- 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
- 1-Propanol
- InChI
- InChI=1S/C3H8O/c1-2-3-4/h4H,2-3H2,1H3
- InChI Key
- BDERNNFJNOPAEC-UHFFFAOYSA-N
- Formula
- C3H8O
- SMILES
- CCCO
- Mol. Weight (g/mol)
- 60.09
- CAS
- 71-23-8
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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 | 0.0505 | 0.4450 |
| 288.20 | 0.1001 | 0.7810 |
| 288.20 | 0.1509 | 1.056 |
| 288.20 | 0.1998 | 1.269 |
| 288.20 | 0.2491 | 1.429 |
| 288.20 | 0.2986 | 1.571 |
| 288.20 | 0.3478 | 1.672 |
| 288.20 | 0.4003 | 1.754 |
| 288.20 | 0.4482 | 1.8 |
| 288.20 | 0.4990 | 1.839 |
| 288.20 | 0.5484 | 1.829 |
| 288.20 | 0.6007 | 1.8 |
| 288.20 | 0.6509 | 1.736 |
| 288.20 | 0.6986 | 1.642 |
| 288.20 | 0.7487 | 1.51 |
| 288.20 | 0.8015 | 1.325 |
| 288.20 | 0.8509 | 1.101 |
| 288.20 | 0.9028 | 0.8040 |
| 288.20 | 0.9503 | 0.4240 |
| 298.20 | 0.0505 | 0.4710 |
| 298.20 | 0.1001 | 0.8450 |
| 298.20 | 0.1509 | 1.154 |
| 298.20 | 0.1998 | 1.387 |
| 298.20 | 0.2491 | 1.588 |
| 298.20 | 0.2986 | 1.723 |
| 298.20 | 0.3478 | 1.858 |
| 298.20 | 0.4003 | 1.948 |
| 298.20 | 0.4482 | 1.987 |
| 298.20 | 0.4990 | 2.025 |
| 298.20 | 0.5484 | 2.009 |
| 298.20 | 0.6007 | 1.98 |
| 298.20 | 0.6509 | 1.894 |
| 298.20 | 0.6986 | 1.777 |
| 298.20 | 0.7487 | 1.622 |
| 298.20 | 0.8015 | 1.424 |
| 298.20 | 0.8509 | 1.177 |
| 298.20 | 0.9028 | 0.8220 |
| 298.20 | 0.9503 | 0.4500 |
| 313.20 | 0.0505 | 0.5140 |
| 313.20 | 0.1001 | 0.9710 |
| 313.20 | 0.1509 | 1.319 |
| 313.20 | 0.1998 | 1.58 |
| 313.20 | 0.2491 | 1.811 |
| 313.20 | 0.2986 | 1.965 |
| 313.20 | 0.3478 | 2.11 |
| 313.20 | 0.4003 | 2.211 |
| 313.20 | 0.4482 | 2.252 |
| 313.20 | 0.4990 | 2.279 |
| 313.20 | 0.5484 | 2.256 |
| 313.20 | 0.6007 | 2.196 |
| 313.20 | 0.6509 | 2.109 |
| 313.20 | 0.6986 | 1.97 |
| 313.20 | 0.7487 | 1.797 |
| 313.20 | 0.8015 | 1.536 |
| 313.20 | 0.8509 | 1.25 |
| 313.20 | 0.9028 | 0.8790 |
| 313.20 | 0.9503 | 0.4540 |
| 328.20 | 0.0505 | 0.5630 |
| 328.20 | 0.1001 | 1.041 |
| 328.20 | 0.1509 | 1.429 |
| 328.20 | 0.1998 | 1.723 |
| 328.20 | 0.2491 | 1.956 |
| 328.20 | 0.2986 | 2.153 |
| 328.20 | 0.3478 | 2.308 |
| 328.20 | 0.4003 | 2.392 |
| 328.20 | 0.4482 | 2.451 |
| 328.20 | 0.4990 | 2.471 |
| 328.20 | 0.5484 | 2.452 |
| 328.20 | 0.6007 | 2.363 |
| 328.20 | 0.6509 | 2.246 |
| 328.20 | 0.6986 | 2.108 |
| 328.20 | 0.7487 | 1.89 |
| 328.20 | 0.8015 | 1.612 |
| 328.20 | 0.8509 | 1.302 |
| 328.20 | 0.9028 | 0.9090 |
| 328.20 | 0.9503 | 0.4530 |
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 | 0.0505 | 0.4450 |
| 288.20 | 0.1001 | 0.7810 |
| 288.20 | 0.1509 | 1.056 |
| 288.20 | 0.1998 | 1.269 |
| 288.20 | 0.2491 | 1.429 |
| 288.20 | 0.2986 | 1.571 |
| 288.20 | 0.3478 | 1.672 |
| 288.20 | 0.4003 | 1.754 |
| 288.20 | 0.4482 | 1.8 |
| 288.20 | 0.4990 | 1.839 |
| 288.20 | 0.5484 | 1.829 |
| 288.20 | 0.6007 | 1.8 |
| 288.20 | 0.6509 | 1.736 |
| 288.20 | 0.6986 | 1.642 |
| 288.20 | 0.7487 | 1.51 |
| 288.20 | 0.8015 | 1.325 |
| 288.20 | 0.8509 | 1.101 |
| 288.20 | 0.9028 | 0.8040 |
| 288.20 | 0.9503 | 0.4240 |
| 298.20 | 0.0505 | 0.4710 |
| 298.20 | 0.1001 | 0.8450 |
| 298.20 | 0.1509 | 1.154 |
| 298.20 | 0.1998 | 1.387 |
| 298.20 | 0.2491 | 1.588 |
| 298.20 | 0.2986 | 1.723 |
| 298.20 | 0.3478 | 1.858 |
| 298.20 | 0.4003 | 1.948 |
| 298.20 | 0.4482 | 1.987 |
| 298.20 | 0.4990 | 2.025 |
| 298.20 | 0.5484 | 2.009 |
| 298.20 | 0.6007 | 1.98 |
| 298.20 | 0.6509 | 1.894 |
| 298.20 | 0.6986 | 1.777 |
| 298.20 | 0.7487 | 1.622 |
| 298.20 | 0.8015 | 1.424 |
| 298.20 | 0.8509 | 1.177 |
| 298.20 | 0.9028 | 0.8220 |
| 298.20 | 0.9503 | 0.4500 |
| 313.20 | 0.0505 | 0.5140 |
| 313.20 | 0.1001 | 0.9710 |
| 313.20 | 0.1509 | 1.319 |
| 313.20 | 0.1998 | 1.58 |
| 313.20 | 0.2491 | 1.811 |
| 313.20 | 0.2986 | 1.965 |
| 313.20 | 0.3478 | 2.11 |
| 313.20 | 0.4003 | 2.211 |
| 313.20 | 0.4482 | 2.252 |
| 313.20 | 0.4990 | 2.279 |
| 313.20 | 0.5484 | 2.256 |
| 313.20 | 0.6007 | 2.196 |
| 313.20 | 0.6509 | 2.109 |
| 313.20 | 0.6986 | 1.97 |
| 313.20 | 0.7487 | 1.797 |
| 313.20 | 0.8015 | 1.536 |
| 313.20 | 0.8509 | 1.25 |
| 313.20 | 0.9028 | 0.8790 |
| 313.20 | 0.9503 | 0.4540 |
| 328.20 | 0.0505 | 0.5630 |
| 328.20 | 0.1001 | 1.041 |
| 328.20 | 0.1509 | 1.429 |
| 328.20 | 0.1998 | 1.723 |
| 328.20 | 0.2491 | 1.956 |
| 328.20 | 0.2986 | 2.153 |
| 328.20 | 0.3478 | 2.308 |
| 328.20 | 0.4003 | 2.392 |
| 328.20 | 0.4482 | 2.451 |
| 328.20 | 0.4990 | 2.471 |
| 328.20 | 0.5484 | 2.452 |
| 328.20 | 0.6007 | 2.363 |
| 328.20 | 0.6509 | 2.246 |
| 328.20 | 0.6986 | 2.108 |
| 328.20 | 0.7487 | 1.89 |
| 328.20 | 0.8015 | 1.612 |
| 328.20 | 0.8509 | 1.302 |
| 328.20 | 0.9028 | 0.9090 |
| 328.20 | 0.9503 | 0.4530 |