Mixture of ((oxybis(ethane-2,1-diyl))bis(oxy))bis(ethane-2,1-diyl) bis(2-methylacrylate) + Carbon dioxide
Datasets
-
Vapor or sublimation pressure, kPa
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Fluid (supercritical or subcritical phases) |
Mole fraction of Carbon dioxide (2) - Fluid (supercritical or subcritical phases) |
Vapor or sublimation pressure, kPa - Fluid (supercritical or subcritical phases) |
| 313.20 |
0.6130 |
4440.00 |
| 323.20 |
0.6130 |
5310.00 |
| 323.20 |
0.6630 |
6000.00 |
| 323.20 |
0.6840 |
6560.00 |
| 323.20 |
0.7500 |
8050.00 |
| 323.20 |
0.8030 |
9620.00 |
| 323.20 |
0.8430 |
10740.00 |
| 323.20 |
0.8830 |
13630.00 |
| 323.20 |
0.9120 |
14630.00 |
| 323.20 |
0.9260 |
15350.00 |
| 323.20 |
0.9430 |
15900.00 |
| 323.20 |
0.9680 |
15960.00 |
| 333.20 |
0.6130 |
6120.00 |
| 333.20 |
0.6630 |
6990.00 |
| 333.20 |
0.6840 |
7610.00 |
| 333.20 |
0.7500 |
9440.00 |
| 333.20 |
0.8030 |
11490.00 |
| 333.20 |
0.8430 |
13260.00 |
| 333.20 |
0.8830 |
16520.00 |
| 333.20 |
0.9120 |
17600.00 |
| 333.20 |
0.9260 |
18450.00 |
| 333.20 |
0.9430 |
19050.00 |
| 333.20 |
0.9680 |
18980.00 |
| 343.20 |
0.6130 |
7070.00 |
| 343.20 |
0.6630 |
8140.00 |
| 343.20 |
0.6840 |
8780.00 |
| 343.20 |
0.7500 |
11010.00 |
| 343.20 |
0.8030 |
13600.00 |
| 343.20 |
0.8430 |
15940.00 |
| 343.20 |
0.8830 |
19030.00 |
| 343.20 |
0.9120 |
20340.00 |
| 343.20 |
0.9260 |
21050.00 |
| 343.20 |
0.9430 |
21510.00 |
| 343.20 |
0.9680 |
21240.00 |
| 353.20 |
0.6130 |
8010.00 |
| 353.20 |
0.6630 |
9260.00 |
| 353.20 |
0.6840 |
9970.00 |
| 353.20 |
0.7500 |
12680.00 |
| 353.20 |
0.8030 |
15740.00 |
| 353.20 |
0.8430 |
18450.00 |
| 353.20 |
0.8830 |
21580.00 |
| 353.20 |
0.9120 |
22890.00 |
| 353.20 |
0.9260 |
23720.00 |
| 353.20 |
0.9430 |
24060.00 |
| 353.20 |
0.9680 |
23720.00 |
| 363.20 |
0.6130 |
8980.00 |
| 363.20 |
0.6630 |
10370.00 |
| 363.20 |
0.6840 |
11250.00 |
| 363.20 |
0.7500 |
14010.00 |
| 363.20 |
0.8030 |
17860.00 |
| 363.20 |
0.8430 |
20450.00 |
| 363.20 |
0.8830 |
24110.00 |
| 363.20 |
0.9120 |
25370.00 |
| 363.20 |
0.9260 |
25990.00 |
| 363.20 |
0.9430 |
26340.00 |
| 363.20 |
0.9680 |
26060.00 |
Sources