Mixture of Ethyl formate + 1-Propanol
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 Ethyl formate (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 |
5000.00 |
0.0488 |
0.2957 |
298.15 |
5000.00 |
0.1003 |
0.6274 |
298.15 |
5000.00 |
0.1515 |
0.8878 |
298.15 |
5000.00 |
0.1993 |
1.0799 |
298.15 |
5000.00 |
0.2498 |
1.2412 |
298.15 |
5000.00 |
0.3000 |
1.3566 |
298.15 |
5000.00 |
0.3498 |
1.4393 |
298.15 |
5000.00 |
0.3992 |
1.5016 |
298.15 |
5000.00 |
0.4512 |
1.5184 |
298.15 |
5000.00 |
0.5000 |
1.5123 |
298.15 |
5000.00 |
0.5513 |
1.4786 |
298.15 |
5000.00 |
0.5995 |
1.4271 |
298.15 |
5000.00 |
0.6501 |
1.3511 |
298.15 |
5000.00 |
0.7003 |
1.2409 |
298.15 |
5000.00 |
0.7502 |
1.1072 |
298.15 |
5000.00 |
0.7998 |
0.9394 |
298.15 |
5000.00 |
0.8490 |
0.7581 |
298.15 |
5000.00 |
0.9006 |
0.5171 |
298.15 |
5000.00 |
0.9491 |
0.2786 |
298.15 |
10000.00 |
0.0487 |
0.3313 |
298.15 |
10000.00 |
0.1000 |
0.6597 |
298.15 |
10000.00 |
0.1511 |
0.9204 |
298.15 |
10000.00 |
0.1988 |
1.1134 |
298.15 |
10000.00 |
0.2492 |
1.2672 |
298.15 |
10000.00 |
0.2993 |
1.385 |
298.15 |
10000.00 |
0.3490 |
1.4649 |
298.15 |
10000.00 |
0.4013 |
1.5196 |
298.15 |
10000.00 |
0.4504 |
1.5461 |
298.15 |
10000.00 |
0.4992 |
1.5413 |
298.15 |
10000.00 |
0.5505 |
1.5088 |
298.15 |
10000.00 |
0.5987 |
1.456 |
298.15 |
10000.00 |
0.6493 |
1.3759 |
298.15 |
10000.00 |
0.6996 |
1.2642 |
298.15 |
10000.00 |
0.7496 |
1.13 |
298.15 |
10000.00 |
0.7993 |
0.9697 |
298.15 |
10000.00 |
0.8513 |
0.7708 |
298.15 |
10000.00 |
0.9003 |
0.5508 |
298.15 |
10000.00 |
0.9490 |
0.3011 |
308.15 |
10000.00 |
0.0487 |
0.2943 |
308.15 |
10000.00 |
0.1511 |
0.9246 |
308.15 |
10000.00 |
0.1988 |
1.1271 |
308.15 |
10000.00 |
0.2492 |
1.2928 |
308.15 |
10000.00 |
0.2993 |
1.4208 |
308.15 |
10000.00 |
0.3490 |
1.5101 |
308.15 |
10000.00 |
0.4013 |
1.5724 |
308.15 |
10000.00 |
0.4504 |
1.6025 |
308.15 |
10000.00 |
0.4992 |
1.5977 |
308.15 |
10000.00 |
0.5505 |
1.5641 |
308.15 |
10000.00 |
0.5987 |
1.5019 |
308.15 |
10000.00 |
0.6493 |
1.4106 |
308.15 |
10000.00 |
0.6996 |
1.3028 |
308.15 |
10000.00 |
0.7496 |
1.1555 |
308.15 |
10000.00 |
0.7993 |
0.9796 |
308.15 |
10000.00 |
0.8513 |
0.7760 |
308.15 |
10000.00 |
0.9003 |
0.5603 |
308.15 |
10000.00 |
0.9490 |
0.2691 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Fixed |
Measured |
Temperature, K - Liquid |
Pressure, kPa - Liquid |
Mole fraction of Ethyl formate (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 |
5000.00 |
0.0488 |
0.2957 |
298.15 |
5000.00 |
0.1003 |
0.6274 |
298.15 |
5000.00 |
0.1515 |
0.8878 |
298.15 |
5000.00 |
0.1993 |
1.0799 |
298.15 |
5000.00 |
0.2498 |
1.2412 |
298.15 |
5000.00 |
0.3000 |
1.3566 |
298.15 |
5000.00 |
0.3498 |
1.4393 |
298.15 |
5000.00 |
0.3992 |
1.5016 |
298.15 |
5000.00 |
0.4512 |
1.5184 |
298.15 |
5000.00 |
0.5000 |
1.5123 |
298.15 |
5000.00 |
0.5513 |
1.4786 |
298.15 |
5000.00 |
0.5995 |
1.4271 |
298.15 |
5000.00 |
0.6501 |
1.3511 |
298.15 |
5000.00 |
0.7003 |
1.2409 |
298.15 |
5000.00 |
0.7502 |
1.1072 |
298.15 |
5000.00 |
0.7998 |
0.9394 |
298.15 |
5000.00 |
0.8490 |
0.7581 |
298.15 |
5000.00 |
0.9006 |
0.5171 |
298.15 |
5000.00 |
0.9491 |
0.2786 |
298.15 |
10000.00 |
0.0487 |
0.3313 |
298.15 |
10000.00 |
0.1000 |
0.6597 |
298.15 |
10000.00 |
0.1511 |
0.9204 |
298.15 |
10000.00 |
0.1988 |
1.1134 |
298.15 |
10000.00 |
0.2492 |
1.2672 |
298.15 |
10000.00 |
0.2993 |
1.385 |
298.15 |
10000.00 |
0.3490 |
1.4649 |
298.15 |
10000.00 |
0.4013 |
1.5196 |
298.15 |
10000.00 |
0.4504 |
1.5461 |
298.15 |
10000.00 |
0.4992 |
1.5413 |
298.15 |
10000.00 |
0.5505 |
1.5088 |
298.15 |
10000.00 |
0.5987 |
1.456 |
298.15 |
10000.00 |
0.6493 |
1.3759 |
298.15 |
10000.00 |
0.6996 |
1.2642 |
298.15 |
10000.00 |
0.7496 |
1.13 |
298.15 |
10000.00 |
0.7993 |
0.9697 |
298.15 |
10000.00 |
0.8513 |
0.7708 |
298.15 |
10000.00 |
0.9003 |
0.5508 |
298.15 |
10000.00 |
0.9490 |
0.3011 |
308.15 |
10000.00 |
0.0487 |
0.2943 |
308.15 |
10000.00 |
0.1511 |
0.9246 |
308.15 |
10000.00 |
0.1988 |
1.1271 |
308.15 |
10000.00 |
0.2492 |
1.2928 |
308.15 |
10000.00 |
0.2993 |
1.4208 |
308.15 |
10000.00 |
0.3490 |
1.5101 |
308.15 |
10000.00 |
0.4013 |
1.5724 |
308.15 |
10000.00 |
0.4504 |
1.6025 |
308.15 |
10000.00 |
0.4992 |
1.5977 |
308.15 |
10000.00 |
0.5505 |
1.5641 |
308.15 |
10000.00 |
0.5987 |
1.5019 |
308.15 |
10000.00 |
0.6493 |
1.4106 |
308.15 |
10000.00 |
0.6996 |
1.3028 |
308.15 |
10000.00 |
0.7496 |
1.1555 |
308.15 |
10000.00 |
0.7993 |
0.9796 |
308.15 |
10000.00 |
0.8513 |
0.7760 |
308.15 |
10000.00 |
0.9003 |
0.5603 |
308.15 |
10000.00 |
0.9490 |
0.2691 |
Sources