Mixture of 2-Propenoic acid, ethenyl ester + Carbon dioxide
Datasets
-
Pc - Critical pressure, kPa (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Tc - Critical temperature, K (2)
-
Vapor or sublimation pressure, kPa (2)
Critical pressure, kPa
[ref]
| Mole fraction of 2-Propenoic acid, ethenyl ester (1) - Liquid |
Critical pressure, kPa - Liquid |
| 0.0550 |
10450.00 |
| 0.0830 |
12100.00 |
| 0.1110 |
13140.00 |
| 0.1920 |
13860.00 |
Critical pressure, kPa
[ref]
| Mole fraction of 2-Propenoic acid, ethenyl ester (1) - Liquid |
Critical pressure, kPa - Liquid |
| 0.0550 |
10450.00 |
| 0.0830 |
12100.00 |
| 0.1110 |
13140.00 |
| 0.1920 |
13860.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 2-Propenoic acid, ethenyl ester (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 318.15 |
0.0830 |
8650.00 |
| 318.15 |
0.1110 |
8410.00 |
| 318.15 |
0.1380 |
8140.00 |
| 318.15 |
0.1920 |
7720.00 |
| 318.15 |
0.1990 |
7670.00 |
| 318.15 |
0.2390 |
7210.00 |
| 318.15 |
0.2990 |
6850.00 |
| 318.15 |
0.3580 |
6530.00 |
| 318.15 |
0.4630 |
5620.00 |
| 318.15 |
0.5100 |
5100.00 |
| 318.15 |
0.5700 |
4910.00 |
| 318.15 |
0.5940 |
4620.00 |
| 338.15 |
0.0830 |
10400.00 |
| 338.15 |
0.1110 |
10360.00 |
| 338.15 |
0.1380 |
10240.00 |
| 338.15 |
0.1920 |
9760.00 |
| 338.15 |
0.1990 |
9700.00 |
| 338.15 |
0.2390 |
9250.00 |
| 338.15 |
0.2990 |
8430.00 |
| 338.15 |
0.3580 |
7850.00 |
| 338.15 |
0.4630 |
6930.00 |
| 338.15 |
0.5100 |
6360.00 |
| 338.15 |
0.5700 |
5910.00 |
| 338.15 |
0.5940 |
5590.00 |
| 358.15 |
0.1110 |
12100.00 |
| 358.15 |
0.1380 |
12030.00 |
| 358.15 |
0.1920 |
11690.00 |
| 358.15 |
0.1990 |
11600.00 |
| 358.15 |
0.2390 |
11160.00 |
| 358.15 |
0.2990 |
10290.00 |
| 358.15 |
0.3580 |
9470.00 |
| 358.15 |
0.4630 |
8170.00 |
| 358.15 |
0.5100 |
7540.00 |
| 358.15 |
0.5700 |
6670.00 |
| 358.15 |
0.5940 |
6430.00 |
| 378.15 |
0.1380 |
13280.00 |
| 378.15 |
0.1920 |
13240.00 |
| 378.15 |
0.1990 |
13220.00 |
| 378.15 |
0.2390 |
12780.00 |
| 378.15 |
0.2990 |
11810.00 |
| 378.15 |
0.3580 |
10950.00 |
| 378.15 |
0.4630 |
9310.00 |
| 378.15 |
0.5100 |
8560.00 |
| 378.15 |
0.5700 |
7530.00 |
| 378.15 |
0.5940 |
7190.00 |
| 398.15 |
0.1990 |
13740.00 |
| 398.15 |
0.2390 |
13680.00 |
| 398.15 |
0.2990 |
13020.00 |
| 398.15 |
0.3580 |
11950.00 |
| 398.15 |
0.4630 |
10350.00 |
| 398.15 |
0.5100 |
9570.00 |
| 398.15 |
0.5700 |
8320.00 |
| 398.15 |
0.5940 |
7950.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of 2-Propenoic acid, ethenyl ester (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 318.15 |
0.0830 |
8650.00 |
| 318.15 |
0.1110 |
8410.00 |
| 318.15 |
0.1380 |
8140.00 |
| 318.15 |
0.1920 |
7720.00 |
| 318.15 |
0.1990 |
7670.00 |
| 318.15 |
0.2390 |
7210.00 |
| 318.15 |
0.2990 |
6850.00 |
| 318.15 |
0.3580 |
6530.00 |
| 318.15 |
0.4630 |
5620.00 |
| 318.15 |
0.5100 |
5100.00 |
| 318.15 |
0.5700 |
4910.00 |
| 318.15 |
0.5940 |
4620.00 |
| 338.15 |
0.0830 |
10400.00 |
| 338.15 |
0.1110 |
10360.00 |
| 338.15 |
0.1380 |
10240.00 |
| 338.15 |
0.1920 |
9760.00 |
| 338.15 |
0.1990 |
9700.00 |
| 338.15 |
0.2390 |
9250.00 |
| 338.15 |
0.2990 |
8430.00 |
| 338.15 |
0.3580 |
7850.00 |
| 338.15 |
0.4630 |
6930.00 |
| 338.15 |
0.5100 |
6360.00 |
| 338.15 |
0.5700 |
5910.00 |
| 338.15 |
0.5940 |
5590.00 |
| 358.15 |
0.1110 |
12100.00 |
| 358.15 |
0.1380 |
12030.00 |
| 358.15 |
0.1920 |
11690.00 |
| 358.15 |
0.1990 |
11600.00 |
| 358.15 |
0.2390 |
11160.00 |
| 358.15 |
0.2990 |
10290.00 |
| 358.15 |
0.3580 |
9470.00 |
| 358.15 |
0.4630 |
8170.00 |
| 358.15 |
0.5100 |
7540.00 |
| 358.15 |
0.5700 |
6670.00 |
| 358.15 |
0.5940 |
6430.00 |
| 378.15 |
0.1380 |
13280.00 |
| 378.15 |
0.1920 |
13240.00 |
| 378.15 |
0.1990 |
13220.00 |
| 378.15 |
0.2390 |
12780.00 |
| 378.15 |
0.2990 |
11810.00 |
| 378.15 |
0.3580 |
10950.00 |
| 378.15 |
0.4630 |
9310.00 |
| 378.15 |
0.5100 |
8560.00 |
| 378.15 |
0.5700 |
7530.00 |
| 378.15 |
0.5940 |
7190.00 |
| 398.15 |
0.1990 |
13740.00 |
| 398.15 |
0.2390 |
13680.00 |
| 398.15 |
0.2990 |
13020.00 |
| 398.15 |
0.3580 |
11950.00 |
| 398.15 |
0.4630 |
10350.00 |
| 398.15 |
0.5100 |
9570.00 |
| 398.15 |
0.5700 |
8320.00 |
| 398.15 |
0.5940 |
7950.00 |
Critical temperature, K
[ref]
| Mole fraction of 2-Propenoic acid, ethenyl ester (1) - Liquid |
Critical temperature, K - Liquid |
| 0.0550 |
338.15 |
| 0.0830 |
358.15 |
| 0.1110 |
378.15 |
| 0.1380 |
398.15 |
Critical temperature, K
[ref]
| Mole fraction of 2-Propenoic acid, ethenyl ester (1) - Liquid |
Critical temperature, K - Liquid |
| 0.0550 |
338.15 |
| 0.0830 |
358.15 |
| 0.1110 |
378.15 |
| 0.1380 |
398.15 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of 2-Propenoic acid, ethenyl ester (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 398.15 |
0.1380 |
13760.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of 2-Propenoic acid, ethenyl ester (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 398.15 |
0.1380 |
13760.00 |
Sources
