- 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
- Name
- 2-Butoxyethyl acetate
- InChI
- InChI=1S/C8H16O3/c1-3-4-5-10-6-7-11-8(2)9/h3-7H2,1-2H3
- InChI Key
- NQBXSWAWVZHKBZ-UHFFFAOYSA-N
- Formula
- C8H16O3
- SMILES
- CCCCOCCOC(C)=O
- Mol. Weight (g/mol)
- 160.21
- CAS
- 112-07-2
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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- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0659 | -0.0943 |
| 0.0985 | -0.1249 |
| 0.1611 | -0.2086 |
| 0.1911 | -0.2281 |
| 0.2486 | -0.2863 |
| 0.3032 | -0.3307 |
| 0.3549 | -0.3678 |
| 0.4041 | -0.3956 |
| 0.4509 | -0.4090 |
| 0.4955 | -0.4200 |
| 0.5585 | -0.4281 |
| 0.5982 | -0.4247 |
| 0.6545 | -0.4091 |
| 0.7073 | -0.3824 |
| 0.7568 | -0.3476 |
| 0.8035 | -0.3043 |
| 0.8615 | -0.2380 |
| 0.9022 | -0.1805 |
| 0.9531 | -0.0944 |
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- (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
|---|---|
| 0.0659 | -0.0943 |
| 0.0985 | -0.1249 |
| 0.1611 | -0.2086 |
| 0.1911 | -0.2281 |
| 0.2486 | -0.2863 |
| 0.3032 | -0.3307 |
| 0.3549 | -0.3678 |
| 0.4041 | -0.3956 |
| 0.4509 | -0.4090 |
| 0.4955 | -0.4200 |
| 0.5585 | -0.4281 |
| 0.5982 | -0.4247 |
| 0.6545 | -0.4091 |
| 0.7073 | -0.3824 |
| 0.7568 | -0.3476 |
| 0.8035 | -0.3043 |
| 0.8615 | -0.2380 |
| 0.9022 | -0.1805 |
| 0.9531 | -0.0944 |
Excess molar volume, m3/mol [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Propane, 1,2-dichloro- (1) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0537 | -0.0000 |
| 0.1015 | -1.0500e-08 |
| 0.1496 | -1.4400e-08 |
| 0.1999 | -1.8800e-08 |
| 0.2481 | -2.2800e-08 |
| 0.2970 | -2.6100e-08 |
| 0.3458 | -2.8600e-08 |
| 0.3982 | -3.0800e-08 |
| 0.4486 | -3.1500e-08 |
| 0.5023 | -3.1600e-08 |
| 0.5502 | -3.0300e-08 |
| 0.6023 | -2.8100e-08 |
| 0.6516 | -2.6100e-08 |
| 0.7002 | -2.3800e-08 |
| 0.7495 | -1.8800e-08 |
| 0.8005 | -1.4900e-08 |
| 0.8585 | -1.0700e-08 |
| 0.8989 | -0.0000 |
| 0.9505 | -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- (1) - Liquid | Excess molar volume, m3/mol - Liquid |
|---|---|
| 0.0537 | -0.0000 |
| 0.1015 | -1.0500e-08 |
| 0.1496 | -1.4400e-08 |
| 0.1999 | -1.8800e-08 |
| 0.2481 | -2.2800e-08 |
| 0.2970 | -2.6100e-08 |
| 0.3458 | -2.8600e-08 |
| 0.3982 | -3.0800e-08 |
| 0.4486 | -3.1500e-08 |
| 0.5023 | -3.1600e-08 |
| 0.5502 | -3.0300e-08 |
| 0.6023 | -2.8100e-08 |
| 0.6516 | -2.6100e-08 |
| 0.7002 | -2.3800e-08 |
| 0.7495 | -1.8800e-08 |
| 0.8005 | -1.4900e-08 |
| 0.8585 | -1.0700e-08 |
| 0.8989 | -0.0000 |
| 0.9505 | -0.0000 |