- 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
- Ethanol, 2-(2-propoxyethoxy)-
- InChI
- InChI=1S/C7H16O3/c1-2-4-9-6-7-10-5-3-8/h8H,2-7H2,1H3
- InChI Key
- DJCYDDALXPHSHR-UHFFFAOYSA-N
- Formula
- C7H16O3
- SMILES
- CCCOCCOCCO
- Mol. Weight (g/mol)
- 148.20
- CAS
- 6881-94-3
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Datasets
- Excess molar enthalpy (molar enthalpy (2)
- ρl - Mass density, kg/m3 (2)
- Excess molar volume, m3/mol (2)
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 |
|---|---|
| 0.0600 | -0.1469 |
| 0.1190 | -0.2506 |
| 0.1470 | -0.2966 |
| 0.2020 | -0.3743 |
| 0.2550 | -0.4290 |
| 0.3060 | -0.4673 |
| 0.3550 | -0.4855 |
| 0.4020 | -0.4906 |
| 0.4470 | -0.4823 |
| 0.5110 | -0.4492 |
| 0.5520 | -0.4136 |
| 0.5920 | -0.3755 |
| 0.6480 | -0.3082 |
| 0.7020 | -0.2346 |
| 0.7530 | -0.1621 |
| 0.8020 | -0.0941 |
| 0.8480 | -0.0302 |
| 0.9070 | 0.0260 |
| 0.9480 | 0.0378 |
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 |
|---|---|
| 0.0600 | -0.1469 |
| 0.1190 | -0.2506 |
| 0.1470 | -0.2966 |
| 0.2020 | -0.3743 |
| 0.2550 | -0.4290 |
| 0.3060 | -0.4673 |
| 0.3550 | -0.4855 |
| 0.4020 | -0.4906 |
| 0.4470 | -0.4823 |
| 0.5110 | -0.4492 |
| 0.5520 | -0.4136 |
| 0.5920 | -0.3755 |
| 0.6480 | -0.3082 |
| 0.7020 | -0.2346 |
| 0.7530 | -0.1621 |
| 0.8020 | -0.0941 |
| 0.8480 | -0.0302 |
| 0.9070 | 0.0260 |
| 0.9480 | 0.0378 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Propane, 1,2-dichloro- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0540 | 969.58 |
| 0.1050 | 976.29 |
| 0.1473 | 982.03 |
| 0.2030 | 989.81 |
| 0.2494 | 996.53 |
| 0.3000 | 1004.1 |
| 0.3488 | 1011.66 |
| 0.4014 | 1020.11 |
| 0.4516 | 1028.46 |
| 0.5005 | 1036.91 |
| 0.5504 | 1045.89 |
| 0.5995 | 1055.07 |
| 0.6509 | 1065.09 |
| 0.7009 | 1075.28 |
| 0.7520 | 1086.18 |
| 0.8015 | 1097.29 |
| 0.8510 | 1109.05 |
| 0.9018 | 1121.84 |
| 0.9476 | 1134.08 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Propane, 1,2-dichloro- (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0540 | 969.58 |
| 0.1050 | 976.29 |
| 0.1473 | 982.03 |
| 0.2030 | 989.81 |
| 0.2494 | 996.53 |
| 0.3000 | 1004.1 |
| 0.3488 | 1011.66 |
| 0.4014 | 1020.11 |
| 0.4516 | 1028.46 |
| 0.5005 | 1036.91 |
| 0.5504 | 1045.89 |
| 0.5995 | 1055.07 |
| 0.6509 | 1065.09 |
| 0.7009 | 1075.28 |
| 0.7520 | 1086.18 |
| 0.8015 | 1097.29 |
| 0.8510 | 1109.05 |
| 0.9018 | 1121.84 |
| 0.9476 | 1134.08 |
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 |
|---|---|
| 0.0540 | -4.5000e-08 |
| 0.1050 | -8.5200e-08 |
| 0.1473 | -1.1560e-07 |
| 0.2030 | -1.4490e-07 |
| 0.2494 | -1.6400e-07 |
| 0.3000 | -1.8080e-07 |
| 0.3488 | -1.9040e-07 |
| 0.4014 | -1.9390e-07 |
| 0.4516 | -1.8890e-07 |
| 0.5005 | -1.7850e-07 |
| 0.5504 | -1.6420e-07 |
| 0.5995 | -1.4510e-07 |
| 0.6509 | -1.1890e-07 |
| 0.7009 | -9.1600e-08 |
| 0.7520 | -6.0800e-08 |
| 0.8015 | -3.1600e-08 |
| 0.8510 | -0.0000 |
| 0.9018 | 0.0000 |
| 0.9476 | 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 |
|---|---|
| 0.0540 | -4.5000e-08 |
| 0.1050 | -8.5200e-08 |
| 0.1473 | -1.1560e-07 |
| 0.2030 | -1.4490e-07 |
| 0.2494 | -1.6400e-07 |
| 0.3000 | -1.8080e-07 |
| 0.3488 | -1.9040e-07 |
| 0.4014 | -1.9390e-07 |
| 0.4516 | -1.8890e-07 |
| 0.5005 | -1.7850e-07 |
| 0.5504 | -1.6420e-07 |
| 0.5995 | -1.4510e-07 |
| 0.6509 | -1.1890e-07 |
| 0.7009 | -9.1600e-08 |
| 0.7520 | -6.0800e-08 |
| 0.8015 | -3.1600e-08 |
| 0.8510 | -0.0000 |
| 0.9018 | 0.0000 |
| 0.9476 | 0.0000 |