Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Linalool (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
283.15 | 0.0420 | -0.0130 |
283.15 | 0.0850 | -0.0210 |
283.15 | 0.1740 | -0.0220 |
283.15 | 0.2650 | -0.0120 |
283.15 | 0.3590 | -0.0010 |
283.15 | 0.4570 | 0.0090 |
283.15 | 0.5590 | 0.0240 |
283.15 | 0.6610 | 0.0400 |
283.15 | 0.7710 | 0.0570 |
283.15 | 0.8840 | 0.0590 |
283.15 | 0.9430 | 0.0440 |
298.15 | 0.0420 | -0.0300 |
298.15 | 0.0850 | -0.0600 |
298.15 | 0.1740 | -0.0950 |
298.15 | 0.2650 | -0.1010 |
298.15 | 0.3590 | -0.0910 |
298.15 | 0.4570 | -0.0760 |
298.15 | 0.5590 | -0.0570 |
298.15 | 0.6610 | -0.0280 |
298.15 | 0.7710 | 0.0030 |
298.15 | 0.8840 | 0.0260 |
298.15 | 0.9430 | 0.0220 |
313.15 | 0.0420 | -0.0300 |
313.15 | 0.0850 | -0.0660 |
313.15 | 0.1740 | -0.1460 |
313.15 | 0.2650 | -0.1950 |
313.15 | 0.3590 | -0.2150 |
313.15 | 0.4570 | -0.2130 |
313.15 | 0.5590 | -0.1870 |
313.15 | 0.6610 | -0.1470 |
313.15 | 0.7710 | -0.0920 |
313.15 | 0.8840 | -0.0310 |
313.15 | 0.9430 | -0.0080 |
328.15 | 0.0420 | -0.0220 |
328.15 | 0.0850 | -0.0920 |
328.15 | 0.1740 | -0.2200 |
328.15 | 0.2650 | -0.3030 |
328.15 | 0.3590 | -0.3430 |
328.15 | 0.4570 | -0.3500 |
328.15 | 0.5590 | -0.3260 |
328.15 | 0.6610 | -0.2610 |
328.15 | 0.7710 | -0.1840 |
328.15 | 0.8840 | -0.0880 |
328.15 | 0.9430 | -0.0370 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Linalool (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
283.15 | 0.0420 | -0.0130 |
283.15 | 0.0850 | -0.0210 |
283.15 | 0.1740 | -0.0220 |
283.15 | 0.2650 | -0.0120 |
283.15 | 0.3590 | -0.0010 |
283.15 | 0.4570 | 0.0090 |
283.15 | 0.5590 | 0.0240 |
283.15 | 0.6610 | 0.0400 |
283.15 | 0.7710 | 0.0570 |
283.15 | 0.8840 | 0.0590 |
283.15 | 0.9430 | 0.0440 |
298.15 | 0.0420 | -0.0300 |
298.15 | 0.0850 | -0.0600 |
298.15 | 0.1740 | -0.0950 |
298.15 | 0.2650 | -0.1010 |
298.15 | 0.3590 | -0.0910 |
298.15 | 0.4570 | -0.0760 |
298.15 | 0.5590 | -0.0570 |
298.15 | 0.6610 | -0.0280 |
298.15 | 0.7710 | 0.0030 |
298.15 | 0.8840 | 0.0260 |
298.15 | 0.9430 | 0.0220 |
313.15 | 0.0420 | -0.0300 |
313.15 | 0.0850 | -0.0660 |
313.15 | 0.1740 | -0.1460 |
313.15 | 0.2650 | -0.1950 |
313.15 | 0.3590 | -0.2150 |
313.15 | 0.4570 | -0.2130 |
313.15 | 0.5590 | -0.1870 |
313.15 | 0.6610 | -0.1470 |
313.15 | 0.7710 | -0.0920 |
313.15 | 0.8840 | -0.0310 |
313.15 | 0.9430 | -0.0080 |
328.15 | 0.0420 | -0.0220 |
328.15 | 0.0850 | -0.0920 |
328.15 | 0.1740 | -0.2200 |
328.15 | 0.2650 | -0.3030 |
328.15 | 0.3590 | -0.3430 |
328.15 | 0.4570 | -0.3500 |
328.15 | 0.5590 | -0.3260 |
328.15 | 0.6610 | -0.2610 |
328.15 | 0.7710 | -0.1840 |
328.15 | 0.8840 | -0.0880 |
328.15 | 0.9430 | -0.0370 |