Mixture of Acetic acid, pentyl ester + Nonane
Datasets
-
Activity coefficient (2)
-
Excess molar enthalpy (molar enthalpy (2)
-
Excess molar volume, m3/mol (2)
Activity coefficient of Nonane (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Nonane (2) - Liquid |
Pressure, kPa - Liquid |
Activity coefficient of Nonane (2) - Liquid |
| 298.15 |
0.0000 |
101.33 |
2.17 |
Activity coefficient of Nonane (2)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid |
Mole fraction of Nonane (2) - Liquid |
Pressure, kPa - Liquid |
Activity coefficient of Nonane (2) - Liquid |
| 298.15 |
0.0000 |
101.33 |
2.17 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 318.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Acetic acid, pentyl ester (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0676 |
0.3006 |
| 0.1364 |
0.5258 |
| 0.2097 |
0.7229 |
| 0.2818 |
0.8656 |
| 0.3491 |
0.9547 |
| 0.4124 |
1.002 |
| 0.4692 |
1.0151 |
| 0.5191 |
1.002 |
| 0.5639 |
0.9717 |
| 0.6210 |
0.9038 |
| 0.6739 |
0.8432 |
| 0.7288 |
0.7571 |
| 0.7858 |
0.6438 |
| 0.8432 |
0.5037 |
| 0.8986 |
0.3456 |
| 0.9529 |
0.1762 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational conditions:
- Temperature, K = 318.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Acetic acid, pentyl ester (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0676 |
0.3006 |
| 0.1364 |
0.5258 |
| 0.2097 |
0.7229 |
| 0.2818 |
0.8656 |
| 0.3491 |
0.9547 |
| 0.4124 |
1.002 |
| 0.4692 |
1.0151 |
| 0.5191 |
1.002 |
| 0.5639 |
0.9717 |
| 0.6210 |
0.9038 |
| 0.6739 |
0.8432 |
| 0.7288 |
0.7571 |
| 0.7858 |
0.6438 |
| 0.8432 |
0.5037 |
| 0.8986 |
0.3456 |
| 0.9529 |
0.1762 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Temperature, K = 318.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Acetic acid, pentyl ester (1) - Liquid |
Excess molar volume, m3/mol - Liquid |
| 0.0672 |
1.5200e-07 |
| 0.1243 |
2.8300e-07 |
| 0.1813 |
4.1400e-07 |
| 0.2354 |
5.1300e-07 |
| 0.3037 |
5.9700e-07 |
| 0.3405 |
6.3000e-07 |
| 0.3995 |
6.6600e-07 |
| 0.4479 |
6.7500e-07 |
| 0.5035 |
6.7700e-07 |
| 0.5492 |
6.6400e-07 |
| 0.6071 |
6.2400e-07 |
| 0.6461 |
5.9100e-07 |
| 0.6850 |
5.4800e-07 |
| 0.7852 |
4.4900e-07 |
| 0.8739 |
3.4200e-07 |
| 0.9451 |
2.1000e-07 |
Excess molar volume, m3/mol
[ref]
Operational conditions:
- Temperature, K = 318.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Acetic acid, pentyl ester (1) - Liquid |
Excess molar volume, m3/mol - Liquid |
| 0.0672 |
1.5200e-07 |
| 0.1243 |
2.8300e-07 |
| 0.1813 |
4.1400e-07 |
| 0.2354 |
5.1300e-07 |
| 0.3037 |
5.9700e-07 |
| 0.3405 |
6.3000e-07 |
| 0.3995 |
6.6600e-07 |
| 0.4479 |
6.7500e-07 |
| 0.5035 |
6.7700e-07 |
| 0.5492 |
6.6400e-07 |
| 0.6071 |
6.2400e-07 |
| 0.6461 |
5.9100e-07 |
| 0.6850 |
5.4800e-07 |
| 0.7852 |
4.4900e-07 |
| 0.8739 |
3.4200e-07 |
| 0.9451 |
2.1000e-07 |
Sources