Datasets
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Mole fraction (2)
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Pvap - Vapor or sublimation pressure, kPa (2)
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Tboil - Boiling temperature at pressure P, K (2)
Mole fraction of 2-Propen-1-ol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 2-Propen-1-ol (1) - Liquid |
Mole fraction of 2-Propen-1-ol (1) - Gas |
0.0410 |
0.1264 |
0.0825 |
0.2282 |
0.1208 |
0.3076 |
0.1663 |
0.3816 |
0.2202 |
0.4598 |
0.2670 |
0.5156 |
0.3230 |
0.5756 |
0.3873 |
0.6379 |
0.4650 |
0.6928 |
0.5389 |
0.7374 |
0.6249 |
0.7900 |
0.7313 |
0.8496 |
0.8186 |
0.8990 |
0.9118 |
0.9494 |
0.9725 |
0.9832 |
Mole fraction of 2-Propen-1-ol (1)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 2-Propen-1-ol (1) - Liquid |
Mole fraction of 2-Propen-1-ol (1) - Gas |
0.0410 |
0.1264 |
0.0825 |
0.2282 |
0.1208 |
0.3076 |
0.1663 |
0.3816 |
0.2202 |
0.4598 |
0.2670 |
0.5156 |
0.3230 |
0.5756 |
0.3873 |
0.6379 |
0.4650 |
0.6928 |
0.5389 |
0.7374 |
0.6249 |
0.7900 |
0.7313 |
0.8496 |
0.8186 |
0.8990 |
0.9118 |
0.9494 |
0.9725 |
0.9832 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Acetic acid, butyl ester (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
373.15 |
1.0000 |
44.71 |
373.15 |
0.9748 |
46.42 |
373.15 |
0.9493 |
49.15 |
373.15 |
0.9235 |
51.69 |
373.15 |
0.8999 |
53.96 |
373.15 |
0.8512 |
58.96 |
373.15 |
0.8018 |
63.77 |
373.15 |
0.7435 |
69.27 |
373.15 |
0.7012 |
72.99 |
373.15 |
0.6521 |
76.99 |
373.15 |
0.6014 |
80.67 |
373.15 |
0.5505 |
84.41 |
373.15 |
0.4997 |
88.26 |
373.15 |
0.4720 |
91.11 |
373.15 |
0.4498 |
91.71 |
373.15 |
0.4196 |
93.27 |
373.15 |
0.3681 |
95.81 |
373.15 |
0.3147 |
98.25 |
373.15 |
0.2621 |
100.46 |
373.15 |
0.2089 |
102.39 |
373.15 |
0.1556 |
104.77 |
373.15 |
0.1042 |
106.88 |
373.15 |
0.0779 |
107.83 |
373.15 |
0.0527 |
108.86 |
373.15 |
0.0264 |
109.47 |
373.15 |
0.0000 |
109.95 |
423.15 |
1.0000 |
195.63 |
423.15 |
0.9754 |
201.76 |
423.15 |
0.9504 |
211.77 |
423.15 |
0.9250 |
222.49 |
423.15 |
0.9017 |
231.83 |
423.15 |
0.8536 |
252.88 |
423.15 |
0.8047 |
270.74 |
423.15 |
0.7465 |
295.15 |
423.15 |
0.7043 |
310.13 |
423.15 |
0.6552 |
328.42 |
423.15 |
0.6042 |
343.55 |
423.15 |
0.5760 |
357.84 |
423.15 |
0.5530 |
361.98 |
423.15 |
0.5260 |
373.71 |
423.15 |
0.5018 |
379.37 |
423.15 |
0.4750 |
389.11 |
423.15 |
0.4516 |
395.91 |
423.15 |
0.4228 |
403.63 |
423.15 |
0.3715 |
418.72 |
423.15 |
0.3182 |
433.25 |
423.15 |
0.2654 |
447.77 |
423.15 |
0.2120 |
462.50 |
423.15 |
0.1581 |
477.27 |
423.15 |
0.1061 |
491.21 |
423.15 |
0.0793 |
497.99 |
423.15 |
0.0537 |
505.66 |
423.15 |
0.0269 |
513.29 |
423.15 |
0.0000 |
518.11 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Acetic acid, butyl ester (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
373.15 |
1.0000 |
44.71 |
373.15 |
0.9748 |
46.42 |
373.15 |
0.9493 |
49.15 |
373.15 |
0.9235 |
51.69 |
373.15 |
0.8999 |
53.96 |
373.15 |
0.8512 |
58.96 |
373.15 |
0.8018 |
63.77 |
373.15 |
0.7435 |
69.27 |
373.15 |
0.7012 |
72.99 |
373.15 |
0.6521 |
76.99 |
373.15 |
0.6014 |
80.67 |
373.15 |
0.5505 |
84.41 |
373.15 |
0.4997 |
88.26 |
373.15 |
0.4720 |
91.11 |
373.15 |
0.4498 |
91.71 |
373.15 |
0.4196 |
93.27 |
373.15 |
0.3681 |
95.81 |
373.15 |
0.3147 |
98.25 |
373.15 |
0.2621 |
100.46 |
373.15 |
0.2089 |
102.39 |
373.15 |
0.1556 |
104.77 |
373.15 |
0.1042 |
106.88 |
373.15 |
0.0779 |
107.83 |
373.15 |
0.0527 |
108.86 |
373.15 |
0.0264 |
109.47 |
373.15 |
0.0000 |
109.95 |
423.15 |
1.0000 |
195.63 |
423.15 |
0.9754 |
201.76 |
423.15 |
0.9504 |
211.77 |
423.15 |
0.9250 |
222.49 |
423.15 |
0.9017 |
231.83 |
423.15 |
0.8536 |
252.88 |
423.15 |
0.8047 |
270.74 |
423.15 |
0.7465 |
295.15 |
423.15 |
0.7043 |
310.13 |
423.15 |
0.6552 |
328.42 |
423.15 |
0.6042 |
343.55 |
423.15 |
0.5760 |
357.84 |
423.15 |
0.5530 |
361.98 |
423.15 |
0.5260 |
373.71 |
423.15 |
0.5018 |
379.37 |
423.15 |
0.4750 |
389.11 |
423.15 |
0.4516 |
395.91 |
423.15 |
0.4228 |
403.63 |
423.15 |
0.3715 |
418.72 |
423.15 |
0.3182 |
433.25 |
423.15 |
0.2654 |
447.77 |
423.15 |
0.2120 |
462.50 |
423.15 |
0.1581 |
477.27 |
423.15 |
0.1061 |
491.21 |
423.15 |
0.0793 |
497.99 |
423.15 |
0.0537 |
505.66 |
423.15 |
0.0269 |
513.29 |
423.15 |
0.0000 |
518.11 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 2-Propen-1-ol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0410 |
395.90 |
0.0825 |
393.10 |
0.1208 |
390.90 |
0.1663 |
388.63 |
0.2202 |
386.15 |
0.2670 |
384.30 |
0.3230 |
382.20 |
0.3873 |
380.30 |
0.4650 |
378.30 |
0.5389 |
376.80 |
0.6249 |
375.20 |
0.7313 |
373.20 |
0.8186 |
372.00 |
0.9118 |
370.90 |
0.9725 |
370.20 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of 2-Propen-1-ol (1) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0410 |
395.90 |
0.0825 |
393.10 |
0.1208 |
390.90 |
0.1663 |
388.63 |
0.2202 |
386.15 |
0.2670 |
384.30 |
0.3230 |
382.20 |
0.3873 |
380.30 |
0.4650 |
378.30 |
0.5389 |
376.80 |
0.6249 |
375.20 |
0.7313 |
373.20 |
0.8186 |
372.00 |
0.9118 |
370.90 |
0.9725 |
370.20 |
Sources