- Name
- Ethanedioic acid, diethyl ester
- InChI
- InChI=1S/C6H10O4/c1-3-9-5(7)6(8)10-4-2/h3-4H2,1-2H3
- InChI Key
- WYACBZDAHNBPPB-UHFFFAOYSA-N
- Formula
- C6H10O4
- SMILES
- CCOC(=O)C(=O)OCC
- Mol. Weight (g/mol)
- 146.14
- CAS
- 95-92-1
- Name
- Methyl Alcohol
- InChI
- InChI=1S/CH4O/c1-2/h2H,1H3
- InChI Key
- OKKJLVBELUTLKV-UHFFFAOYSA-N
- Formula
- CH4O
- SMILES
- CO
- Mol. Weight (g/mol)
- 32.04
- CAS
- 67-56-1
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Datasets
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanedioic acid, diethyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 288.20 | 0.0494 | 0.1940 |
| 288.20 | 0.1005 | 0.3710 |
| 288.20 | 0.2004 | 0.6510 |
| 288.20 | 0.2507 | 0.7720 |
| 288.20 | 0.2991 | 0.8670 |
| 288.20 | 0.3511 | 0.9450 |
| 288.20 | 0.4019 | 1.012 |
| 288.20 | 0.4496 | 1.055 |
| 288.20 | 0.4975 | 1.092 |
| 288.20 | 0.5509 | 1.112 |
| 288.20 | 0.5969 | 1.109 |
| 288.20 | 0.6475 | 1.09 |
| 288.20 | 0.7033 | 1.032 |
| 288.20 | 0.7469 | 0.9760 |
| 288.20 | 0.8039 | 0.8670 |
| 288.20 | 0.8450 | 0.7540 |
| 288.20 | 0.9005 | 0.5310 |
| 288.20 | 0.9484 | 0.2830 |
| 298.20 | 0.0493 | 0.2190 |
| 298.20 | 0.1004 | 0.4240 |
| 298.20 | 0.1593 | 0.6260 |
| 298.20 | 0.2003 | 0.7410 |
| 298.20 | 0.2505 | 0.8660 |
| 298.20 | 0.2990 | 0.9720 |
| 298.20 | 0.3509 | 1.065 |
| 298.20 | 0.4017 | 1.132 |
| 298.20 | 0.4494 | 1.181 |
| 298.20 | 0.4973 | 1.217 |
| 298.20 | 0.5507 | 1.231 |
| 298.20 | 0.5967 | 1.228 |
| 298.20 | 0.6473 | 1.195 |
| 298.20 | 0.7032 | 1.127 |
| 298.20 | 0.7468 | 1.083 |
| 298.20 | 0.8037 | 0.9960 |
| 298.20 | 0.8449 | 0.8730 |
| 298.20 | 0.9004 | 0.6380 |
| 298.20 | 0.9484 | 0.3710 |
| 313.20 | 0.0493 | 0.2510 |
| 313.20 | 0.1004 | 0.5020 |
| 313.20 | 0.1593 | 0.7380 |
| 313.20 | 0.2003 | 0.8770 |
| 313.20 | 0.2505 | 1.012 |
| 313.20 | 0.2990 | 1.14 |
| 313.20 | 0.3509 | 1.246 |
| 313.20 | 0.4017 | 1.322 |
| 313.20 | 0.4494 | 1.374 |
| 313.20 | 0.4973 | 1.417 |
| 313.20 | 0.5507 | 1.422 |
| 313.20 | 0.5967 | 1.413 |
| 313.20 | 0.6473 | 1.37 |
| 313.20 | 0.7032 | 1.302 |
| 313.20 | 0.7468 | 1.218 |
| 313.20 | 0.8037 | 1.085 |
| 313.20 | 0.8449 | 0.9560 |
| 313.20 | 0.9004 | 0.6510 |
| 313.20 | 0.9484 | 0.3950 |
| 328.20 | 0.0493 | 0.2820 |
| 328.20 | 0.1004 | 0.5800 |
| 328.20 | 0.1593 | 0.8540 |
| 328.20 | 0.2003 | 1.007 |
| 328.20 | 0.2505 | 1.167 |
| 328.20 | 0.2990 | 1.308 |
| 328.20 | 0.3509 | 1.425 |
| 328.20 | 0.4017 | 1.513 |
| 328.20 | 0.4494 | 1.561 |
| 328.20 | 0.4973 | 1.608 |
| 328.20 | 0.5507 | 1.608 |
| 328.20 | 0.5967 | 1.589 |
| 328.20 | 0.6473 | 1.52 |
| 328.20 | 0.7032 | 1.418 |
| 328.20 | 0.7468 | 1.299 |
| 328.20 | 0.8037 | 1.105 |
| 328.20 | 0.8449 | 0.9270 |
| 328.20 | 0.9004 | 0.6170 |
| 328.20 | 0.9484 | 0.3530 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational condition: Pressure, kPa = 101.3 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Ethanedioic acid, diethyl ester (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
| 288.20 | 0.0494 | 0.1940 |
| 288.20 | 0.1005 | 0.3710 |
| 288.20 | 0.2004 | 0.6510 |
| 288.20 | 0.2507 | 0.7720 |
| 288.20 | 0.2991 | 0.8670 |
| 288.20 | 0.3511 | 0.9450 |
| 288.20 | 0.4019 | 1.012 |
| 288.20 | 0.4496 | 1.055 |
| 288.20 | 0.4975 | 1.092 |
| 288.20 | 0.5509 | 1.112 |
| 288.20 | 0.5969 | 1.109 |
| 288.20 | 0.6475 | 1.09 |
| 288.20 | 0.7033 | 1.032 |
| 288.20 | 0.7469 | 0.9760 |
| 288.20 | 0.8039 | 0.8670 |
| 288.20 | 0.8450 | 0.7540 |
| 288.20 | 0.9005 | 0.5310 |
| 288.20 | 0.9484 | 0.2830 |
| 298.20 | 0.0493 | 0.2190 |
| 298.20 | 0.1004 | 0.4240 |
| 298.20 | 0.1593 | 0.6260 |
| 298.20 | 0.2003 | 0.7410 |
| 298.20 | 0.2505 | 0.8660 |
| 298.20 | 0.2990 | 0.9720 |
| 298.20 | 0.3509 | 1.065 |
| 298.20 | 0.4017 | 1.132 |
| 298.20 | 0.4494 | 1.181 |
| 298.20 | 0.4973 | 1.217 |
| 298.20 | 0.5507 | 1.231 |
| 298.20 | 0.5967 | 1.228 |
| 298.20 | 0.6473 | 1.195 |
| 298.20 | 0.7032 | 1.127 |
| 298.20 | 0.7468 | 1.083 |
| 298.20 | 0.8037 | 0.9960 |
| 298.20 | 0.8449 | 0.8730 |
| 298.20 | 0.9004 | 0.6380 |
| 298.20 | 0.9484 | 0.3710 |
| 313.20 | 0.0493 | 0.2510 |
| 313.20 | 0.1004 | 0.5020 |
| 313.20 | 0.1593 | 0.7380 |
| 313.20 | 0.2003 | 0.8770 |
| 313.20 | 0.2505 | 1.012 |
| 313.20 | 0.2990 | 1.14 |
| 313.20 | 0.3509 | 1.246 |
| 313.20 | 0.4017 | 1.322 |
| 313.20 | 0.4494 | 1.374 |
| 313.20 | 0.4973 | 1.417 |
| 313.20 | 0.5507 | 1.422 |
| 313.20 | 0.5967 | 1.413 |
| 313.20 | 0.6473 | 1.37 |
| 313.20 | 0.7032 | 1.302 |
| 313.20 | 0.7468 | 1.218 |
| 313.20 | 0.8037 | 1.085 |
| 313.20 | 0.8449 | 0.9560 |
| 313.20 | 0.9004 | 0.6510 |
| 313.20 | 0.9484 | 0.3950 |
| 328.20 | 0.0493 | 0.2820 |
| 328.20 | 0.1004 | 0.5800 |
| 328.20 | 0.1593 | 0.8540 |
| 328.20 | 0.2003 | 1.007 |
| 328.20 | 0.2505 | 1.167 |
| 328.20 | 0.2990 | 1.308 |
| 328.20 | 0.3509 | 1.425 |
| 328.20 | 0.4017 | 1.513 |
| 328.20 | 0.4494 | 1.561 |
| 328.20 | 0.4973 | 1.608 |
| 328.20 | 0.5507 | 1.608 |
| 328.20 | 0.5967 | 1.589 |
| 328.20 | 0.6473 | 1.52 |
| 328.20 | 0.7032 | 1.418 |
| 328.20 | 0.7468 | 1.299 |
| 328.20 | 0.8037 | 1.105 |
| 328.20 | 0.8449 | 0.9270 |
| 328.20 | 0.9004 | 0.6170 |
| 328.20 | 0.9484 | 0.3530 |