Datasets
-
Mole fraction (2)
-
Pvap - Vapor or sublimation pressure, kPa (2)
-
Vapor or sublimation pressure, kPa (2)
Mole fraction of 1-Hexanol, 2-ethyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Mole fraction of 1-Hexanol, 2-ethyl- (2) - Fluid (supercritical or subcritical phases) |
| 313.00 |
6800.00 |
0.0006 |
| 313.00 |
7200.00 |
0.0008 |
| 313.00 |
8100.00 |
0.0016 |
| 313.00 |
9000.00 |
0.0150 |
| 313.00 |
9900.00 |
0.0379 |
| 313.00 |
11000.00 |
0.0445 |
| 313.00 |
12000.00 |
0.0434 |
| 313.00 |
12600.00 |
0.0447 |
| 313.00 |
13500.00 |
0.0449 |
| 313.00 |
14400.00 |
0.0445 |
| 313.00 |
15300.00 |
0.0484 |
| 313.00 |
18000.00 |
0.0458 |
| 323.00 |
6800.00 |
0.0008 |
| 323.00 |
7200.00 |
0.0010 |
| 323.00 |
8100.00 |
0.0014 |
| 323.00 |
11000.00 |
0.0148 |
| 323.00 |
12000.00 |
0.0446 |
| 323.00 |
12600.00 |
0.0692 |
| 323.00 |
13500.00 |
0.0666 |
| 323.00 |
14400.00 |
0.0691 |
| 323.00 |
15300.00 |
0.0664 |
| 323.00 |
18000.00 |
0.0687 |
Mole fraction of 1-Hexanol, 2-ethyl- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Mole fraction of 1-Hexanol, 2-ethyl- (2) - Fluid (supercritical or subcritical phases) |
| 313.00 |
6800.00 |
0.0006 |
| 313.00 |
7200.00 |
0.0008 |
| 313.00 |
8100.00 |
0.0016 |
| 313.00 |
9000.00 |
0.0150 |
| 313.00 |
9900.00 |
0.0379 |
| 313.00 |
11000.00 |
0.0445 |
| 313.00 |
12000.00 |
0.0434 |
| 313.00 |
12600.00 |
0.0447 |
| 313.00 |
13500.00 |
0.0449 |
| 313.00 |
14400.00 |
0.0445 |
| 313.00 |
15300.00 |
0.0484 |
| 313.00 |
18000.00 |
0.0458 |
| 323.00 |
6800.00 |
0.0008 |
| 323.00 |
7200.00 |
0.0010 |
| 323.00 |
8100.00 |
0.0014 |
| 323.00 |
11000.00 |
0.0148 |
| 323.00 |
12000.00 |
0.0446 |
| 323.00 |
12600.00 |
0.0692 |
| 323.00 |
13500.00 |
0.0666 |
| 323.00 |
14400.00 |
0.0691 |
| 323.00 |
15300.00 |
0.0664 |
| 323.00 |
18000.00 |
0.0687 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 343.00 |
0.4970 |
9140.00 |
| 343.00 |
0.5990 |
11580.00 |
| 343.00 |
0.7000 |
13360.00 |
| 343.00 |
0.8000 |
13930.00 |
| 353.00 |
0.4970 |
9880.00 |
| 353.00 |
0.5990 |
12600.00 |
| 353.00 |
0.7000 |
14000.00 |
| 353.00 |
0.8000 |
15070.00 |
| 368.00 |
0.4970 |
10630.00 |
| 368.00 |
0.5990 |
13680.00 |
| 368.00 |
0.7000 |
15160.00 |
| 368.00 |
0.8000 |
16470.00 |
| 383.00 |
0.4970 |
11340.00 |
| 383.00 |
0.5990 |
14500.00 |
| 383.00 |
0.7000 |
16630.00 |
| 383.00 |
0.8000 |
18150.00 |
| 393.00 |
0.4970 |
11710.00 |
| 393.00 |
0.5990 |
14970.00 |
| 393.00 |
0.7000 |
17250.00 |
| 393.00 |
0.8000 |
18850.00 |
Vapor or sublimation pressure, kPa
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Carbon dioxide (1) - Liquid |
Vapor or sublimation pressure, kPa - Liquid |
| 343.00 |
0.4970 |
9140.00 |
| 343.00 |
0.5990 |
11580.00 |
| 343.00 |
0.7000 |
13360.00 |
| 343.00 |
0.8000 |
13930.00 |
| 353.00 |
0.4970 |
9880.00 |
| 353.00 |
0.5990 |
12600.00 |
| 353.00 |
0.7000 |
14000.00 |
| 353.00 |
0.8000 |
15070.00 |
| 368.00 |
0.4970 |
10630.00 |
| 368.00 |
0.5990 |
13680.00 |
| 368.00 |
0.7000 |
15160.00 |
| 368.00 |
0.8000 |
16470.00 |
| 383.00 |
0.4970 |
11340.00 |
| 383.00 |
0.5990 |
14500.00 |
| 383.00 |
0.7000 |
16630.00 |
| 383.00 |
0.8000 |
18150.00 |
| 393.00 |
0.4970 |
11710.00 |
| 393.00 |
0.5990 |
14970.00 |
| 393.00 |
0.7000 |
17250.00 |
| 393.00 |
0.8000 |
18850.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mole fraction =
0.901 (Gas)
| Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 343.00 |
13980.00 |
| 353.00 |
15620.00 |
| 368.00 |
17080.00 |
| 383.00 |
18510.00 |
| 393.00 |
19400.00 |
Vapor or sublimation pressure, kPa
[ref]
Operational condition: Mole fraction =
0.901 (Gas)
| Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 343.00 |
13980.00 |
| 353.00 |
15620.00 |
| 368.00 |
17080.00 |
| 383.00 |
18510.00 |
| 393.00 |
19400.00 |
Sources
