Operational conditions:
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Carbon dioxide (2) - Liquid | Mole fraction of n-Hexane (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0480 | 0.9500 | 0.1930 |
| 0.0930 | 0.9020 | 0.3360 |
| 0.1950 | 0.7950 | 0.6050 |
| 0.2490 | 0.7380 | 0.7330 |
| 0.2990 | 0.6850 | 0.8540 |
| 0.3460 | 0.6360 | 0.9060 |
| 0.4030 | 0.5760 | 0.9890 |
| 0.4540 | 0.5220 | 1.024 |
| 0.5010 | 0.4720 | 1.054 |
| 0.5550 | 0.4160 | 1.054 |
| 0.6030 | 0.3650 | 1.032 |
| 0.6470 | 0.3190 | 1.006 |
| 0.7020 | 0.2610 | 0.9370 |
| 0.7500 | 0.2100 | 0.8220 |
| 0.7990 | 0.1590 | 0.7020 |
| 0.8520 | 0.1030 | 0.5170 |
| 0.8990 | 0.0540 | 0.3510 |
| 0.9230 | 0.0280 | 0.2310 |
| 0.9500 | 0.0000 | 0.0970 |
Operational conditions:
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Carbon dioxide (2) - Liquid | Mole fraction of n-Hexane (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 0.0480 | 0.9500 | 0.1930 |
| 0.0930 | 0.9020 | 0.3360 |
| 0.1950 | 0.7950 | 0.6050 |
| 0.2490 | 0.7380 | 0.7330 |
| 0.2990 | 0.6850 | 0.8540 |
| 0.3460 | 0.6360 | 0.9060 |
| 0.4030 | 0.5760 | 0.9890 |
| 0.4540 | 0.5220 | 1.024 |
| 0.5010 | 0.4720 | 1.054 |
| 0.5550 | 0.4160 | 1.054 |
| 0.6030 | 0.3650 | 1.032 |
| 0.6470 | 0.3190 | 1.006 |
| 0.7020 | 0.2610 | 0.9370 |
| 0.7500 | 0.2100 | 0.8220 |
| 0.7990 | 0.1590 | 0.7020 |
| 0.8520 | 0.1030 | 0.5170 |
| 0.8990 | 0.0540 | 0.3510 |
| 0.9230 | 0.0280 | 0.2310 |
| 0.9500 | 0.0000 | 0.0970 |