Operational conditions:
| Mole fraction of 1,2-Ethanediol, monoacetate (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1030 | 0.2880 |
| 0.2310 | 0.5450 |
| 0.3777 | 0.6830 |
| 0.5367 | 0.6990 |
| 0.7024 | 0.5960 |
| 0.8299 | 0.4100 |
| 0.9272 | 0.2070 |
Operational conditions:
| Mole fraction of 1,2-Ethanediol, monoacetate (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.1030 | 0.2880 |
| 0.2310 | 0.5450 |
| 0.3777 | 0.6830 |
| 0.5367 | 0.6990 |
| 0.7024 | 0.5960 |
| 0.8299 | 0.4100 |
| 0.9272 | 0.2070 |
Operational condition: Temperature, K = 363.15 (Liquid)
| Mole fraction of 1,2-Ethanediol, diacetate (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.0000 | 2.23 |
| 0.0019 | 2.24 |
| 0.0040 | 2.24 |
| 0.0059 | 2.26 |
| 0.0107 | 2.27 |
| 0.0199 | 2.29 |
| 0.0421 | 2.35 |
| 0.0703 | 2.40 |
| 0.1068 | 2.45 |
| 0.1541 | 2.51 |
| 0.2134 | 2.58 |
| 0.2789 | 2.63 |
| 0.3461 | 2.67 |
| 0.4174 | 2.70 |
| 0.4852 | 2.73 |
| 0.5624 | 2.76 |
| 0.6458 | 2.78 |
| 0.7293 | 2.79 |
| 0.8023 | 2.80 |
| 0.8631 | 2.79 |
| 0.9131 | 2.79 |
| 0.9545 | 2.79 |
| 0.9748 | 2.78 |
| 0.9852 | 2.77 |
| 0.9901 | 2.77 |
| 0.9950 | 2.76 |
| 1.0000 | 2.74 |
Operational condition: Temperature, K = 363.15 (Liquid)
| Mole fraction of 1,2-Ethanediol, diacetate (1) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
|---|---|
| 0.0000 | 2.23 |
| 0.0019 | 2.24 |
| 0.0040 | 2.24 |
| 0.0059 | 2.26 |
| 0.0107 | 2.27 |
| 0.0199 | 2.29 |
| 0.0421 | 2.35 |
| 0.0703 | 2.40 |
| 0.1068 | 2.45 |
| 0.1541 | 2.51 |
| 0.2134 | 2.58 |
| 0.2789 | 2.63 |
| 0.3461 | 2.67 |
| 0.4174 | 2.70 |
| 0.4852 | 2.73 |
| 0.5624 | 2.76 |
| 0.6458 | 2.78 |
| 0.7293 | 2.79 |
| 0.8023 | 2.80 |
| 0.8631 | 2.79 |
| 0.9131 | 2.79 |
| 0.9545 | 2.79 |
| 0.9748 | 2.78 |
| 0.9852 | 2.77 |
| 0.9901 | 2.77 |
| 0.9950 | 2.76 |
| 1.0000 | 2.74 |