- 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
- Ethanol
- InChI
- InChI=1S/C2H6O/c1-2-3/h3H,2H2,1H3
- InChI Key
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N
- Formula
- C2H6O
- SMILES
- CCO
- Mol. Weight (g/mol)
- 46.07
- CAS
- 64-17-5
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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 | 0.0495 | 0.2920 |
| 288.20 | 0.0994 | 0.5640 |
| 288.20 | 0.1508 | 0.8120 |
| 288.20 | 0.2004 | 0.9930 |
| 288.20 | 0.2497 | 1.156 |
| 288.20 | 0.3009 | 1.274 |
| 288.20 | 0.3502 | 1.369 |
| 288.20 | 0.4003 | 1.45 |
| 288.20 | 0.4508 | 1.492 |
| 288.20 | 0.5011 | 1.524 |
| 288.20 | 0.5506 | 1.527 |
| 288.20 | 0.5986 | 1.511 |
| 288.20 | 0.6502 | 1.469 |
| 288.20 | 0.6996 | 1.391 |
| 288.20 | 0.7525 | 1.279 |
| 288.20 | 0.8021 | 1.135 |
| 288.20 | 0.8473 | 0.9490 |
| 288.20 | 0.9034 | 0.6860 |
| 288.20 | 0.9460 | 0.4170 |
| 298.20 | 0.0495 | 0.3500 |
| 298.20 | 0.0994 | 0.6720 |
| 298.20 | 0.1508 | 0.9290 |
| 298.20 | 0.2004 | 1.121 |
| 298.20 | 0.2497 | 1.29 |
| 298.20 | 0.3009 | 1.427 |
| 298.20 | 0.3502 | 1.529 |
| 298.20 | 0.4003 | 1.609 |
| 298.20 | 0.4508 | 1.669 |
| 298.20 | 0.5011 | 1.695 |
| 298.20 | 0.5506 | 1.695 |
| 298.20 | 0.5986 | 1.674 |
| 298.20 | 0.6502 | 1.611 |
| 298.20 | 0.6996 | 1.522 |
| 298.20 | 0.7525 | 1.389 |
| 298.20 | 0.8021 | 1.228 |
| 298.20 | 0.8473 | 1.038 |
| 298.20 | 0.9034 | 0.7190 |
| 298.20 | 0.9460 | 0.4210 |
| 313.20 | 0.0495 | 0.3970 |
| 313.20 | 0.0994 | 0.7750 |
| 313.20 | 0.1508 | 1.075 |
| 313.20 | 0.2004 | 1.294 |
| 313.20 | 0.2497 | 1.491 |
| 313.20 | 0.3009 | 1.644 |
| 313.20 | 0.3502 | 1.761 |
| 313.20 | 0.4003 | 1.849 |
| 313.20 | 0.4508 | 1.917 |
| 313.20 | 0.5011 | 1.937 |
| 313.20 | 0.5506 | 1.93 |
| 313.20 | 0.5986 | 1.9 |
| 313.20 | 0.6502 | 1.825 |
| 313.20 | 0.6996 | 1.716 |
| 313.20 | 0.7525 | 1.561 |
| 313.20 | 0.8021 | 1.36 |
| 313.20 | 0.8473 | 1.126 |
| 313.20 | 0.9034 | 0.7950 |
| 313.20 | 0.9460 | 0.4870 |
| 328.20 | 0.0495 | 0.4370 |
| 328.20 | 0.0994 | 0.8590 |
| 328.20 | 0.1508 | 1.203 |
| 328.20 | 0.2004 | 1.451 |
| 328.20 | 0.2497 | 1.676 |
| 328.20 | 0.3009 | 1.832 |
| 328.20 | 0.3502 | 1.969 |
| 328.20 | 0.4003 | 2.064 |
| 328.20 | 0.4508 | 2.126 |
| 328.20 | 0.5011 | 2.145 |
| 328.20 | 0.5506 | 2.139 |
| 328.20 | 0.5986 | 2.088 |
| 328.20 | 0.6502 | 1.998 |
| 328.20 | 0.6996 | 1.872 |
| 328.20 | 0.7525 | 1.674 |
| 328.20 | 0.8021 | 1.446 |
| 328.20 | 0.8473 | 1.204 |
| 328.20 | 0.9034 | 0.8120 |
| 328.20 | 0.9460 | 0.4860 |
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 | 0.0495 | 0.2920 |
| 288.20 | 0.0994 | 0.5640 |
| 288.20 | 0.1508 | 0.8120 |
| 288.20 | 0.2004 | 0.9930 |
| 288.20 | 0.2497 | 1.156 |
| 288.20 | 0.3009 | 1.274 |
| 288.20 | 0.3502 | 1.369 |
| 288.20 | 0.4003 | 1.45 |
| 288.20 | 0.4508 | 1.492 |
| 288.20 | 0.5011 | 1.524 |
| 288.20 | 0.5506 | 1.527 |
| 288.20 | 0.5986 | 1.511 |
| 288.20 | 0.6502 | 1.469 |
| 288.20 | 0.6996 | 1.391 |
| 288.20 | 0.7525 | 1.279 |
| 288.20 | 0.8021 | 1.135 |
| 288.20 | 0.8473 | 0.9490 |
| 288.20 | 0.9034 | 0.6860 |
| 288.20 | 0.9460 | 0.4170 |
| 298.20 | 0.0495 | 0.3500 |
| 298.20 | 0.0994 | 0.6720 |
| 298.20 | 0.1508 | 0.9290 |
| 298.20 | 0.2004 | 1.121 |
| 298.20 | 0.2497 | 1.29 |
| 298.20 | 0.3009 | 1.427 |
| 298.20 | 0.3502 | 1.529 |
| 298.20 | 0.4003 | 1.609 |
| 298.20 | 0.4508 | 1.669 |
| 298.20 | 0.5011 | 1.695 |
| 298.20 | 0.5506 | 1.695 |
| 298.20 | 0.5986 | 1.674 |
| 298.20 | 0.6502 | 1.611 |
| 298.20 | 0.6996 | 1.522 |
| 298.20 | 0.7525 | 1.389 |
| 298.20 | 0.8021 | 1.228 |
| 298.20 | 0.8473 | 1.038 |
| 298.20 | 0.9034 | 0.7190 |
| 298.20 | 0.9460 | 0.4210 |
| 313.20 | 0.0495 | 0.3970 |
| 313.20 | 0.0994 | 0.7750 |
| 313.20 | 0.1508 | 1.075 |
| 313.20 | 0.2004 | 1.294 |
| 313.20 | 0.2497 | 1.491 |
| 313.20 | 0.3009 | 1.644 |
| 313.20 | 0.3502 | 1.761 |
| 313.20 | 0.4003 | 1.849 |
| 313.20 | 0.4508 | 1.917 |
| 313.20 | 0.5011 | 1.937 |
| 313.20 | 0.5506 | 1.93 |
| 313.20 | 0.5986 | 1.9 |
| 313.20 | 0.6502 | 1.825 |
| 313.20 | 0.6996 | 1.716 |
| 313.20 | 0.7525 | 1.561 |
| 313.20 | 0.8021 | 1.36 |
| 313.20 | 0.8473 | 1.126 |
| 313.20 | 0.9034 | 0.7950 |
| 313.20 | 0.9460 | 0.4870 |
| 328.20 | 0.0495 | 0.4370 |
| 328.20 | 0.0994 | 0.8590 |
| 328.20 | 0.1508 | 1.203 |
| 328.20 | 0.2004 | 1.451 |
| 328.20 | 0.2497 | 1.676 |
| 328.20 | 0.3009 | 1.832 |
| 328.20 | 0.3502 | 1.969 |
| 328.20 | 0.4003 | 2.064 |
| 328.20 | 0.4508 | 2.126 |
| 328.20 | 0.5011 | 2.145 |
| 328.20 | 0.5506 | 2.139 |
| 328.20 | 0.5986 | 2.088 |
| 328.20 | 0.6502 | 1.998 |
| 328.20 | 0.6996 | 1.872 |
| 328.20 | 0.7525 | 1.674 |
| 328.20 | 0.8021 | 1.446 |
| 328.20 | 0.8473 | 1.204 |
| 328.20 | 0.9034 | 0.8120 |
| 328.20 | 0.9460 | 0.4860 |