Operational conditions:
| Mole fraction of n-Amyl ether (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0242 | 0.0190 |
| 0.0473 | 0.0370 |
| 0.0693 | 0.0510 |
| 0.0903 | 0.0650 |
| 0.1104 | 0.0770 |
| 0.1296 | 0.0880 |
| 0.1480 | 0.0980 |
| 0.1657 | 0.1070 |
| 0.1869 | 0.1170 |
| 0.2071 | 0.1260 |
| 0.2262 | 0.1340 |
| 0.2445 | 0.1410 |
| 0.2619 | 0.1470 |
| 0.2786 | 0.1520 |
| 0.2989 | 0.1580 |
| 0.3181 | 0.1630 |
| 0.3363 | 0.1670 |
| 0.3535 | 0.1710 |
| 0.3699 | 0.1740 |
| 0.3855 | 0.1770 |
| 0.4003 | 0.1780 |
| 0.4144 | 0.1790 |
| 0.4310 | 0.1810 |
| 0.4466 | 0.1810 |
| 0.4614 | 0.1820 |
| 0.4754 | 0.1820 |
| 0.4887 | 0.1820 |
| 0.5014 | 0.1810 |
| 0.5129 | 0.1810 |
| 0.5241 | 0.1810 |
| 0.5358 | 0.1800 |
| 0.5481 | 0.1800 |
| 0.5609 | 0.1790 |
| 0.5743 | 0.1780 |
| 0.5884 | 0.1770 |
| 0.6031 | 0.1750 |
| 0.6161 | 0.1730 |
| 0.6297 | 0.1710 |
| 0.6440 | 0.1680 |
| 0.6589 | 0.1660 |
| 0.6745 | 0.1620 |
| 0.6908 | 0.1580 |
| 0.7056 | 0.1530 |
| 0.7210 | 0.1480 |
| 0.7371 | 0.1430 |
| 0.7539 | 0.1370 |
| 0.7715 | 0.1310 |
| 0.7900 | 0.1230 |
| 0.8057 | 0.1170 |
| 0.8221 | 0.1090 |
| 0.8391 | 0.1010 |
| 0.8569 | 0.0920 |
| 0.8754 | 0.0820 |
| 0.8947 | 0.0700 |
| 0.9107 | 0.0610 |
| 0.9273 | 0.0510 |
| 0.9445 | 0.0400 |
| 0.9623 | 0.0270 |
| 0.9808 | 0.0140 |
Operational conditions:
| Mole fraction of n-Amyl ether (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0242 | 0.0190 |
| 0.0473 | 0.0370 |
| 0.0693 | 0.0510 |
| 0.0903 | 0.0650 |
| 0.1104 | 0.0770 |
| 0.1296 | 0.0880 |
| 0.1480 | 0.0980 |
| 0.1657 | 0.1070 |
| 0.1869 | 0.1170 |
| 0.2071 | 0.1260 |
| 0.2262 | 0.1340 |
| 0.2445 | 0.1410 |
| 0.2619 | 0.1470 |
| 0.2786 | 0.1520 |
| 0.2989 | 0.1580 |
| 0.3181 | 0.1630 |
| 0.3363 | 0.1670 |
| 0.3535 | 0.1710 |
| 0.3699 | 0.1740 |
| 0.3855 | 0.1770 |
| 0.4003 | 0.1780 |
| 0.4144 | 0.1790 |
| 0.4310 | 0.1810 |
| 0.4466 | 0.1810 |
| 0.4614 | 0.1820 |
| 0.4754 | 0.1820 |
| 0.4887 | 0.1820 |
| 0.5014 | 0.1810 |
| 0.5129 | 0.1810 |
| 0.5241 | 0.1810 |
| 0.5358 | 0.1800 |
| 0.5481 | 0.1800 |
| 0.5609 | 0.1790 |
| 0.5743 | 0.1780 |
| 0.5884 | 0.1770 |
| 0.6031 | 0.1750 |
| 0.6161 | 0.1730 |
| 0.6297 | 0.1710 |
| 0.6440 | 0.1680 |
| 0.6589 | 0.1660 |
| 0.6745 | 0.1620 |
| 0.6908 | 0.1580 |
| 0.7056 | 0.1530 |
| 0.7210 | 0.1480 |
| 0.7371 | 0.1430 |
| 0.7539 | 0.1370 |
| 0.7715 | 0.1310 |
| 0.7900 | 0.1230 |
| 0.8057 | 0.1170 |
| 0.8221 | 0.1090 |
| 0.8391 | 0.1010 |
| 0.8569 | 0.0920 |
| 0.8754 | 0.0820 |
| 0.8947 | 0.0700 |
| 0.9107 | 0.0610 |
| 0.9273 | 0.0510 |
| 0.9445 | 0.0400 |
| 0.9623 | 0.0270 |
| 0.9808 | 0.0140 |