Mixture of Carbon dioxide + 2-Propenoic acid, 2-methyl-, (tetrahydro-2-furanyl)methyl ester
Datasets
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Vapor or sublimation pressure, kPa (2)
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 313.15 |
0.5650 |
5280.00 |
| 313.15 |
0.6090 |
6030.00 |
| 313.15 |
0.6510 |
6020.00 |
| 313.15 |
0.6840 |
6040.00 |
| 313.15 |
0.7250 |
6680.00 |
| 313.15 |
0.7660 |
6860.00 |
| 313.15 |
0.7850 |
7450.00 |
| 313.15 |
0.8280 |
7470.00 |
| 313.15 |
0.8500 |
7530.00 |
| 313.15 |
0.8870 |
7700.00 |
| 313.15 |
0.9000 |
7870.00 |
| 313.15 |
0.9210 |
8050.00 |
| 313.15 |
0.9380 |
8310.00 |
| 313.15 |
0.9460 |
8060.00 |
| 323.15 |
0.5650 |
6180.00 |
| 323.15 |
0.6090 |
6870.00 |
| 323.15 |
0.6510 |
7090.00 |
| 323.15 |
0.6840 |
7280.00 |
| 323.15 |
0.7250 |
8100.00 |
| 323.15 |
0.7660 |
8200.00 |
| 323.15 |
0.7850 |
8870.00 |
| 323.15 |
0.8280 |
9040.00 |
| 323.15 |
0.8500 |
9400.00 |
| 323.15 |
0.8870 |
9440.00 |
| 323.15 |
0.9000 |
9690.00 |
| 323.15 |
0.9210 |
9820.00 |
| 323.15 |
0.9380 |
10150.00 |
| 323.15 |
0.9460 |
9880.00 |
| 333.15 |
0.5650 |
6970.00 |
| 333.15 |
0.6090 |
7870.00 |
| 333.15 |
0.6510 |
8040.00 |
| 333.15 |
0.6840 |
8500.00 |
| 333.15 |
0.7250 |
9390.00 |
| 333.15 |
0.7660 |
9660.00 |
| 333.15 |
0.7850 |
10430.00 |
| 333.15 |
0.8280 |
10860.00 |
| 333.15 |
0.8500 |
11390.00 |
| 333.15 |
0.8870 |
11440.00 |
| 343.15 |
0.5650 |
8000.00 |
| 343.15 |
0.6090 |
8730.00 |
| 343.15 |
0.6510 |
9230.00 |
| 343.15 |
0.6840 |
9850.00 |
| 343.15 |
0.7250 |
10860.00 |
| 343.15 |
0.7660 |
11360.00 |
| 343.15 |
0.7850 |
12080.00 |
| 343.15 |
0.8280 |
12760.00 |
| 343.15 |
0.8500 |
13260.00 |
| 343.15 |
0.8870 |
13500.00 |
| 353.15 |
0.5650 |
9040.00 |
| 353.15 |
0.6090 |
9960.00 |
| 353.15 |
0.6510 |
10550.00 |
| 353.15 |
0.6840 |
11150.00 |
| 353.15 |
0.7250 |
12340.00 |
| 353.15 |
0.7660 |
13040.00 |
| 353.15 |
0.7850 |
13700.00 |
| 353.15 |
0.8280 |
14620.00 |
| 353.15 |
0.8500 |
15020.00 |
| 353.15 |
0.8870 |
15440.00 |
| 363.15 |
0.5650 |
10100.00 |
| 363.15 |
0.6090 |
10660.00 |
| 363.15 |
0.6510 |
11610.00 |
| 363.15 |
0.6840 |
12560.00 |
| 363.15 |
0.7250 |
13600.00 |
| 363.15 |
0.7660 |
14650.00 |
| 363.15 |
0.7850 |
15300.00 |
| 363.15 |
0.8280 |
16440.00 |
| 363.15 |
0.8500 |
16640.00 |
| 363.15 |
0.8870 |
17240.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 313.15 |
0.5650 |
5280.00 |
| 313.15 |
0.6090 |
6030.00 |
| 313.15 |
0.6510 |
6020.00 |
| 313.15 |
0.6840 |
6040.00 |
| 313.15 |
0.7250 |
6680.00 |
| 313.15 |
0.7660 |
6860.00 |
| 313.15 |
0.7850 |
7450.00 |
| 313.15 |
0.8280 |
7470.00 |
| 313.15 |
0.8500 |
7530.00 |
| 313.15 |
0.8870 |
7700.00 |
| 313.15 |
0.9000 |
7870.00 |
| 313.15 |
0.9210 |
8050.00 |
| 313.15 |
0.9380 |
8310.00 |
| 313.15 |
0.9460 |
8060.00 |
| 323.15 |
0.5650 |
6180.00 |
| 323.15 |
0.6090 |
6870.00 |
| 323.15 |
0.6510 |
7090.00 |
| 323.15 |
0.6840 |
7280.00 |
| 323.15 |
0.7250 |
8100.00 |
| 323.15 |
0.7660 |
8200.00 |
| 323.15 |
0.7850 |
8870.00 |
| 323.15 |
0.8280 |
9040.00 |
| 323.15 |
0.8500 |
9400.00 |
| 323.15 |
0.8870 |
9440.00 |
| 323.15 |
0.9000 |
9690.00 |
| 323.15 |
0.9210 |
9820.00 |
| 323.15 |
0.9380 |
10150.00 |
| 323.15 |
0.9460 |
9880.00 |
| 333.15 |
0.5650 |
6970.00 |
| 333.15 |
0.6090 |
7870.00 |
| 333.15 |
0.6510 |
8040.00 |
| 333.15 |
0.6840 |
8500.00 |
| 333.15 |
0.7250 |
9390.00 |
| 333.15 |
0.7660 |
9660.00 |
| 333.15 |
0.7850 |
10430.00 |
| 333.15 |
0.8280 |
10860.00 |
| 333.15 |
0.8500 |
11390.00 |
| 333.15 |
0.8870 |
11440.00 |
| 343.15 |
0.5650 |
8000.00 |
| 343.15 |
0.6090 |
8730.00 |
| 343.15 |
0.6510 |
9230.00 |
| 343.15 |
0.6840 |
9850.00 |
| 343.15 |
0.7250 |
10860.00 |
| 343.15 |
0.7660 |
11360.00 |
| 343.15 |
0.7850 |
12080.00 |
| 343.15 |
0.8280 |
12760.00 |
| 343.15 |
0.8500 |
13260.00 |
| 343.15 |
0.8870 |
13500.00 |
| 353.15 |
0.5650 |
9040.00 |
| 353.15 |
0.6090 |
9960.00 |
| 353.15 |
0.6510 |
10550.00 |
| 353.15 |
0.6840 |
11150.00 |
| 353.15 |
0.7250 |
12340.00 |
| 353.15 |
0.7660 |
13040.00 |
| 353.15 |
0.7850 |
13700.00 |
| 353.15 |
0.8280 |
14620.00 |
| 353.15 |
0.8500 |
15020.00 |
| 353.15 |
0.8870 |
15440.00 |
| 363.15 |
0.5650 |
10100.00 |
| 363.15 |
0.6090 |
10660.00 |
| 363.15 |
0.6510 |
11610.00 |
| 363.15 |
0.6840 |
12560.00 |
| 363.15 |
0.7250 |
13600.00 |
| 363.15 |
0.7660 |
14650.00 |
| 363.15 |
0.7850 |
15300.00 |
| 363.15 |
0.8280 |
16440.00 |
| 363.15 |
0.8500 |
16640.00 |
| 363.15 |
0.8870 |
17240.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 333.15 |
0.9000 |
11710.00 |
| 333.15 |
0.9210 |
11860.00 |
| 333.15 |
0.9380 |
12200.00 |
| 333.15 |
0.9460 |
11820.00 |
| 343.15 |
0.9000 |
13800.00 |
| 343.15 |
0.9210 |
13900.00 |
| 343.15 |
0.9380 |
14160.00 |
| 343.15 |
0.9460 |
13800.00 |
| 353.15 |
0.9000 |
15700.00 |
| 353.15 |
0.9210 |
15790.00 |
| 353.15 |
0.9380 |
16010.00 |
| 353.15 |
0.9460 |
15610.00 |
| 363.15 |
0.9000 |
17410.00 |
| 363.15 |
0.9210 |
17520.00 |
| 363.15 |
0.9380 |
17700.00 |
| 363.15 |
0.9460 |
17200.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 333.15 |
0.9000 |
11710.00 |
| 333.15 |
0.9210 |
11860.00 |
| 333.15 |
0.9380 |
12200.00 |
| 333.15 |
0.9460 |
11820.00 |
| 343.15 |
0.9000 |
13800.00 |
| 343.15 |
0.9210 |
13900.00 |
| 343.15 |
0.9380 |
14160.00 |
| 343.15 |
0.9460 |
13800.00 |
| 353.15 |
0.9000 |
15700.00 |
| 353.15 |
0.9210 |
15790.00 |
| 353.15 |
0.9380 |
16010.00 |
| 353.15 |
0.9460 |
15610.00 |
| 363.15 |
0.9000 |
17410.00 |
| 363.15 |
0.9210 |
17520.00 |
| 363.15 |
0.9380 |
17700.00 |
| 363.15 |
0.9460 |
17200.00 |
Sources
