Mixture of Ethanol, 2-methoxy- + 2-Propanol, 1-methoxy-
Datasets
-
Mole fraction (2)
-
Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 2-Propanol, 1-methoxy- (2)
[ref]
Fixed |
Measured |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Gas |
0.0701 |
74.50 |
0.1658 |
0.1493 |
74.50 |
0.3851 |
0.1980 |
74.50 |
0.4238 |
0.3016 |
74.50 |
0.5315 |
0.3955 |
74.50 |
0.6412 |
0.5084 |
74.50 |
0.7782 |
0.6841 |
74.50 |
0.8826 |
0.7458 |
74.50 |
0.9353 |
0.0214 |
101.30 |
0.0888 |
0.0592 |
101.30 |
0.1917 |
0.1540 |
101.30 |
0.3474 |
0.2051 |
101.30 |
0.4104 |
0.3544 |
101.30 |
0.5665 |
0.4164 |
101.30 |
0.6446 |
0.5673 |
101.30 |
0.7722 |
0.6936 |
101.30 |
0.8482 |
0.1175 |
134.00 |
0.2263 |
0.2031 |
134.00 |
0.3467 |
0.2366 |
134.00 |
0.4232 |
0.3009 |
134.00 |
0.5249 |
0.3705 |
134.00 |
0.5933 |
0.4850 |
134.00 |
0.7547 |
0.5603 |
134.00 |
0.8451 |
0.7420 |
134.00 |
0.9603 |
Mole fraction of 2-Propanol, 1-methoxy- (2)
[ref]
Fixed |
Measured |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Pressure, kPa - Liquid |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Gas |
0.0701 |
74.50 |
0.1658 |
0.1493 |
74.50 |
0.3851 |
0.1980 |
74.50 |
0.4238 |
0.3016 |
74.50 |
0.5315 |
0.3955 |
74.50 |
0.6412 |
0.5084 |
74.50 |
0.7782 |
0.6841 |
74.50 |
0.8826 |
0.7458 |
74.50 |
0.9353 |
0.0214 |
101.30 |
0.0888 |
0.0592 |
101.30 |
0.1917 |
0.1540 |
101.30 |
0.3474 |
0.2051 |
101.30 |
0.4104 |
0.3544 |
101.30 |
0.5665 |
0.4164 |
101.30 |
0.6446 |
0.5673 |
101.30 |
0.7722 |
0.6936 |
101.30 |
0.8482 |
0.1175 |
134.00 |
0.2263 |
0.2031 |
134.00 |
0.3467 |
0.2366 |
134.00 |
0.4232 |
0.3009 |
134.00 |
0.5249 |
0.3705 |
134.00 |
0.5933 |
0.4850 |
134.00 |
0.7547 |
0.5603 |
134.00 |
0.8451 |
0.7420 |
134.00 |
0.9603 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0701 |
74.50 |
387.00 |
0.1493 |
74.50 |
386.40 |
0.1980 |
74.50 |
386.00 |
0.3016 |
74.50 |
385.40 |
0.3955 |
74.50 |
385.00 |
0.5084 |
74.50 |
384.40 |
0.6841 |
74.50 |
384.00 |
0.7458 |
74.50 |
383.80 |
0.0214 |
101.30 |
397.30 |
0.0592 |
101.30 |
396.80 |
0.1540 |
101.30 |
395.90 |
0.2051 |
101.30 |
395.50 |
0.3544 |
101.30 |
394.60 |
0.4164 |
101.30 |
394.20 |
0.5673 |
101.30 |
393.60 |
0.6936 |
101.30 |
393.40 |
0.1175 |
134.00 |
405.80 |
0.2031 |
134.00 |
405.10 |
0.2366 |
134.00 |
404.80 |
0.3009 |
134.00 |
404.30 |
0.3705 |
134.00 |
403.90 |
0.4850 |
134.00 |
403.20 |
0.5603 |
134.00 |
402.90 |
0.7420 |
134.00 |
402.40 |
Boiling temperature at pressure P, K
[ref]
Fixed |
Measured |
Mole fraction of 2-Propanol, 1-methoxy- (2) - Liquid |
Pressure, kPa - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0701 |
74.50 |
387.00 |
0.1493 |
74.50 |
386.40 |
0.1980 |
74.50 |
386.00 |
0.3016 |
74.50 |
385.40 |
0.3955 |
74.50 |
385.00 |
0.5084 |
74.50 |
384.40 |
0.6841 |
74.50 |
384.00 |
0.7458 |
74.50 |
383.80 |
0.0214 |
101.30 |
397.30 |
0.0592 |
101.30 |
396.80 |
0.1540 |
101.30 |
395.90 |
0.2051 |
101.30 |
395.50 |
0.3544 |
101.30 |
394.60 |
0.4164 |
101.30 |
394.20 |
0.5673 |
101.30 |
393.60 |
0.6936 |
101.30 |
393.40 |
0.1175 |
134.00 |
405.80 |
0.2031 |
134.00 |
405.10 |
0.2366 |
134.00 |
404.80 |
0.3009 |
134.00 |
404.30 |
0.3705 |
134.00 |
403.90 |
0.4850 |
134.00 |
403.20 |
0.5603 |
134.00 |
402.90 |
0.7420 |
134.00 |
402.40 |
Sources