Mixture of Isopropyl Alcohol + N,N-Dimethylaminoethanol
Datasets
-
Excess molar enthalpy (molar enthalpy (2)
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of N,N-Dimethylaminoethanol (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.20 |
100.00 |
0.1008 |
0.0162 |
298.20 |
100.00 |
0.1502 |
0.0279 |
298.20 |
100.00 |
0.1994 |
0.0372 |
298.20 |
100.00 |
0.2501 |
0.0433 |
298.20 |
100.00 |
0.3005 |
0.0467 |
298.20 |
100.00 |
0.3504 |
0.0480 |
298.20 |
100.00 |
0.3999 |
0.0476 |
298.20 |
100.00 |
0.4507 |
0.0454 |
298.20 |
100.00 |
0.5010 |
0.0420 |
298.20 |
100.00 |
0.5505 |
0.0373 |
298.20 |
100.00 |
0.5993 |
0.0328 |
298.20 |
10000.00 |
0.0998 |
0.0136 |
298.20 |
10000.00 |
0.2005 |
0.0345 |
298.20 |
10000.00 |
0.2496 |
0.0401 |
298.20 |
10000.00 |
0.3000 |
0.0433 |
298.20 |
10000.00 |
0.3500 |
0.0447 |
298.20 |
10000.00 |
0.3995 |
0.0446 |
298.20 |
10000.00 |
0.4504 |
0.0431 |
298.20 |
10000.00 |
0.5006 |
0.0406 |
298.20 |
10000.00 |
0.5501 |
0.0372 |
298.20 |
10000.00 |
0.6009 |
0.0330 |
313.20 |
100.00 |
0.0496 |
-0.0169 |
313.20 |
100.00 |
0.1008 |
-0.0173 |
313.20 |
100.00 |
0.1502 |
-0.0127 |
313.20 |
100.00 |
0.1994 |
-0.0070 |
313.20 |
100.00 |
0.2501 |
-0.0027 |
313.20 |
100.00 |
0.3005 |
0.0009 |
313.20 |
100.00 |
0.3504 |
0.0029 |
313.20 |
100.00 |
0.3999 |
0.0034 |
313.20 |
100.00 |
0.4507 |
0.0030 |
313.20 |
100.00 |
0.5010 |
0.0020 |
313.20 |
100.00 |
0.5505 |
-0.0005 |
313.20 |
100.00 |
0.5993 |
-0.0012 |
313.20 |
10000.00 |
0.0499 |
-0.0184 |
313.20 |
10000.00 |
0.0998 |
-0.0194 |
313.20 |
10000.00 |
0.1494 |
-0.0191 |
313.20 |
10000.00 |
0.2005 |
-0.0099 |
313.20 |
10000.00 |
0.2496 |
-0.0056 |
313.20 |
10000.00 |
0.3000 |
-0.0025 |
313.20 |
10000.00 |
0.3500 |
-0.0007 |
313.20 |
10000.00 |
0.3995 |
-0.0001 |
313.20 |
10000.00 |
0.4504 |
-0.0004 |
313.20 |
10000.00 |
0.5006 |
-0.0013 |
313.20 |
10000.00 |
0.5501 |
-0.0026 |
328.20 |
100.00 |
0.0499 |
-0.0359 |
328.20 |
100.00 |
0.1014 |
-0.0511 |
328.20 |
100.00 |
0.1511 |
-0.0566 |
328.20 |
100.00 |
0.2005 |
-0.0574 |
328.20 |
100.00 |
0.2513 |
-0.0566 |
328.20 |
100.00 |
0.3018 |
-0.0553 |
328.20 |
100.00 |
0.3519 |
-0.0543 |
328.20 |
100.00 |
0.4015 |
-0.0533 |
328.20 |
100.00 |
0.4524 |
-0.0518 |
328.20 |
100.00 |
0.5026 |
-0.0501 |
328.20 |
100.00 |
0.5522 |
-0.0481 |
328.20 |
100.00 |
0.6009 |
-0.0458 |
328.20 |
100.00 |
0.6508 |
-0.0429 |
328.20 |
10000.00 |
0.0499 |
-0.0392 |
328.20 |
10000.00 |
0.0998 |
-0.0539 |
328.20 |
10000.00 |
0.2005 |
-0.0607 |
328.20 |
10000.00 |
0.2496 |
-0.0598 |
328.20 |
10000.00 |
0.3000 |
-0.0583 |
328.20 |
10000.00 |
0.3500 |
-0.0566 |
328.20 |
10000.00 |
0.3995 |
-0.0550 |
328.20 |
10000.00 |
0.4504 |
-0.0532 |
328.20 |
10000.00 |
0.5006 |
-0.0513 |
328.20 |
10000.00 |
0.5501 |
-0.0492 |
328.20 |
10000.00 |
0.6009 |
-0.0466 |
328.20 |
10000.00 |
0.6508 |
-0.0457 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of N,N-Dimethylaminoethanol (2) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.20 |
100.00 |
0.1008 |
0.0162 |
298.20 |
100.00 |
0.1502 |
0.0279 |
298.20 |
100.00 |
0.1994 |
0.0372 |
298.20 |
100.00 |
0.2501 |
0.0433 |
298.20 |
100.00 |
0.3005 |
0.0467 |
298.20 |
100.00 |
0.3504 |
0.0480 |
298.20 |
100.00 |
0.3999 |
0.0476 |
298.20 |
100.00 |
0.4507 |
0.0454 |
298.20 |
100.00 |
0.5010 |
0.0420 |
298.20 |
100.00 |
0.5505 |
0.0373 |
298.20 |
100.00 |
0.5993 |
0.0328 |
298.20 |
10000.00 |
0.0998 |
0.0136 |
298.20 |
10000.00 |
0.2005 |
0.0345 |
298.20 |
10000.00 |
0.2496 |
0.0401 |
298.20 |
10000.00 |
0.3000 |
0.0433 |
298.20 |
10000.00 |
0.3500 |
0.0447 |
298.20 |
10000.00 |
0.3995 |
0.0446 |
298.20 |
10000.00 |
0.4504 |
0.0431 |
298.20 |
10000.00 |
0.5006 |
0.0406 |
298.20 |
10000.00 |
0.5501 |
0.0372 |
298.20 |
10000.00 |
0.6009 |
0.0330 |
313.20 |
100.00 |
0.0496 |
-0.0169 |
313.20 |
100.00 |
0.1008 |
-0.0173 |
313.20 |
100.00 |
0.1502 |
-0.0127 |
313.20 |
100.00 |
0.1994 |
-0.0070 |
313.20 |
100.00 |
0.2501 |
-0.0027 |
313.20 |
100.00 |
0.3005 |
0.0009 |
313.20 |
100.00 |
0.3504 |
0.0029 |
313.20 |
100.00 |
0.3999 |
0.0034 |
313.20 |
100.00 |
0.4507 |
0.0030 |
313.20 |
100.00 |
0.5010 |
0.0020 |
313.20 |
100.00 |
0.5505 |
-0.0005 |
313.20 |
100.00 |
0.5993 |
-0.0012 |
313.20 |
10000.00 |
0.0499 |
-0.0184 |
313.20 |
10000.00 |
0.0998 |
-0.0194 |
313.20 |
10000.00 |
0.1494 |
-0.0191 |
313.20 |
10000.00 |
0.2005 |
-0.0099 |
313.20 |
10000.00 |
0.2496 |
-0.0056 |
313.20 |
10000.00 |
0.3000 |
-0.0025 |
313.20 |
10000.00 |
0.3500 |
-0.0007 |
313.20 |
10000.00 |
0.3995 |
-0.0001 |
313.20 |
10000.00 |
0.4504 |
-0.0004 |
313.20 |
10000.00 |
0.5006 |
-0.0013 |
313.20 |
10000.00 |
0.5501 |
-0.0026 |
328.20 |
100.00 |
0.0499 |
-0.0359 |
328.20 |
100.00 |
0.1014 |
-0.0511 |
328.20 |
100.00 |
0.1511 |
-0.0566 |
328.20 |
100.00 |
0.2005 |
-0.0574 |
328.20 |
100.00 |
0.2513 |
-0.0566 |
328.20 |
100.00 |
0.3018 |
-0.0553 |
328.20 |
100.00 |
0.3519 |
-0.0543 |
328.20 |
100.00 |
0.4015 |
-0.0533 |
328.20 |
100.00 |
0.4524 |
-0.0518 |
328.20 |
100.00 |
0.5026 |
-0.0501 |
328.20 |
100.00 |
0.5522 |
-0.0481 |
328.20 |
100.00 |
0.6009 |
-0.0458 |
328.20 |
100.00 |
0.6508 |
-0.0429 |
328.20 |
10000.00 |
0.0499 |
-0.0392 |
328.20 |
10000.00 |
0.0998 |
-0.0539 |
328.20 |
10000.00 |
0.2005 |
-0.0607 |
328.20 |
10000.00 |
0.2496 |
-0.0598 |
328.20 |
10000.00 |
0.3000 |
-0.0583 |
328.20 |
10000.00 |
0.3500 |
-0.0566 |
328.20 |
10000.00 |
0.3995 |
-0.0550 |
328.20 |
10000.00 |
0.4504 |
-0.0532 |
328.20 |
10000.00 |
0.5006 |
-0.0513 |
328.20 |
10000.00 |
0.5501 |
-0.0492 |
328.20 |
10000.00 |
0.6009 |
-0.0466 |
328.20 |
10000.00 |
0.6508 |
-0.0457 |
Sources