Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mole fraction of Ethanol (2) - Liquid mixture 2 |
|---|---|
| 294.40 | 0.2551 |
| 298.15 | 0.2918 |
| 308.15 | 0.3836 |
| 318.15 | 0.4907 |
| 323.15 | 0.5544 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Ethanol (2) - Liquid mixture 1 |
|---|---|
| 294.40 | 0.9621 |
| 298.15 | 0.9597 |
| 308.15 | 0.9510 |
| 318.15 | 0.9359 |
| 323.15 | 0.9054 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mole fraction of Ethanol (2) - Liquid mixture 2 |
|---|---|
| 294.40 | 0.2551 |
| 298.15 | 0.2918 |
| 308.15 | 0.3836 |
| 318.15 | 0.4907 |
| 323.15 | 0.5544 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Ethanol (2) - Liquid mixture 1 |
|---|---|
| 294.40 | 0.9621 |
| 298.15 | 0.9597 |
| 308.15 | 0.9510 |
| 318.15 | 0.9359 |
| 323.15 | 0.9054 |
Operational condition: Temperature, K = 325.25 (VLE)
| P [kPa] - VLE | x1[mol/mol] of Ethanol (2) - Liquid |
|---|---|
| 3.6104 | 0.0057 |
| 6.943 | 0.0115 |
| 9.947 | 0.0175 |
| 14.532 | 0.0292 |
| 18.824 | 0.0468 |
| 21.708 | 0.0665 |
| 23.698 | 0.0870 |
| 25.714 | 0.1181 |
| 27.015 | 0.1469 |
| 28.555 | 0.1968 |
| 29.578 | 0.2472 |
| 30.267 | 0.2975 |
| 30.741 | 0.3478 |
| 31.064 | 0.3984 |
| 31.419 | 0.4486 |
| 31.5 | 0.4988 |
| 31.543 | 0.5491 |
| 31.563 | 0.5996 |
| 31.567 | 0.6495 |
| 31.658 | 0.7003 |
| 31.571 | 0.7491 |
| 31.575 | 0.7991 |
| 31.603 | 0.8492 |
| 31.664 | 0.8992 |
| 31.835 | 0.9296 |
| 32.111 | 0.9597 |
| 32.321 | 0.9899 |
| 32.456 | 0.9949 |
Operational condition: Temperature, K = 298.15 (VLE)
| P [kPa] - VLE | x1[mol/mol] of Ethanol (2) - Liquid |
|---|---|
| 5.84 | 0.0860 |
| 6.346 | 0.0920 |
| 7.599 | 0.1910 |
| 7.733 | 0.3800 |
| 7.733 | 0.9600 |
Operational condition: Temperature, K = 313.15 (VLE)
| P [kPa] - VLE | x1[mol/mol] of Ethanol (2) - Liquid |
|---|---|
| 7.946 | 0.0420 |
| 13.212 | 0.0920 |
| 16.385 | 0.1910 |
| 17.305 | 0.5170 |
| 17.305 | 0.9410 |