
0.6990 |
336.36 |
| 26.70 |
0.7990 |
336.40 |
| 26.70 |
0.8500 |
336.22 |
| 26.70 |
0.9000 |
336.38 |
| 26.70 |
0.9500 |
336.33 |
| 26.70 |
0.9750 |
336.33 |
| 26.70 |
0.9900 |
336.53 |
| 53.30 |
0.0480 |
384.45 |
| 53.30 |
0.0980 |
376.04 |
| 53.30 |
0.1980 |
364.01 |
| 53.30 |
0.2980 |
358.41 |
| 53.30 |
0.3980 |
354.91 |
| 53.30 |
0.4990 |
352.97 |
| 53.30 |
0.5990 |
352.51 |
| 53.30 |
0.6990 |
352.45 |
| 53.30 |
0.7990 |
352.53 |
| 53.30 |
0.8500 |
352.38 |
| 53.30 |
0.9000 |
352.45 |
| 53.30 |
0.9500 |
352.45 |
| 53.30 |
0.9750 |
352.45 |
| 53.30 |
0.9900 |
352.53 |
| 93.30 |
0.0480 |
402.43 |
| 93.30 |
0.0980 |
392.58 |
| 93.30 |
0.1980 |
379.53 |
| 93.30 |
0.2980 |
372.33 |
| 93.30 |
0.3980 |
369.54 |
| 93.30 |
0.4990 |
367.68 |
| 93.30 |
0.5990 |
367.07 |
| 93.30 |
0.6990 |
367.05 |
| 93.30 |
0.7990 |
367.09 |
| 93.30 |
0.8500 |
367.01 |
| 93.30 |
0.9000 |
367.04 |
| 93.30 |
0.9500 |
367.05 |
| 93.30 |
0.9750 |
367.09 |
| 93.30 |
0.9900 |
367.78 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid |
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
| 26.70 |
0.0480 |
366.00 |
| 26.70 |
0.0980 |
358.22 |
| 26.70 |
0.2000 |
347.96 |
| 26.70 |
0.2980 |
343.19 |
| 26.70 |
0.3980 |
339.47 |
| 26.70 |
0.4990 |
336.93 |
| 26.70 |
0.5990 |
336.54 |
| 26.70 |
0.6990 |
336.36 |
| 26.70 |
0.7990 |
336.40 |
| 26.70 |
0.8500 |
336.22 |
| 26.70 |
0.9000 |
336.38 |
| 26.70 |
0.9500 |
336.33 |
| 26.70 |
0.9750 |
336.33 |
| 26.70 |
0.9900 |
336.53 |
| 53.30 |
0.0480 |
384.45 |
| 53.30 |
0.0980 |
376.04 |
| 53.30 |
0.1980 |
364.01 |
| 53.30 |
0.2980 |
358.41 |
| 53.30 |
0.3980 |
354.91 |
| 53.30 |
0.4990 |
352.97 |
| 53.30 |
0.5990 |
352.51 |
| 53.30 |
0.6990 |
352.45 |
| 53.30 |
0.7990 |
352.53 |
| 53.30 |
0.8500 |
352.38 |
| 53.30 |
0.9000 |
352.45 |
| 53.30 |
0.9500 |
352.45 |
| 53.30 |
0.9750 |
352.45 |
| 53.30 |
0.9900 |
352.53 |
| 93.30 |
0.0480 |
402.43 |
| 93.30 |
0.0980 |
392.58 |
| 93.30 |
0.1980 |
379.53 |
| 93.30 |
0.2980 |
372.33 |
| 93.30 |
0.3980 |
369.54 |
| 93.30 |
0.4990 |
367.68 |
| 93.30 |
0.5990 |
367.07 |
| 93.30 |
0.6990 |
367.05 |
| 93.30 |
0.7990 |
367.09 |
| 93.30 |
0.8500 |
367.01 |
| 93.30 |
0.9000 |
367.04 |
| 93.30 |
0.9500 |
367.05 |
| 93.30 |
0.9750 |
367.09 |
| 93.30 |
0.9900 |
367.78 |
Sources