- 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
- Isopropyl Alcohol
- InChI
- InChI=1S/C3H8O/c1-3(2)4/h3-4H,1-2H3
- InChI Key
- KFZMGEQAYNKOFK-UHFFFAOYSA-N
- Formula
- C3H8O
- SMILES
- CC(C)O
- Mol. Weight (g/mol)
- 60.09
- CAS
- 67-63-0
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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 | 0.0492 | 0.5190 |
| 288.20 | 0.0997 | 0.9430 |
| 288.20 | 0.1514 | 1.265 |
| 288.20 | 0.2009 | 1.492 |
| 288.20 | 0.2507 | 1.712 |
| 288.20 | 0.3005 | 1.832 |
| 288.20 | 0.3499 | 1.959 |
| 288.20 | 0.3987 | 2.024 |
| 288.20 | 0.4504 | 2.076 |
| 288.20 | 0.5010 | 2.082 |
| 288.20 | 0.5500 | 2.09 |
| 288.20 | 0.6018 | 2.04 |
| 288.20 | 0.6515 | 1.965 |
| 288.20 | 0.6985 | 1.849 |
| 288.20 | 0.7478 | 1.693 |
| 288.20 | 0.7996 | 1.481 |
| 288.20 | 0.8479 | 1.228 |
| 288.20 | 0.8985 | 0.9080 |
| 288.20 | 0.9515 | 0.4930 |
| 298.20 | 0.0492 | 0.5480 |
| 298.20 | 0.0997 | 1.035 |
| 298.20 | 0.1514 | 1.389 |
| 298.20 | 0.2009 | 1.647 |
| 298.20 | 0.2507 | 1.9 |
| 298.20 | 0.3005 | 2.03 |
| 298.20 | 0.3499 | 2.163 |
| 298.20 | 0.3987 | 2.236 |
| 298.20 | 0.4504 | 2.285 |
| 298.20 | 0.5010 | 2.279 |
| 298.20 | 0.5500 | 2.277 |
| 298.20 | 0.6018 | 2.211 |
| 298.20 | 0.6515 | 2.122 |
| 298.20 | 0.6985 | 1.993 |
| 298.20 | 0.7478 | 1.807 |
| 298.20 | 0.7996 | 1.574 |
| 298.20 | 0.8479 | 1.287 |
| 298.20 | 0.8985 | 0.9320 |
| 298.20 | 0.9515 | 0.4680 |
| 313.20 | 0.0492 | 0.5850 |
| 313.20 | 0.0997 | 1.124 |
| 313.20 | 0.1514 | 1.526 |
| 313.20 | 0.2009 | 1.831 |
| 313.20 | 0.2507 | 2.094 |
| 313.20 | 0.3005 | 2.257 |
| 313.20 | 0.3499 | 2.392 |
| 313.20 | 0.3987 | 2.467 |
| 313.20 | 0.4504 | 2.532 |
| 313.20 | 0.5010 | 2.524 |
| 313.20 | 0.5500 | 2.486 |
| 313.20 | 0.6018 | 2.415 |
| 313.20 | 0.6515 | 2.295 |
| 313.20 | 0.6985 | 2.152 |
| 313.20 | 0.7478 | 1.955 |
| 313.20 | 0.7996 | 1.667 |
| 313.20 | 0.8479 | 1.372 |
| 313.20 | 0.8985 | 0.9950 |
| 313.20 | 0.9515 | 0.4790 |
| 328.20 | 0.0492 | 0.6050 |
| 328.20 | 0.0997 | 1.202 |
| 328.20 | 0.1514 | 1.633 |
| 328.20 | 0.2009 | 1.949 |
| 328.20 | 0.2507 | 2.246 |
| 328.20 | 0.3005 | 2.402 |
| 328.20 | 0.3499 | 2.549 |
| 328.20 | 0.3987 | 2.657 |
| 328.20 | 0.4504 | 2.685 |
| 328.20 | 0.5010 | 2.68 |
| 328.20 | 0.5500 | 2.643 |
| 328.20 | 0.6018 | 2.563 |
| 328.20 | 0.6515 | 2.416 |
| 328.20 | 0.6985 | 2.253 |
| 328.20 | 0.7478 | 2.028 |
| 328.20 | 0.7996 | 1.743 |
| 328.20 | 0.8479 | 1.404 |
| 328.20 | 0.8985 | 0.9820 |
| 328.20 | 0.9515 | 0.5050 |
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 | 0.0492 | 0.5190 |
| 288.20 | 0.0997 | 0.9430 |
| 288.20 | 0.1514 | 1.265 |
| 288.20 | 0.2009 | 1.492 |
| 288.20 | 0.2507 | 1.712 |
| 288.20 | 0.3005 | 1.832 |
| 288.20 | 0.3499 | 1.959 |
| 288.20 | 0.3987 | 2.024 |
| 288.20 | 0.4504 | 2.076 |
| 288.20 | 0.5010 | 2.082 |
| 288.20 | 0.5500 | 2.09 |
| 288.20 | 0.6018 | 2.04 |
| 288.20 | 0.6515 | 1.965 |
| 288.20 | 0.6985 | 1.849 |
| 288.20 | 0.7478 | 1.693 |
| 288.20 | 0.7996 | 1.481 |
| 288.20 | 0.8479 | 1.228 |
| 288.20 | 0.8985 | 0.9080 |
| 288.20 | 0.9515 | 0.4930 |
| 298.20 | 0.0492 | 0.5480 |
| 298.20 | 0.0997 | 1.035 |
| 298.20 | 0.1514 | 1.389 |
| 298.20 | 0.2009 | 1.647 |
| 298.20 | 0.2507 | 1.9 |
| 298.20 | 0.3005 | 2.03 |
| 298.20 | 0.3499 | 2.163 |
| 298.20 | 0.3987 | 2.236 |
| 298.20 | 0.4504 | 2.285 |
| 298.20 | 0.5010 | 2.279 |
| 298.20 | 0.5500 | 2.277 |
| 298.20 | 0.6018 | 2.211 |
| 298.20 | 0.6515 | 2.122 |
| 298.20 | 0.6985 | 1.993 |
| 298.20 | 0.7478 | 1.807 |
| 298.20 | 0.7996 | 1.574 |
| 298.20 | 0.8479 | 1.287 |
| 298.20 | 0.8985 | 0.9320 |
| 298.20 | 0.9515 | 0.4680 |
| 313.20 | 0.0492 | 0.5850 |
| 313.20 | 0.0997 | 1.124 |
| 313.20 | 0.1514 | 1.526 |
| 313.20 | 0.2009 | 1.831 |
| 313.20 | 0.2507 | 2.094 |
| 313.20 | 0.3005 | 2.257 |
| 313.20 | 0.3499 | 2.392 |
| 313.20 | 0.3987 | 2.467 |
| 313.20 | 0.4504 | 2.532 |
| 313.20 | 0.5010 | 2.524 |
| 313.20 | 0.5500 | 2.486 |
| 313.20 | 0.6018 | 2.415 |
| 313.20 | 0.6515 | 2.295 |
| 313.20 | 0.6985 | 2.152 |
| 313.20 | 0.7478 | 1.955 |
| 313.20 | 0.7996 | 1.667 |
| 313.20 | 0.8479 | 1.372 |
| 313.20 | 0.8985 | 0.9950 |
| 313.20 | 0.9515 | 0.4790 |
| 328.20 | 0.0492 | 0.6050 |
| 328.20 | 0.0997 | 1.202 |
| 328.20 | 0.1514 | 1.633 |
| 328.20 | 0.2009 | 1.949 |
| 328.20 | 0.2507 | 2.246 |
| 328.20 | 0.3005 | 2.402 |
| 328.20 | 0.3499 | 2.549 |
| 328.20 | 0.3987 | 2.657 |
| 328.20 | 0.4504 | 2.685 |
| 328.20 | 0.5010 | 2.68 |
| 328.20 | 0.5500 | 2.643 |
| 328.20 | 0.6018 | 2.563 |
| 328.20 | 0.6515 | 2.416 |
| 328.20 | 0.6985 | 2.253 |
| 328.20 | 0.7478 | 2.028 |
| 328.20 | 0.7996 | 1.743 |
| 328.20 | 0.8479 | 1.404 |
| 328.20 | 0.8985 | 0.9820 |
| 328.20 | 0.9515 | 0.5050 |