Operational conditions:
Mole fraction of 1,2-Ethanediol, monoacetate (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0784 | 0.1820 |
0.1656 | 0.3380 |
0.2632 | 0.4650 |
0.3732 | 0.5510 |
0.4718 | 0.5810 |
0.5815 | 0.5700 |
0.7043 | 0.4910 |
0.8065 | 0.3740 |
0.9188 | 0.1800 |
Operational conditions:
Mole fraction of 1,2-Ethanediol, monoacetate (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0784 | 0.1820 |
0.1656 | 0.3380 |
0.2632 | 0.4650 |
0.3732 | 0.5510 |
0.4718 | 0.5810 |
0.5815 | 0.5700 |
0.7043 | 0.4910 |
0.8065 | 0.3740 |
0.9188 | 0.1800 |
Operational condition: Temperature, K = 363.15 (Liquid)
Mole fraction of 1,2-Ethanediol, monoacetate (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.0000 | 1.28 |
0.0017 | 1.29 |
0.0033 | 1.30 |
0.0050 | 1.31 |
0.0105 | 1.32 |
0.0199 | 1.35 |
0.0382 | 1.41 |
0.0618 | 1.48 |
0.0928 | 1.55 |
0.1335 | 1.64 |
0.1856 | 1.72 |
0.2446 | 1.81 |
0.3073 | 1.88 |
0.3217 | 1.90 |
0.3685 | 1.95 |
0.3774 | 1.95 |
0.4271 | 2.00 |
0.4439 | 2.01 |
0.5211 | 2.08 |
0.6069 | 2.14 |
0.6949 | 2.18 |
0.7733 | 2.20 |
0.8398 | 2.21 |
0.8948 | 2.21 |
0.9406 | 2.22 |
0.9668 | 2.22 |
0.9853 | 2.21 |
0.9930 | 2.21 |
0.9966 | 2.21 |
1.0000 | 2.20 |
Operational condition: Temperature, K = 363.15 (Liquid)
Mole fraction of 1,2-Ethanediol, monoacetate (2) - Liquid | Vapor or sublimation pressure, kPa - Liquid |
---|---|
0.0000 | 1.28 |
0.0017 | 1.29 |
0.0033 | 1.30 |
0.0050 | 1.31 |
0.0105 | 1.32 |
0.0199 | 1.35 |
0.0382 | 1.41 |
0.0618 | 1.48 |
0.0928 | 1.55 |
0.1335 | 1.64 |
0.1856 | 1.72 |
0.2446 | 1.81 |
0.3073 | 1.88 |
0.3217 | 1.90 |
0.3685 | 1.95 |
0.3774 | 1.95 |
0.4271 | 2.00 |
0.4439 | 2.01 |
0.5211 | 2.08 |
0.6069 | 2.14 |
0.6949 | 2.18 |
0.7733 | 2.20 |
0.8398 | 2.21 |
0.8948 | 2.21 |
0.9406 | 2.22 |
0.9668 | 2.22 |
0.9853 | 2.21 |
0.9930 | 2.21 |
0.9966 | 2.21 |
1.0000 | 2.20 |