Mixture of Pentanoic acid, ethyl ester + Carbon dioxide + Ethanol
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 (2) - Liquid |
Mole fraction of Pentanoic acid, ethyl ester (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
303.15 |
0.5907 |
0.2048 |
4810.00 |
303.15 |
0.6703 |
0.1650 |
5130.00 |
303.15 |
0.8093 |
0.0954 |
5430.00 |
303.15 |
0.9023 |
0.0489 |
6020.00 |
303.15 |
0.9373 |
0.0314 |
6350.00 |
313.15 |
0.5907 |
0.2048 |
5350.00 |
313.15 |
0.6703 |
0.1650 |
6070.00 |
313.15 |
0.8093 |
0.0954 |
6580.00 |
313.15 |
0.9023 |
0.0489 |
7480.00 |
313.15 |
0.9373 |
0.0314 |
7930.00 |
323.15 |
0.5907 |
0.2048 |
6460.00 |
323.15 |
0.6703 |
0.1650 |
7140.00 |
323.15 |
0.8093 |
0.0954 |
8010.00 |
323.15 |
0.9023 |
0.0489 |
8750.00 |
323.15 |
0.9373 |
0.0314 |
9210.00 |
333.15 |
0.5907 |
0.2048 |
7300.00 |
333.15 |
0.6703 |
0.1650 |
8140.00 |
333.15 |
0.8093 |
0.0954 |
9290.00 |
333.15 |
0.9023 |
0.0489 |
9840.00 |
333.15 |
0.9373 |
0.0314 |
10050.00 |
343.15 |
0.5907 |
0.2048 |
8210.00 |
343.15 |
0.6703 |
0.1650 |
9160.00 |
343.15 |
0.8093 |
0.0954 |
10460.00 |
343.15 |
0.9023 |
0.0489 |
11340.00 |
353.15 |
0.5907 |
0.2048 |
9080.00 |
353.15 |
0.6703 |
0.1650 |
10170.00 |
353.15 |
0.8093 |
0.0954 |
11650.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Mole fraction of Pentanoic acid, ethyl ester (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
303.15 |
0.5907 |
0.2048 |
4810.00 |
303.15 |
0.6703 |
0.1650 |
5130.00 |
303.15 |
0.8093 |
0.0954 |
5430.00 |
303.15 |
0.9023 |
0.0489 |
6020.00 |
303.15 |
0.9373 |
0.0314 |
6350.00 |
313.15 |
0.5907 |
0.2048 |
5350.00 |
313.15 |
0.6703 |
0.1650 |
6070.00 |
313.15 |
0.8093 |
0.0954 |
6580.00 |
313.15 |
0.9023 |
0.0489 |
7480.00 |
313.15 |
0.9373 |
0.0314 |
7930.00 |
323.15 |
0.5907 |
0.2048 |
6460.00 |
323.15 |
0.6703 |
0.1650 |
7140.00 |
323.15 |
0.8093 |
0.0954 |
8010.00 |
323.15 |
0.9023 |
0.0489 |
8750.00 |
323.15 |
0.9373 |
0.0314 |
9210.00 |
333.15 |
0.5907 |
0.2048 |
7300.00 |
333.15 |
0.6703 |
0.1650 |
8140.00 |
333.15 |
0.8093 |
0.0954 |
9290.00 |
333.15 |
0.9023 |
0.0489 |
9840.00 |
333.15 |
0.9373 |
0.0314 |
10050.00 |
343.15 |
0.5907 |
0.2048 |
8210.00 |
343.15 |
0.6703 |
0.1650 |
9160.00 |
343.15 |
0.8093 |
0.0954 |
10460.00 |
343.15 |
0.9023 |
0.0489 |
11340.00 |
353.15 |
0.5907 |
0.2048 |
9080.00 |
353.15 |
0.6703 |
0.1650 |
10170.00 |
353.15 |
0.8093 |
0.0954 |
11650.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Carbon dioxide (2) - Gas |
Mole fraction of Ethanol (3) - Gas |
Vapor or sublimation pressure, kPa - Gas |
343.15 |
0.9373 |
0.0314 |
11150.00 |
353.15 |
0.9023 |
0.0489 |
12290.00 |
353.15 |
0.9373 |
0.0314 |
12270.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Temperature, K - Gas |
Mole fraction of Carbon dioxide (2) - Gas |
Mole fraction of Ethanol (3) - Gas |
Vapor or sublimation pressure, kPa - Gas |
343.15 |
0.9373 |
0.0314 |
11150.00 |
353.15 |
0.9023 |
0.0489 |
12290.00 |
353.15 |
0.9373 |
0.0314 |
12270.00 |
Sources