Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Activity coefficient of Ethyl Acetate (2) - Liquid |
---|---|
303.16 | 3.252 |
313.17 | 3.054 |
323.20 | 2.878 |
333.16 | 2.706 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Activity coefficient of Ethyl Acetate (2) - Liquid |
---|---|
303.16 | 3.252 |
313.17 | 3.054 |
323.20 | 2.878 |
333.16 | 2.706 |
Operational conditions:
Mole fraction of Dodecane (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0232 | 0.2360 |
0.0541 | 0.5030 |
0.0898 | 0.7710 |
0.1316 | 1.031 |
0.1800 | 1.279 |
0.2292 | 1.478 |
0.2790 | 1.628 |
0.3296 | 1.74 |
0.3789 | 1.817 |
0.4062 | 1.849 |
0.4261 | 1.859 |
0.4718 | 1.874 |
0.4736 | 1.868 |
0.5534 | 1.798 |
0.6470 | 1.612 |
0.7424 | 1.309 |
0.8396 | 0.8960 |
0.9339 | 0.4230 |
Operational conditions:
Mole fraction of Dodecane (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
---|---|
0.0232 | 0.2360 |
0.0541 | 0.5030 |
0.0898 | 0.7710 |
0.1316 | 1.031 |
0.1800 | 1.279 |
0.2292 | 1.478 |
0.2790 | 1.628 |
0.3296 | 1.74 |
0.3789 | 1.817 |
0.4062 | 1.849 |
0.4261 | 1.859 |
0.4718 | 1.874 |
0.4736 | 1.868 |
0.5534 | 1.798 |
0.6470 | 1.612 |
0.7424 | 1.309 |
0.8396 | 0.8960 |
0.9339 | 0.4230 |
Operational conditions:
Mole fraction of Dodecane (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0970 | 860.06 |
0.1460 | 846.23 |
0.1976 | 833.46 |
0.2508 | 821.88 |
0.2979 | 812.79 |
0.3903 | 797.68 |
0.4943 | 783.92 |
0.6000 | 772.56 |
0.6909 | 764.45 |
0.7392 | 760.65 |
0.7931 | 756.85 |
0.8213 | 754.91 |
0.8798 | 751.38 |
0.9374 | 748.08 |
Operational conditions:
Mole fraction of Dodecane (1) - Liquid | Mass density, kg/m3 - Liquid |
---|---|
0.0970 | 860.06 |
0.1460 | 846.23 |
0.1976 | 833.46 |
0.2508 | 821.88 |
0.2979 | 812.79 |
0.3903 | 797.68 |
0.4943 | 783.92 |
0.6000 | 772.56 |
0.6909 | 764.45 |
0.7392 | 760.65 |
0.7931 | 756.85 |
0.8213 | 754.91 |
0.8798 | 751.38 |
0.9374 | 748.08 |