Mixture of Propane, 2-methoxy-2-methyl- + 2-Butanone, 3,3-dimethyl-
Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
| Fixed |
Measured |
| Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Gas |
| 0.0000 |
320.00 |
0.0000 |
| 0.0000 |
330.00 |
0.0000 |
| 0.0000 |
340.00 |
0.0000 |
| 0.0029 |
320.00 |
0.0185 |
| 0.0033 |
330.00 |
0.0304 |
| 0.0058 |
340.00 |
0.0331 |
| 0.0176 |
320.00 |
0.1101 |
| 0.0178 |
330.00 |
0.1048 |
| 0.0183 |
340.00 |
0.0985 |
| 0.0253 |
320.00 |
0.1451 |
| 0.0336 |
330.00 |
0.1881 |
| 0.0356 |
320.00 |
0.1994 |
| 0.0394 |
340.00 |
0.1945 |
| 0.0470 |
320.00 |
0.2531 |
| 0.0630 |
330.00 |
0.3032 |
| 0.0694 |
340.00 |
0.3102 |
| 0.0824 |
330.00 |
0.3651 |
| 0.0903 |
340.00 |
0.3762 |
| 0.1232 |
330.00 |
0.4781 |
| 0.1320 |
340.00 |
0.4735 |
| 0.2011 |
320.00 |
0.6209 |
| 0.2084 |
330.00 |
0.6243 |
| 0.2174 |
340.00 |
0.6111 |
| 0.3095 |
320.00 |
0.7309 |
| 0.3182 |
330.00 |
0.7352 |
| 0.3256 |
340.00 |
0.7254 |
| 0.4140 |
330.00 |
0.7925 |
| 0.4148 |
320.00 |
0.8128 |
| 0.4152 |
340.00 |
0.7890 |
| 0.4987 |
320.00 |
0.8579 |
| 0.5064 |
330.00 |
0.8371 |
| 0.5182 |
340.00 |
0.8416 |
| 0.5793 |
320.00 |
0.8912 |
| 0.5828 |
340.00 |
0.8728 |
| 0.5918 |
330.00 |
0.8856 |
| 0.6501 |
320.00 |
0.9138 |
| 0.6505 |
340.00 |
0.9014 |
| 0.6565 |
330.00 |
0.9084 |
| 0.7331 |
320.00 |
0.9379 |
| 0.7366 |
330.00 |
0.9330 |
| 0.7389 |
340.00 |
0.9277 |
| 0.8192 |
330.00 |
0.9562 |
| 0.8208 |
320.00 |
0.9603 |
| 0.8795 |
320.00 |
0.9737 |
| 0.8799 |
330.00 |
0.9721 |
| 1.0000 |
320.00 |
1.0000 |
| 1.0000 |
330.00 |
1.0000 |
| 1.0000 |
340.00 |
1.0000 |
Mole fraction of Propane, 2-methoxy-2-methyl- (1)
[ref]
| Fixed |
Measured |
| Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid |
Temperature, K - Liquid |
Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Gas |
| 0.0000 |
320.00 |
0.0000 |
| 0.0000 |
330.00 |
0.0000 |
| 0.0000 |
340.00 |
0.0000 |
| 0.0029 |
320.00 |
0.0185 |
| 0.0033 |
330.00 |
0.0304 |
| 0.0058 |
340.00 |
0.0331 |
| 0.0176 |
320.00 |
0.1101 |
| 0.0178 |
330.00 |
0.1048 |
| 0.0183 |
340.00 |
0.0985 |
| 0.0253 |
320.00 |
0.1451 |
| 0.0336 |
330.00 |
0.1881 |
| 0.0356 |
320.00 |
0.1994 |
| 0.0394 |
340.00 |
0.1945 |
| 0.0470 |
320.00 |
0.2531 |
| 0.0630 |
330.00 |
0.3032 |
| 0.0694 |
340.00 |
0.3102 |
| 0.0824 |
330.00 |
0.3651 |
| 0.0903 |
340.00 |
0.3762 |
| 0.1232 |
330.00 |
0.4781 |
| 0.1320 |
340.00 |
0.4735 |
| 0.2011 |
320.00 |
0.6209 |
| 0.2084 |
330.00 |
0.6243 |
| 0.2174 |
340.00 |
0.6111 |
| 0.3095 |
320.00 |
0.7309 |
| 0.3182 |
330.00 |
0.7352 |
| 0.3256 |
340.00 |
0.7254 |
| 0.4140 |
330.00 |
0.7925 |
| 0.4148 |
320.00 |
0.8128 |
| 0.4152 |
340.00 |
0.7890 |
| 0.4987 |
320.00 |
0.8579 |
| 0.5064 |
330.00 |
0.8371 |
| 0.5182 |
340.00 |
0.8416 |
| 0.5793 |
320.00 |
0.8912 |
| 0.5828 |
340.00 |
0.8728 |
| 0.5918 |
330.00 |
0.8856 |
| 0.6501 |
320.00 |
0.9138 |
| 0.6505 |
340.00 |
0.9014 |
| 0.6565 |
330.00 |
0.9084 |
| 0.7331 |
320.00 |
0.9379 |
| 0.7366 |
330.00 |
0.9330 |
| 0.7389 |
340.00 |
0.9277 |
| 0.8192 |
330.00 |
0.9562 |
| 0.8208 |
320.00 |
0.9603 |
| 0.8795 |
320.00 |
0.9737 |
| 0.8799 |
330.00 |
0.9721 |
| 1.0000 |
320.00 |
1.0000 |
| 1.0000 |
330.00 |
1.0000 |
| 1.0000 |
340.00 |
1.0000 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0000 |
320.00 |
12.13 |
| 0.0000 |
330.00 |
18.65 |
| 0.0000 |
340.00 |
27.72 |
| 0.0029 |
320.00 |
12.25 |
| 0.0033 |
330.00 |
19.16 |
| 0.0058 |
340.00 |
28.51 |
| 0.0176 |
320.00 |
13.37 |
| 0.0178 |
330.00 |
20.34 |
| 0.0183 |
340.00 |
30.01 |
| 0.0253 |
320.00 |
13.97 |
| 0.0336 |
330.00 |
22.07 |
| 0.0356 |
320.00 |
14.72 |
| 0.0394 |
340.00 |
32.91 |
| 0.0470 |
320.00 |
15.73 |
| 0.0630 |
330.00 |
25.01 |
| 0.0694 |
340.00 |
37.19 |
| 0.0824 |
330.00 |
27.00 |
| 0.0903 |
340.00 |
40.13 |
| 0.1232 |
330.00 |
31.33 |
| 0.1320 |
340.00 |
45.50 |
| 0.2011 |
320.00 |
27.02 |
| 0.2084 |
330.00 |
39.81 |
| 0.2174 |
340.00 |
56.52 |
| 0.3095 |
320.00 |
34.12 |
| 0.3182 |
330.00 |
49.46 |
| 0.3256 |
340.00 |
69.98 |
| 0.4140 |
330.00 |
57.98 |
| 0.4148 |
320.00 |
40.95 |
| 0.4152 |
340.00 |
80.36 |
| 0.4987 |
320.00 |
46.36 |
| 0.5064 |
330.00 |
66.13 |
| 0.5182 |
340.00 |
92.04 |
| 0.5793 |
320.00 |
51.57 |
| 0.5828 |
340.00 |
100.18 |
| 0.5918 |
330.00 |
73.35 |
| 0.6501 |
320.00 |
55.74 |
| 0.6505 |
340.00 |
109.26 |
| 0.6565 |
330.00 |
78.95 |
| 0.7331 |
320.00 |
60.84 |
| 0.7366 |
330.00 |
85.85 |
| 0.7389 |
340.00 |
118.26 |
| 0.8192 |
330.00 |
92.81 |
| 0.8208 |
320.00 |
66.16 |
| 0.8795 |
320.00 |
69.77 |
| 0.8799 |
330.00 |
98.39 |
| 1.0000 |
320.00 |
76.17 |
| 1.0000 |
330.00 |
108.14 |
| 1.0000 |
340.00 |
146.97 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Mole fraction of Propane, 2-methoxy-2-methyl- (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 0.0000 |
320.00 |
12.13 |
| 0.0000 |
330.00 |
18.65 |
| 0.0000 |
340.00 |
27.72 |
| 0.0029 |
320.00 |
12.25 |
| 0.0033 |
330.00 |
19.16 |
| 0.0058 |
340.00 |
28.51 |
| 0.0176 |
320.00 |
13.37 |
| 0.0178 |
330.00 |
20.34 |
| 0.0183 |
340.00 |
30.01 |
| 0.0253 |
320.00 |
13.97 |
| 0.0336 |
330.00 |
22.07 |
| 0.0356 |
320.00 |
14.72 |
| 0.0394 |
340.00 |
32.91 |
| 0.0470 |
320.00 |
15.73 |
| 0.0630 |
330.00 |
25.01 |
| 0.0694 |
340.00 |
37.19 |
| 0.0824 |
330.00 |
27.00 |
| 0.0903 |
340.00 |
40.13 |
| 0.1232 |
330.00 |
31.33 |
| 0.1320 |
340.00 |
45.50 |
| 0.2011 |
320.00 |
27.02 |
| 0.2084 |
330.00 |
39.81 |
| 0.2174 |
340.00 |
56.52 |
| 0.3095 |
320.00 |
34.12 |
| 0.3182 |
330.00 |
49.46 |
| 0.3256 |
340.00 |
69.98 |
| 0.4140 |
330.00 |
57.98 |
| 0.4148 |
320.00 |
40.95 |
| 0.4152 |
340.00 |
80.36 |
| 0.4987 |
320.00 |
46.36 |
| 0.5064 |
330.00 |
66.13 |
| 0.5182 |
340.00 |
92.04 |
| 0.5793 |
320.00 |
51.57 |
| 0.5828 |
340.00 |
100.18 |
| 0.5918 |
330.00 |
73.35 |
| 0.6501 |
320.00 |
55.74 |
| 0.6505 |
340.00 |
109.26 |
| 0.6565 |
330.00 |
78.95 |
| 0.7331 |
320.00 |
60.84 |
| 0.7366 |
330.00 |
85.85 |
| 0.7389 |
340.00 |
118.26 |
| 0.8192 |
330.00 |
92.81 |
| 0.8208 |
320.00 |
66.16 |
| 0.8795 |
320.00 |
69.77 |
| 0.8799 |
330.00 |
98.39 |
| 1.0000 |
320.00 |
76.17 |
| 1.0000 |
330.00 |
108.14 |
| 1.0000 |
340.00 |
146.97 |
Sources