Operational conditions:
| Mole fraction of 1,2-Ethanediol, diacetate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0219 | 0.2020 |
| 0.0451 | 0.4040 |
| 0.0698 | 0.5940 |
| 0.0960 | 0.7950 |
| 0.1241 | 0.9690 |
| 0.1541 | 1.123 |
| 0.1862 | 1.265 |
| 0.2208 | 1.389 |
| 0.2580 | 1.513 |
| 0.2982 | 1.626 |
| 0.3419 | 1.725 |
| 0.3893 | 1.817 |
| 0.4411 | 1.907 |
| 0.4979 | 1.95 |
| 0.5604 | 1.943 |
| 0.6296 | 1.892 |
| 0.7066 | 1.748 |
| 0.7927 | 1.445 |
| 0.8898 | 0.9050 |
Operational conditions:
| Mole fraction of 1,2-Ethanediol, diacetate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0219 | 0.2020 |
| 0.0451 | 0.4040 |
| 0.0698 | 0.5940 |
| 0.0960 | 0.7950 |
| 0.1241 | 0.9690 |
| 0.1541 | 1.123 |
| 0.1862 | 1.265 |
| 0.2208 | 1.389 |
| 0.2580 | 1.513 |
| 0.2982 | 1.626 |
| 0.3419 | 1.725 |
| 0.3893 | 1.817 |
| 0.4411 | 1.907 |
| 0.4979 | 1.95 |
| 0.5604 | 1.943 |
| 0.6296 | 1.892 |
| 0.7066 | 1.748 |
| 0.7927 | 1.445 |
| 0.8898 | 0.9050 |
Operational condition: Temperature, K = 363.15 (Liquid)
| Mole fraction of 1,2-Ethanediol, diacetate (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.0000 | 1.20 |
| 0.0012 | 1.24 |
| 0.0024 | 1.27 |
| 0.0035 | 1.31 |
| 0.0063 | 1.38 |
| 0.0121 | 1.52 |
| 0.0257 | 1.78 |
| 0.0431 | 2.04 |
| 0.0665 | 2.27 |
| 0.0978 | 2.47 |
| 0.1389 | 2.62 |
| 0.1871 | 2.72 |
| 0.2394 | 2.78 |
| 0.2933 | 2.83 |
| 0.3469 | 2.86 |
| 0.3608 | 2.87 |
| 0.4353 | 2.90 |
| 0.5232 | 2.92 |
| 0.6194 | 2.94 |
| 0.7111 | 2.95 |
| 0.7934 | 2.94 |
| 0.8652 | 2.92 |
| 0.9275 | 2.88 |
| 0.9575 | 2.85 |
| 0.9766 | 2.81 |
| 0.9880 | 2.78 |
| 0.9939 | 2.77 |
| 1.0000 | 2.77 |
Operational condition: Temperature, K = 363.15 (Liquid)
| Mole fraction of 1,2-Ethanediol, diacetate (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.0000 | 1.20 |
| 0.0012 | 1.24 |
| 0.0024 | 1.27 |
| 0.0035 | 1.31 |
| 0.0063 | 1.38 |
| 0.0121 | 1.52 |
| 0.0257 | 1.78 |
| 0.0431 | 2.04 |
| 0.0665 | 2.27 |
| 0.0978 | 2.47 |
| 0.1389 | 2.62 |
| 0.1871 | 2.72 |
| 0.2394 | 2.78 |
| 0.2933 | 2.83 |
| 0.3469 | 2.86 |
| 0.3608 | 2.87 |
| 0.4353 | 2.90 |
| 0.5232 | 2.92 |
| 0.6194 | 2.94 |
| 0.7111 | 2.95 |
| 0.7934 | 2.94 |
| 0.8652 | 2.92 |
| 0.9275 | 2.88 |
| 0.9575 | 2.85 |
| 0.9766 | 2.81 |
| 0.9880 | 2.78 |
| 0.9939 | 2.77 |
| 1.0000 | 2.77 |