Mixture of Diisopropyl ether + 2-Butanone, 3-methyl-
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of Diisopropyl ether (1)
[ref]
Fixed |
Measured |
Mole fraction of Diisopropyl ether (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Diisopropyl ether (1) - Gas |
0.0000 |
313.15 |
0.0000 |
0.0300 |
313.15 |
0.1096 |
0.0593 |
313.15 |
0.1910 |
0.1143 |
313.15 |
0.3315 |
0.2171 |
313.15 |
0.4937 |
0.3526 |
313.15 |
0.6284 |
0.4930 |
313.15 |
0.7271 |
0.6188 |
313.15 |
0.7950 |
0.7195 |
313.15 |
0.8466 |
0.8324 |
313.15 |
0.9030 |
0.9289 |
313.15 |
0.9555 |
0.9759 |
313.15 |
0.9818 |
1.0000 |
313.15 |
1.0000 |
0.0000 |
323.15 |
0.0000 |
0.0329 |
323.15 |
0.1117 |
0.0596 |
323.15 |
0.1929 |
0.1153 |
323.15 |
0.3188 |
0.2213 |
323.15 |
0.4859 |
0.3581 |
323.15 |
0.6200 |
0.4965 |
323.15 |
0.7176 |
0.6210 |
323.15 |
0.7884 |
0.7184 |
323.15 |
0.8399 |
0.8323 |
323.15 |
0.8924 |
0.9290 |
323.15 |
0.9544 |
0.9757 |
323.15 |
0.9839 |
1.0000 |
323.15 |
1.0000 |
0.0000 |
333.15 |
0.0000 |
0.0327 |
333.15 |
0.1100 |
0.0624 |
333.15 |
0.1910 |
0.1159 |
333.15 |
0.3083 |
0.2291 |
333.15 |
0.4776 |
0.3638 |
333.15 |
0.6106 |
0.5032 |
333.15 |
0.7097 |
0.6253 |
333.15 |
0.7805 |
0.7180 |
333.15 |
0.8331 |
0.8344 |
333.15 |
0.8979 |
0.9303 |
333.15 |
0.9537 |
0.9768 |
333.15 |
0.9833 |
1.0000 |
333.15 |
1.0000 |
Mole fraction of Diisopropyl ether (1)
[ref]
Fixed |
Measured |
Mole fraction of Diisopropyl ether (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Diisopropyl ether (1) - Gas |
0.0000 |
313.15 |
0.0000 |
0.0300 |
313.15 |
0.1096 |
0.0593 |
313.15 |
0.1910 |
0.1143 |
313.15 |
0.3315 |
0.2171 |
313.15 |
0.4937 |
0.3526 |
313.15 |
0.6284 |
0.4930 |
313.15 |
0.7271 |
0.6188 |
313.15 |
0.7950 |
0.7195 |
313.15 |
0.8466 |
0.8324 |
313.15 |
0.9030 |
0.9289 |
313.15 |
0.9555 |
0.9759 |
313.15 |
0.9818 |
1.0000 |
313.15 |
1.0000 |
0.0000 |
323.15 |
0.0000 |
0.0329 |
323.15 |
0.1117 |
0.0596 |
323.15 |
0.1929 |
0.1153 |
323.15 |
0.3188 |
0.2213 |
323.15 |
0.4859 |
0.3581 |
323.15 |
0.6200 |
0.4965 |
323.15 |
0.7176 |
0.6210 |
323.15 |
0.7884 |
0.7184 |
323.15 |
0.8399 |
0.8323 |
323.15 |
0.8924 |
0.9290 |
323.15 |
0.9544 |
0.9757 |
323.15 |
0.9839 |
1.0000 |
323.15 |
1.0000 |
0.0000 |
333.15 |
0.0000 |
0.0327 |
333.15 |
0.1100 |
0.0624 |
333.15 |
0.1910 |
0.1159 |
333.15 |
0.3083 |
0.2291 |
333.15 |
0.4776 |
0.3638 |
333.15 |
0.6106 |
0.5032 |
333.15 |
0.7097 |
0.6253 |
333.15 |
0.7805 |
0.7180 |
333.15 |
0.8331 |
0.8344 |
333.15 |
0.8979 |
0.9303 |
333.15 |
0.9537 |
0.9768 |
333.15 |
0.9833 |
1.0000 |
333.15 |
1.0000 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Diisopropyl ether (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
313.15 |
13.73 |
0.0300 |
313.15 |
14.94 |
0.0593 |
313.15 |
16.11 |
0.1143 |
313.15 |
18.36 |
0.2171 |
313.15 |
21.83 |
0.3526 |
313.15 |
25.58 |
0.4930 |
313.15 |
28.80 |
0.6188 |
313.15 |
31.17 |
0.7195 |
313.15 |
32.99 |
0.8324 |
313.15 |
34.79 |
0.9289 |
313.15 |
36.21 |
0.9759 |
313.15 |
36.75 |
1.0000 |
313.15 |
37.09 |
0.0000 |
323.15 |
21.09 |
0.0329 |
323.15 |
22.92 |
0.0596 |
323.15 |
24.59 |
0.1153 |
323.15 |
27.63 |
0.2213 |
323.15 |
32.75 |
0.3581 |
323.15 |
38.04 |
0.4965 |
323.15 |
42.54 |
0.6210 |
323.15 |
45.98 |
0.7184 |
323.15 |
48.38 |
0.8323 |
323.15 |
50.84 |
0.9290 |
323.15 |
52.91 |
0.9757 |
323.15 |
53.76 |
1.0000 |
323.15 |
54.14 |
0.0000 |
333.15 |
31.43 |
0.0327 |
333.15 |
34.00 |
0.0624 |
333.15 |
36.40 |
0.1159 |
333.15 |
40.39 |
0.2291 |
333.15 |
47.71 |
0.3638 |
333.15 |
54.93 |
0.5032 |
333.15 |
61.15 |
0.6253 |
333.15 |
65.86 |
0.7180 |
333.15 |
69.03 |
0.8344 |
333.15 |
72.67 |
0.9303 |
333.15 |
75.28 |
0.9768 |
333.15 |
76.41 |
1.0000 |
333.15 |
76.90 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Diisopropyl ether (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.0000 |
313.15 |
13.73 |
0.0300 |
313.15 |
14.94 |
0.0593 |
313.15 |
16.11 |
0.1143 |
313.15 |
18.36 |
0.2171 |
313.15 |
21.83 |
0.3526 |
313.15 |
25.58 |
0.4930 |
313.15 |
28.80 |
0.6188 |
313.15 |
31.17 |
0.7195 |
313.15 |
32.99 |
0.8324 |
313.15 |
34.79 |
0.9289 |
313.15 |
36.21 |
0.9759 |
313.15 |
36.75 |
1.0000 |
313.15 |
37.09 |
0.0000 |
323.15 |
21.09 |
0.0329 |
323.15 |
22.92 |
0.0596 |
323.15 |
24.59 |
0.1153 |
323.15 |
27.63 |
0.2213 |
323.15 |
32.75 |
0.3581 |
323.15 |
38.04 |
0.4965 |
323.15 |
42.54 |
0.6210 |
323.15 |
45.98 |
0.7184 |
323.15 |
48.38 |
0.8323 |
323.15 |
50.84 |
0.9290 |
323.15 |
52.91 |
0.9757 |
323.15 |
53.76 |
1.0000 |
323.15 |
54.14 |
0.0000 |
333.15 |
31.43 |
0.0327 |
333.15 |
34.00 |
0.0624 |
333.15 |
36.40 |
0.1159 |
333.15 |
40.39 |
0.2291 |
333.15 |
47.71 |
0.3638 |
333.15 |
54.93 |
0.5032 |
333.15 |
61.15 |
0.6253 |
333.15 |
65.86 |
0.7180 |
333.15 |
69.03 |
0.8344 |
333.15 |
72.67 |
0.9303 |
333.15 |
75.28 |
0.9768 |
333.15 |
76.41 |
1.0000 |
333.15 |
76.90 |
Sources