Mixture of Carbon dioxide + Benzaldehyde, 2-hydroxy-3-methoxy-
Datasets
-
Mole fraction (2)
-
Vapor or sublimation pressure, kPa (2)
Mole fraction of Benzaldehyde, 2-hydroxy-3-methoxy- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Mole fraction of Benzaldehyde, 2-hydroxy-3-methoxy- (2) - Fluid (supercritical or subcritical phases) |
| 313.20 |
8900.00 |
0.0027 |
| 313.20 |
10650.00 |
0.0041 |
| 313.20 |
14650.00 |
0.0106 |
| 313.20 |
16800.00 |
0.0202 |
| 313.20 |
20380.00 |
0.0344 |
| 313.20 |
22600.00 |
0.0520 |
| 313.20 |
26450.00 |
0.0635 |
| 313.20 |
29200.00 |
0.0650 |
| 313.20 |
30200.00 |
0.0641 |
| 333.20 |
7830.00 |
0.0005 |
| 333.20 |
11600.00 |
0.0051 |
| 333.20 |
15200.00 |
0.0141 |
| 333.20 |
17750.00 |
0.0272 |
| 333.20 |
20100.00 |
0.0341 |
| 333.20 |
21400.00 |
0.0392 |
| 333.20 |
22980.00 |
0.0452 |
| 333.20 |
25100.00 |
0.0457 |
| 333.20 |
25650.00 |
0.0437 |
| 333.20 |
27100.00 |
0.0402 |
| 333.20 |
28430.00 |
0.0361 |
| 333.20 |
30370.00 |
0.0326 |
| 353.20 |
8130.00 |
0.0006 |
| 353.20 |
11100.00 |
0.0018 |
| 353.20 |
14500.00 |
0.0119 |
| 353.20 |
17480.00 |
0.0236 |
| 353.20 |
19830.00 |
0.0337 |
| 353.20 |
22650.00 |
0.0370 |
| 353.20 |
24200.00 |
0.0424 |
| 353.20 |
25350.00 |
0.0386 |
| 353.20 |
27650.00 |
0.0416 |
| 353.20 |
30030.00 |
0.0440 |
Mole fraction of Benzaldehyde, 2-hydroxy-3-methoxy- (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Fluid (supercritical or subcritical phases) |
Pressure, kPa - Fluid (supercritical or subcritical phases) |
Mole fraction of Benzaldehyde, 2-hydroxy-3-methoxy- (2) - Fluid (supercritical or subcritical phases) |
| 313.20 |
8900.00 |
0.0027 |
| 313.20 |
10650.00 |
0.0041 |
| 313.20 |
14650.00 |
0.0106 |
| 313.20 |
16800.00 |
0.0202 |
| 313.20 |
20380.00 |
0.0344 |
| 313.20 |
22600.00 |
0.0520 |
| 313.20 |
26450.00 |
0.0635 |
| 313.20 |
29200.00 |
0.0650 |
| 313.20 |
30200.00 |
0.0641 |
| 333.20 |
7830.00 |
0.0005 |
| 333.20 |
11600.00 |
0.0051 |
| 333.20 |
15200.00 |
0.0141 |
| 333.20 |
17750.00 |
0.0272 |
| 333.20 |
20100.00 |
0.0341 |
| 333.20 |
21400.00 |
0.0392 |
| 333.20 |
22980.00 |
0.0452 |
| 333.20 |
25100.00 |
0.0457 |
| 333.20 |
25650.00 |
0.0437 |
| 333.20 |
27100.00 |
0.0402 |
| 333.20 |
28430.00 |
0.0361 |
| 333.20 |
30370.00 |
0.0326 |
| 353.20 |
8130.00 |
0.0006 |
| 353.20 |
11100.00 |
0.0018 |
| 353.20 |
14500.00 |
0.0119 |
| 353.20 |
17480.00 |
0.0236 |
| 353.20 |
19830.00 |
0.0337 |
| 353.20 |
22650.00 |
0.0370 |
| 353.20 |
24200.00 |
0.0424 |
| 353.20 |
25350.00 |
0.0386 |
| 353.20 |
27650.00 |
0.0416 |
| 353.20 |
30030.00 |
0.0440 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 294.00 |
5500.00 |
| 299.20 |
4680.00 |
| 301.30 |
4250.00 |
| 304.20 |
3630.00 |
| 309.30 |
2230.00 |
| 313.20 |
1030.00 |
| 314.60 |
550.00 |
| 315.60 |
400.00 |
| 315.70 |
200.00 |
| 316.10 |
50.00 |
| 316.60 |
100.00 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Gas |
Vapor or sublimation pressure, kPa - Gas |
| 294.00 |
5500.00 |
| 299.20 |
4680.00 |
| 301.30 |
4250.00 |
| 304.20 |
3630.00 |
| 309.30 |
2230.00 |
| 313.20 |
1030.00 |
| 314.60 |
550.00 |
| 315.60 |
400.00 |
| 315.70 |
200.00 |
| 316.10 |
50.00 |
| 316.60 |
100.00 |
Sources
