Mixture of 2-Propenoic acid, 2-methyl-, 1,2-ethanediylbis(oxy-2,1-ethanediyl) ester + Carbon dioxide
Datasets
-
Vapor or sublimation pressure, kPa (2)
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 |
0.5630 |
4150.00 |
313.20 |
0.6010 |
4740.00 |
313.20 |
0.6670 |
5500.00 |
313.20 |
0.6960 |
5920.00 |
313.20 |
0.7760 |
7080.00 |
313.20 |
0.7970 |
7510.00 |
313.20 |
0.8390 |
7950.00 |
313.20 |
0.8960 |
9050.00 |
313.20 |
0.9370 |
10150.00 |
313.20 |
0.9530 |
10410.00 |
323.20 |
0.5630 |
4900.00 |
323.20 |
0.6010 |
5500.00 |
323.20 |
0.6670 |
6510.00 |
323.20 |
0.6960 |
7010.00 |
323.20 |
0.7370 |
7960.00 |
323.20 |
0.7760 |
8570.00 |
323.20 |
0.7970 |
9160.00 |
323.20 |
0.8390 |
9910.00 |
323.20 |
0.8960 |
11950.00 |
323.20 |
0.9370 |
13680.00 |
323.20 |
0.9530 |
13570.00 |
333.20 |
0.5630 |
5610.00 |
333.20 |
0.6010 |
6350.00 |
333.20 |
0.6670 |
7570.00 |
333.20 |
0.6960 |
8230.00 |
333.20 |
0.7370 |
9700.00 |
333.20 |
0.7760 |
10210.00 |
333.20 |
0.7970 |
11040.00 |
333.20 |
0.8390 |
12180.00 |
333.20 |
0.8960 |
14880.00 |
333.20 |
0.9370 |
16290.00 |
333.20 |
0.9530 |
16460.00 |
343.20 |
0.5630 |
6510.00 |
343.20 |
0.6010 |
7140.00 |
343.20 |
0.6670 |
8670.00 |
343.20 |
0.6960 |
9500.00 |
343.20 |
0.7370 |
11170.00 |
343.20 |
0.7760 |
11950.00 |
343.20 |
0.7970 |
12950.00 |
343.20 |
0.8390 |
14520.00 |
343.20 |
0.8960 |
17560.00 |
343.20 |
0.9370 |
18910.00 |
343.20 |
0.9530 |
19140.00 |
353.20 |
0.5630 |
7290.00 |
353.20 |
0.6010 |
7890.00 |
353.20 |
0.6670 |
9800.00 |
353.20 |
0.6960 |
10870.00 |
353.20 |
0.7370 |
12680.00 |
353.20 |
0.7760 |
13730.00 |
353.20 |
0.7970 |
14920.00 |
353.20 |
0.8390 |
17030.00 |
353.20 |
0.8960 |
20240.00 |
353.20 |
0.9370 |
21060.00 |
353.20 |
0.9530 |
21220.00 |
363.20 |
0.5630 |
8080.00 |
363.20 |
0.6010 |
8750.00 |
363.20 |
0.6670 |
10970.00 |
363.20 |
0.6960 |
12280.00 |
363.20 |
0.7370 |
14390.00 |
363.20 |
0.7760 |
15560.00 |
363.20 |
0.7970 |
16870.00 |
363.20 |
0.8390 |
19260.00 |
363.20 |
0.8960 |
22040.00 |
363.20 |
0.9370 |
23170.00 |
363.20 |
0.9530 |
23300.00 |
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 |
0.5630 |
4150.00 |
313.20 |
0.6010 |
4740.00 |
313.20 |
0.6670 |
5500.00 |
313.20 |
0.6960 |
5920.00 |
313.20 |
0.7760 |
7080.00 |
313.20 |
0.7970 |
7510.00 |
313.20 |
0.8390 |
7950.00 |
313.20 |
0.8960 |
9050.00 |
313.20 |
0.9370 |
10150.00 |
313.20 |
0.9530 |
10410.00 |
323.20 |
0.5630 |
4900.00 |
323.20 |
0.6010 |
5500.00 |
323.20 |
0.6670 |
6510.00 |
323.20 |
0.6960 |
7010.00 |
323.20 |
0.7370 |
7960.00 |
323.20 |
0.7760 |
8570.00 |
323.20 |
0.7970 |
9160.00 |
323.20 |
0.8390 |
9910.00 |
323.20 |
0.8960 |
11950.00 |
323.20 |
0.9370 |
13680.00 |
323.20 |
0.9530 |
13570.00 |
333.20 |
0.5630 |
5610.00 |
333.20 |
0.6010 |
6350.00 |
333.20 |
0.6670 |
7570.00 |
333.20 |
0.6960 |
8230.00 |
333.20 |
0.7370 |
9700.00 |
333.20 |
0.7760 |
10210.00 |
333.20 |
0.7970 |
11040.00 |
333.20 |
0.8390 |
12180.00 |
333.20 |
0.8960 |
14880.00 |
333.20 |
0.9370 |
16290.00 |
333.20 |
0.9530 |
16460.00 |
343.20 |
0.5630 |
6510.00 |
343.20 |
0.6010 |
7140.00 |
343.20 |
0.6670 |
8670.00 |
343.20 |
0.6960 |
9500.00 |
343.20 |
0.7370 |
11170.00 |
343.20 |
0.7760 |
11950.00 |
343.20 |
0.7970 |
12950.00 |
343.20 |
0.8390 |
14520.00 |
343.20 |
0.8960 |
17560.00 |
343.20 |
0.9370 |
18910.00 |
343.20 |
0.9530 |
19140.00 |
353.20 |
0.5630 |
7290.00 |
353.20 |
0.6010 |
7890.00 |
353.20 |
0.6670 |
9800.00 |
353.20 |
0.6960 |
10870.00 |
353.20 |
0.7370 |
12680.00 |
353.20 |
0.7760 |
13730.00 |
353.20 |
0.7970 |
14920.00 |
353.20 |
0.8390 |
17030.00 |
353.20 |
0.8960 |
20240.00 |
353.20 |
0.9370 |
21060.00 |
353.20 |
0.9530 |
21220.00 |
363.20 |
0.5630 |
8080.00 |
363.20 |
0.6010 |
8750.00 |
363.20 |
0.6670 |
10970.00 |
363.20 |
0.6960 |
12280.00 |
363.20 |
0.7370 |
14390.00 |
363.20 |
0.7760 |
15560.00 |
363.20 |
0.7970 |
16870.00 |
363.20 |
0.8390 |
19260.00 |
363.20 |
0.8960 |
22040.00 |
363.20 |
0.9370 |
23170.00 |
363.20 |
0.9530 |
23300.00 |
Sources