Mixture of Carbon dioxide + Propanoic acid, 2-hydroxy-, propyl 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 |
323.20 |
0.5680 |
6200.00 |
323.20 |
0.6080 |
6520.00 |
323.20 |
0.6430 |
6650.00 |
323.20 |
0.7050 |
7380.00 |
323.20 |
0.7440 |
7790.00 |
323.20 |
0.7840 |
8280.00 |
323.20 |
0.8250 |
8500.00 |
323.20 |
0.8640 |
8810.00 |
323.20 |
0.9010 |
8960.00 |
323.20 |
0.9260 |
9250.00 |
333.20 |
0.5680 |
7040.00 |
333.20 |
0.6080 |
7450.00 |
333.20 |
0.6430 |
7710.00 |
333.20 |
0.7050 |
8600.00 |
333.20 |
0.7440 |
9060.00 |
333.20 |
0.7840 |
9660.00 |
333.20 |
0.8250 |
10020.00 |
333.20 |
0.8640 |
10420.00 |
333.20 |
0.9010 |
10550.00 |
343.20 |
0.5680 |
7910.00 |
343.20 |
0.6080 |
8440.00 |
343.20 |
0.6430 |
8770.00 |
343.20 |
0.7050 |
9720.00 |
343.20 |
0.7440 |
10370.00 |
343.20 |
0.7840 |
11080.00 |
343.20 |
0.8250 |
11520.00 |
343.20 |
0.8640 |
12010.00 |
343.20 |
0.9010 |
12140.00 |
353.20 |
0.5680 |
8820.00 |
353.20 |
0.6080 |
9380.00 |
353.20 |
0.6430 |
9900.00 |
353.20 |
0.7050 |
10700.00 |
353.20 |
0.7440 |
11680.00 |
353.20 |
0.7840 |
12460.00 |
353.20 |
0.8250 |
13020.00 |
353.20 |
0.8640 |
13490.00 |
353.20 |
0.9010 |
13710.00 |
363.20 |
0.5680 |
9720.00 |
363.20 |
0.6080 |
10390.00 |
363.20 |
0.6430 |
10930.00 |
363.20 |
0.7050 |
11910.00 |
363.20 |
0.7440 |
12920.00 |
363.20 |
0.7840 |
13710.00 |
363.20 |
0.8250 |
14310.00 |
363.20 |
0.8640 |
14820.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
323.20 |
0.5680 |
6200.00 |
323.20 |
0.6080 |
6520.00 |
323.20 |
0.6430 |
6650.00 |
323.20 |
0.7050 |
7380.00 |
323.20 |
0.7440 |
7790.00 |
323.20 |
0.7840 |
8280.00 |
323.20 |
0.8250 |
8500.00 |
323.20 |
0.8640 |
8810.00 |
323.20 |
0.9010 |
8960.00 |
323.20 |
0.9260 |
9250.00 |
333.20 |
0.5680 |
7040.00 |
333.20 |
0.6080 |
7450.00 |
333.20 |
0.6430 |
7710.00 |
333.20 |
0.7050 |
8600.00 |
333.20 |
0.7440 |
9060.00 |
333.20 |
0.7840 |
9660.00 |
333.20 |
0.8250 |
10020.00 |
333.20 |
0.8640 |
10420.00 |
333.20 |
0.9010 |
10550.00 |
343.20 |
0.5680 |
7910.00 |
343.20 |
0.6080 |
8440.00 |
343.20 |
0.6430 |
8770.00 |
343.20 |
0.7050 |
9720.00 |
343.20 |
0.7440 |
10370.00 |
343.20 |
0.7840 |
11080.00 |
343.20 |
0.8250 |
11520.00 |
343.20 |
0.8640 |
12010.00 |
343.20 |
0.9010 |
12140.00 |
353.20 |
0.5680 |
8820.00 |
353.20 |
0.6080 |
9380.00 |
353.20 |
0.6430 |
9900.00 |
353.20 |
0.7050 |
10700.00 |
353.20 |
0.7440 |
11680.00 |
353.20 |
0.7840 |
12460.00 |
353.20 |
0.8250 |
13020.00 |
353.20 |
0.8640 |
13490.00 |
353.20 |
0.9010 |
13710.00 |
363.20 |
0.5680 |
9720.00 |
363.20 |
0.6080 |
10390.00 |
363.20 |
0.6430 |
10930.00 |
363.20 |
0.7050 |
11910.00 |
363.20 |
0.7440 |
12920.00 |
363.20 |
0.7840 |
13710.00 |
363.20 |
0.8250 |
14310.00 |
363.20 |
0.8640 |
14820.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
323.20 |
0.9460 |
9560.00 |
323.20 |
0.9620 |
9650.00 |
333.20 |
0.9260 |
10840.00 |
333.20 |
0.9460 |
11100.00 |
333.20 |
0.9620 |
11110.00 |
343.20 |
0.9260 |
12420.00 |
343.20 |
0.9460 |
12570.00 |
343.20 |
0.9620 |
12450.00 |
353.20 |
0.9260 |
13820.00 |
353.20 |
0.9460 |
13930.00 |
353.20 |
0.9620 |
13710.00 |
363.20 |
0.9010 |
14970.00 |
363.20 |
0.9260 |
15020.00 |
363.20 |
0.9460 |
15040.00 |
363.20 |
0.9620 |
14760.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Carbon dioxide (1) - Gas |
Vapor or sublimation pressure, kPa - Gas |
323.20 |
0.9460 |
9560.00 |
323.20 |
0.9620 |
9650.00 |
333.20 |
0.9260 |
10840.00 |
333.20 |
0.9460 |
11100.00 |
333.20 |
0.9620 |
11110.00 |
343.20 |
0.9260 |
12420.00 |
343.20 |
0.9460 |
12570.00 |
343.20 |
0.9620 |
12450.00 |
353.20 |
0.9260 |
13820.00 |
353.20 |
0.9460 |
13930.00 |
353.20 |
0.9620 |
13710.00 |
363.20 |
0.9010 |
14970.00 |
363.20 |
0.9260 |
15020.00 |
363.20 |
0.9460 |
15040.00 |
363.20 |
0.9620 |
14760.00 |
Sources