- Name
- 2-Ethoxyethyl acetate
- InChI
- InChI=1S/C6H12O3/c1-3-8-4-5-9-6(2)7/h3-5H2,1-2H3
- InChI Key
- SVONRAPFKPVNKG-UHFFFAOYSA-N
- Formula
- C6H12O3
- SMILES
- CCOCCOC(C)=O
- Mol. Weight (g/mol)
- 132.16
- CAS
- 111-15-9
- Name
- Propane, 1,2-dichloro-
- InChI
- InChI=1S/C3H6Cl2/c1-3(5)2-4/h3H,2H2,1H3
- InChI Key
- KNKRKFALVUDBJE-UHFFFAOYSA-N
- Formula
- C3H6Cl2
- SMILES
- CC(Cl)CCl
- Mol. Weight (g/mol)
- 112.99
- CAS
- 78-87-5
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Datasets
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Propane, 1,2-dichloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0532 | -0.0732 |
| 0.1067 | -0.1266 |
| 0.1585 | -0.1993 |
| 0.2088 | -0.2485 |
| 0.2575 | -0.2899 |
| 0.3049 | -0.3232 |
| 0.3510 | -0.3520 |
| 0.3957 | -0.3738 |
| 0.4605 | -0.3964 |
| 0.5022 | -0.4031 |
| 0.5428 | -0.4049 |
| 0.6017 | -0.3985 |
| 0.6583 | -0.3875 |
| 0.6949 | -0.3677 |
| 0.7480 | -0.3324 |
| 0.7991 | -0.2877 |
| 0.8485 | -0.2364 |
| 0.8960 | -0.1754 |
| 0.9569 | -0.0829 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Propane, 1,2-dichloro- (2) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0532 | -0.0732 |
| 0.1067 | -0.1266 |
| 0.1585 | -0.1993 |
| 0.2088 | -0.2485 |
| 0.2575 | -0.2899 |
| 0.3049 | -0.3232 |
| 0.3510 | -0.3520 |
| 0.3957 | -0.3738 |
| 0.4605 | -0.3964 |
| 0.5022 | -0.4031 |
| 0.5428 | -0.4049 |
| 0.6017 | -0.3985 |
| 0.6583 | -0.3875 |
| 0.6949 | -0.3677 |
| 0.7480 | -0.3324 |
| 0.7991 | -0.2877 |
| 0.8485 | -0.2364 |
| 0.8960 | -0.1754 |
| 0.9569 | -0.0829 |
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Propane, 1,2-dichloro- (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0446 | -0.0000 |
| 0.0924 | -0.0000 |
| 0.1427 | -0.0000 |
| 0.2032 | -0.0000 |
| 0.2473 | 0.0000 |
| 0.2970 | 0.0000 |
| 0.3504 | 0.0000 |
| 0.3974 | 0.0000 |
| 0.4454 | 0.0000 |
| 0.4983 | 1.0900e-08 |
| 0.5465 | 1.1600e-08 |
| 0.5984 | 1.1300e-08 |
| 0.6432 | 1.0700e-08 |
| 0.6978 | 0.0000 |
| 0.7475 | 0.0000 |
| 0.7943 | 0.0000 |
| 0.8505 | 0.0000 |
| 0.8997 | 0.0000 |
| 0.9491 | 0.0000 |
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Propane, 1,2-dichloro- (2) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0446 | -0.0000 |
| 0.0924 | -0.0000 |
| 0.1427 | -0.0000 |
| 0.2032 | -0.0000 |
| 0.2473 | 0.0000 |
| 0.2970 | 0.0000 |
| 0.3504 | 0.0000 |
| 0.3974 | 0.0000 |
| 0.4454 | 0.0000 |
| 0.4983 | 1.0900e-08 |
| 0.5465 | 1.1600e-08 |
| 0.5984 | 1.1300e-08 |
| 0.6432 | 1.0700e-08 |
| 0.6978 | 0.0000 |
| 0.7475 | 0.0000 |
| 0.7943 | 0.0000 |
| 0.8505 | 0.0000 |
| 0.8997 | 0.0000 |
| 0.9491 | 0.0000 |