Datasets
-
Pvap - Vapor or sublimation pressure, kPa (4)
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2999 |
371.42 |
6140.00 |
0.2999 |
383.30 |
6670.00 |
0.2999 |
392.81 |
6940.00 |
0.3978 |
328.29 |
5550.00 |
0.3978 |
348.21 |
6720.00 |
0.3978 |
371.48 |
8080.00 |
0.3978 |
388.23 |
9040.00 |
0.4635 |
338.92 |
7150.00 |
0.4635 |
357.45 |
8500.00 |
0.4635 |
375.30 |
9810.00 |
0.4635 |
387.20 |
10630.00 |
0.5147 |
328.23 |
6850.00 |
0.5147 |
348.61 |
8570.00 |
0.5147 |
372.20 |
10620.00 |
0.5147 |
398.45 |
12410.00 |
0.6001 |
313.35 |
6130.00 |
0.6001 |
342.37 |
8950.00 |
0.6001 |
371.55 |
11630.00 |
0.6501 |
313.15 |
6330.00 |
0.6501 |
323.25 |
7360.00 |
0.6501 |
333.20 |
8370.00 |
0.6998 |
313.20 |
6510.00 |
0.6998 |
323.25 |
7620.00 |
0.6998 |
333.15 |
8690.00 |
0.7490 |
313.15 |
6620.00 |
0.7490 |
323.15 |
7740.00 |
0.7490 |
333.18 |
8940.00 |
0.7671 |
313.25 |
6670.00 |
0.7671 |
323.20 |
7840.00 |
0.7671 |
333.15 |
8990.00 |
0.8001 |
313.15 |
6930.00 |
0.8001 |
323.15 |
8230.00 |
0.8001 |
333.15 |
9420.00 |
0.8504 |
313.62 |
7210.00 |
0.8504 |
323.22 |
8470.00 |
0.8504 |
333.15 |
9750.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mole fraction =
0.4635 (Liquid)
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
338.95 |
6977.00 |
357.45 |
8587.00 |
375.15 |
9150.00 |
387.15 |
10567.00 |
Vapor or sublimation pressure, kPa
[ref]
Fixed |
Measured |
Mole fraction of Carbon dioxide (1) - Liquid |
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
0.2999 |
371.42 |
6140.00 |
0.2999 |
383.30 |
6670.00 |
0.2999 |
392.81 |
6940.00 |
0.3978 |
328.29 |
5550.00 |
0.3978 |
348.21 |
6720.00 |
0.3978 |
371.48 |
8080.00 |
0.3978 |
388.23 |
9040.00 |
0.4635 |
338.92 |
7150.00 |
0.4635 |
357.45 |
8500.00 |
0.4635 |
375.30 |
9810.00 |
0.4635 |
387.20 |
10630.00 |
0.5147 |
328.23 |
6850.00 |
0.5147 |
348.61 |
8570.00 |
0.5147 |
372.20 |
10620.00 |
0.5147 |
398.45 |
12410.00 |
0.6001 |
313.35 |
6130.00 |
0.6001 |
342.37 |
8950.00 |
0.6001 |
371.55 |
11630.00 |
0.6501 |
313.15 |
6330.00 |
0.6501 |
323.25 |
7360.00 |
0.6501 |
333.20 |
8370.00 |
0.6998 |
313.20 |
6510.00 |
0.6998 |
323.25 |
7620.00 |
0.6998 |
333.15 |
8690.00 |
0.7490 |
313.15 |
6620.00 |
0.7490 |
323.15 |
7740.00 |
0.7490 |
333.18 |
8940.00 |
0.7671 |
313.25 |
6670.00 |
0.7671 |
323.20 |
7840.00 |
0.7671 |
333.15 |
8990.00 |
0.8001 |
313.15 |
6930.00 |
0.8001 |
323.15 |
8230.00 |
0.8001 |
333.15 |
9420.00 |
0.8504 |
313.62 |
7210.00 |
0.8504 |
323.22 |
8470.00 |
0.8504 |
333.15 |
9750.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mole fraction =
0.4635 (Liquid)
Temperature, K - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
338.95 |
6977.00 |
357.45 |
8587.00 |
375.15 |
9150.00 |
387.15 |
10567.00 |
Sources