Operational conditions:
| Mole fraction of Decanoic acid, methyl ester (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0000 | 0.0000 |
| 0.0636 | 0.1970 |
| 0.1131 | 0.3390 |
| 0.1619 | 0.4490 |
| 0.2010 | 0.5390 |
| 0.2575 | 0.6410 |
| 0.3056 | 0.7100 |
| 0.3584 | 0.7710 |
| 0.3980 | 0.8140 |
| 0.4494 | 0.8270 |
| 0.4955 | 0.8280 |
| 0.5479 | 0.8160 |
| 0.5983 | 0.7860 |
| 0.6494 | 0.7390 |
| 0.7034 | 0.6810 |
| 0.7512 | 0.6080 |
| 0.8015 | 0.5280 |
| 0.8493 | 0.4280 |
| 0.8995 | 0.2960 |
| 0.9495 | 0.1530 |
| 1.0000 | 0.0000 |
Operational conditions:
| Mole fraction of Decanoic acid, methyl ester (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0000 | 0.0000 |
| 0.0636 | 0.1970 |
| 0.1131 | 0.3390 |
| 0.1619 | 0.4490 |
| 0.2010 | 0.5390 |
| 0.2575 | 0.6410 |
| 0.3056 | 0.7100 |
| 0.3584 | 0.7710 |
| 0.3980 | 0.8140 |
| 0.4494 | 0.8270 |
| 0.4955 | 0.8280 |
| 0.5479 | 0.8160 |
| 0.5983 | 0.7860 |
| 0.6494 | 0.7390 |
| 0.7034 | 0.6810 |
| 0.7512 | 0.6080 |
| 0.8015 | 0.5280 |
| 0.8493 | 0.4280 |
| 0.8995 | 0.2960 |
| 0.9495 | 0.1530 |
| 1.0000 | 0.0000 |
Operational conditions:
| Mole fraction of Decanoic acid, methyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 769.8 |
| 0.0499 | 773.1 |
| 0.0998 | 776.6 |
| 0.1501 | 780.26 |
| 0.2000 | 783.98 |
| 0.2497 | 787.88 |
| 0.3006 | 791.99 |
| 0.3497 | 796.11 |
| 0.4001 | 800.47 |
| 0.4500 | 804.97 |
| 0.4997 | 809.64 |
| 0.5502 | 814.55 |
| 0.5995 | 819.57 |
| 0.6501 | 824.85 |
| 0.6996 | 830.28 |
| 0.7497 | 835.95 |
| 0.7997 | 841.91 |
| 0.8489 | 847.93 |
| 0.8992 | 854.43 |
| 0.9494 | 861.11 |
| 1.0000 | 868.02 |
Operational conditions:
| Mole fraction of Decanoic acid, methyl ester (2) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0000 | 769.8 |
| 0.0499 | 773.1 |
| 0.0998 | 776.6 |
| 0.1501 | 780.26 |
| 0.2000 | 783.98 |
| 0.2497 | 787.88 |
| 0.3006 | 791.99 |
| 0.3497 | 796.11 |
| 0.4001 | 800.47 |
| 0.4500 | 804.97 |
| 0.4997 | 809.64 |
| 0.5502 | 814.55 |
| 0.5995 | 819.57 |
| 0.6501 | 824.85 |
| 0.6996 | 830.28 |
| 0.7497 | 835.95 |
| 0.7997 | 841.91 |
| 0.8489 | 847.93 |
| 0.8992 | 854.43 |
| 0.9494 | 861.11 |
| 1.0000 | 868.02 |