Mixture of Hexanenitrile + Carbon dioxide
Datasets
-
Pc - Critical pressure, kPa (4)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Vapor or sublimation pressure, kPa (2)
Critical pressure, kPa
[ref]
| Temperature, K - Liquid |
Critical pressure, kPa - Liquid |
| 373.20 |
16720.00 |
| 393.20 |
18520.00 |
Critical pressure, kPa
[ref]
| Mole fraction of Hexanenitrile (1) - Liquid |
Critical pressure, kPa - Liquid |
| 0.1010 |
16720.00 |
| 0.1510 |
18520.00 |
Critical pressure, kPa
[ref]
| Temperature, K - Liquid |
Critical pressure, kPa - Liquid |
| 373.20 |
16720.00 |
| 393.20 |
18520.00 |
Critical pressure, kPa
[ref]
| Mole fraction of Hexanenitrile (1) - Liquid |
Critical pressure, kPa - Liquid |
| 0.1010 |
16720.00 |
| 0.1510 |
18520.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 313.20 |
0.0450 |
9300.00 |
| 313.20 |
0.0580 |
9280.00 |
| 313.20 |
0.1010 |
8830.00 |
| 313.20 |
0.1510 |
8660.00 |
| 313.20 |
0.2060 |
8450.00 |
| 313.20 |
0.2630 |
7550.00 |
| 313.20 |
0.3060 |
7140.00 |
| 313.20 |
0.3610 |
6720.00 |
| 313.20 |
0.4340 |
6040.00 |
| 313.20 |
0.4980 |
5550.00 |
| 313.20 |
0.5700 |
4910.00 |
| 313.20 |
0.6140 |
4520.00 |
| 313.20 |
0.6820 |
3970.00 |
| 333.20 |
0.0580 |
11690.00 |
| 333.20 |
0.1010 |
11830.00 |
| 333.20 |
0.1510 |
11480.00 |
| 333.20 |
0.2060 |
11210.00 |
| 333.20 |
0.2630 |
10170.00 |
| 333.20 |
0.3060 |
9760.00 |
| 333.20 |
0.3610 |
8830.00 |
| 333.20 |
0.4340 |
7620.00 |
| 333.20 |
0.4980 |
6930.00 |
| 333.20 |
0.5700 |
6170.00 |
| 333.20 |
0.6140 |
5550.00 |
| 333.20 |
0.6820 |
4900.00 |
| 353.20 |
0.1010 |
14660.00 |
| 353.20 |
0.1510 |
15000.00 |
| 353.20 |
0.2060 |
14030.00 |
| 353.20 |
0.2630 |
12860.00 |
| 353.20 |
0.3060 |
12170.00 |
| 353.20 |
0.3610 |
11210.00 |
| 353.20 |
0.4340 |
9350.00 |
| 353.20 |
0.4980 |
8310.00 |
| 353.20 |
0.5700 |
7280.00 |
| 353.20 |
0.6140 |
6720.00 |
| 353.20 |
0.6820 |
5690.00 |
| 373.20 |
0.1510 |
17100.00 |
| 373.20 |
0.2060 |
16720.00 |
| 373.20 |
0.2630 |
15070.00 |
| 373.20 |
0.3060 |
14690.00 |
| 373.20 |
0.3610 |
13140.00 |
| 373.20 |
0.4340 |
11070.00 |
| 373.20 |
0.4980 |
9690.00 |
| 373.20 |
0.5700 |
8590.00 |
| 373.20 |
0.6140 |
7620.00 |
| 373.20 |
0.6820 |
6450.00 |
| 393.20 |
0.2060 |
18170.00 |
| 393.20 |
0.2630 |
17380.00 |
| 393.20 |
0.3060 |
16450.00 |
| 393.20 |
0.3610 |
15170.00 |
| 393.20 |
0.4340 |
12860.00 |
| 393.20 |
0.4980 |
11030.00 |
| 393.20 |
0.5700 |
9660.00 |
| 393.20 |
0.6140 |
8590.00 |
| 393.20 |
0.6820 |
7100.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (2) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 313.20 |
0.0450 |
9300.00 |
| 313.20 |
0.0580 |
9280.00 |
| 313.20 |
0.1010 |
8830.00 |
| 313.20 |
0.1510 |
8660.00 |
| 313.20 |
0.2060 |
8450.00 |
| 313.20 |
0.2630 |
7550.00 |
| 313.20 |
0.3060 |
7140.00 |
| 313.20 |
0.3610 |
6720.00 |
| 313.20 |
0.4340 |
6040.00 |
| 313.20 |
0.4980 |
5550.00 |
| 313.20 |
0.5700 |
4910.00 |
| 313.20 |
0.6140 |
4520.00 |
| 313.20 |
0.6820 |
3970.00 |
| 333.20 |
0.0580 |
11690.00 |
| 333.20 |
0.1010 |
11830.00 |
| 333.20 |
0.1510 |
11480.00 |
| 333.20 |
0.2060 |
11210.00 |
| 333.20 |
0.2630 |
10170.00 |
| 333.20 |
0.3060 |
9760.00 |
| 333.20 |
0.3610 |
8830.00 |
| 333.20 |
0.4340 |
7620.00 |
| 333.20 |
0.4980 |
6930.00 |
| 333.20 |
0.5700 |
6170.00 |
| 333.20 |
0.6140 |
5550.00 |
| 333.20 |
0.6820 |
4900.00 |
| 353.20 |
0.1010 |
14660.00 |
| 353.20 |
0.1510 |
15000.00 |
| 353.20 |
0.2060 |
14030.00 |
| 353.20 |
0.2630 |
12860.00 |
| 353.20 |
0.3060 |
12170.00 |
| 353.20 |
0.3610 |
11210.00 |
| 353.20 |
0.4340 |
9350.00 |
| 353.20 |
0.4980 |
8310.00 |
| 353.20 |
0.5700 |
7280.00 |
| 353.20 |
0.6140 |
6720.00 |
| 353.20 |
0.6820 |
5690.00 |
| 373.20 |
0.1510 |
17100.00 |
| 373.20 |
0.2060 |
16720.00 |
| 373.20 |
0.2630 |
15070.00 |
| 373.20 |
0.3060 |
14690.00 |
| 373.20 |
0.3610 |
13140.00 |
| 373.20 |
0.4340 |
11070.00 |
| 373.20 |
0.4980 |
9690.00 |
| 373.20 |
0.5700 |
8590.00 |
| 373.20 |
0.6140 |
7620.00 |
| 373.20 |
0.6820 |
6450.00 |
| 393.20 |
0.2060 |
18170.00 |
| 393.20 |
0.2630 |
17380.00 |
| 393.20 |
0.3060 |
16450.00 |
| 393.20 |
0.3610 |
15170.00 |
| 393.20 |
0.4340 |
12860.00 |
| 393.20 |
0.4980 |
11030.00 |
| 393.20 |
0.5700 |
9660.00 |
| 393.20 |
0.6140 |
8590.00 |
| 393.20 |
0.6820 |
7100.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Carbon dioxide (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 333.20 |
0.0450 |
11660.00 |
| 353.20 |
0.0450 |
13970.00 |
| 353.20 |
0.0580 |
14240.00 |
| 373.20 |
0.0450 |
15620.00 |
| 373.20 |
0.0580 |
16170.00 |
| 393.20 |
0.0450 |
16450.00 |
| 393.20 |
0.0580 |
17210.00 |
| 393.20 |
0.1010 |
18070.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Gas |
Mole fraction of Carbon dioxide (2) - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 333.20 |
0.0450 |
11660.00 |
| 353.20 |
0.0450 |
13970.00 |
| 353.20 |
0.0580 |
14240.00 |
| 373.20 |
0.0450 |
15620.00 |
| 373.20 |
0.0580 |
16170.00 |
| 393.20 |
0.0450 |
16450.00 |
| 393.20 |
0.0580 |
17210.00 |
| 393.20 |
0.1010 |
18070.00 |
Sources
