- Name
- Butane, 2-methoxy-2-methyl-
- InChI
- InChI=1S/C6H14O/c1-5-6(2,3)7-4/h5H2,1-4H3
- InChI Key
- HVZJRWJGKQPSFL-UHFFFAOYSA-N
- Formula
- C6H14O
- SMILES
- CCC(C)(C)OC
- Mol. Weight (g/mol)
- 102.17
- CAS
- 994-05-8
- Name
- Water
- InChI
- InChI=1S/H2O/h1H2
- InChI Key
- XLYOFNOQVPJJNP-UHFFFAOYSA-N
- Formula
- H2O
- SMILES
- O
- Mol. Weight (g/mol)
- 18.02
- CAS
- 7732-18-5
Datasets
- Activity coefficient (4)
- Mass fraction (8)
- Interfacial tension, N/m (2)
- ρl - Mass density, kg/m3 (4)
Activity coefficient of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational conditions:
- Mole fraction = 0 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Butane, 2-methoxy-2-methyl- (1) - Liquid |
|---|---|
| 288.15 | 390.0 |
| 298.15 | 529.0 |
| 308.15 | 725.0 |
| 318.15 | 1074.0 |
Activity coefficient of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Butane, 2-methoxy-2-methyl- (1) - Liquid |
|---|---|
| 303.25 | 643.0 |
| 313.25 | 796.0 |
| 323.25 | 942.0 |
| 333.25 | 1080.0 |
Activity coefficient of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational conditions:
- Mole fraction = 0 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Butane, 2-methoxy-2-methyl- (1) - Liquid |
|---|---|
| 288.15 | 390.0 |
| 298.15 | 529.0 |
| 308.15 | 725.0 |
| 318.15 | 1074.0 |
Activity coefficient of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Butane, 2-methoxy-2-methyl- (1) - Liquid |
|---|---|
| 303.25 | 643.0 |
| 313.25 | 796.0 |
| 323.25 | 942.0 |
| 333.25 | 1080.0 |
Mass fraction of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass fraction of Butane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
|---|---|
| 298.20 | 0.9910 |
| 298.20 | 0.9920 |
| 321.70 | 0.9890 |
| 341.10 | 0.9880 |
| 322.40 | 0.9900 |
| 342.20 | 0.9890 |
Mass fraction of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass fraction of Butane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
|---|---|
| 298.20 | 0.0100 |
| 298.20 | 0.0110 |
| 321.70 | 0.0060 |
| 341.10 | 0.0050 |
| 322.40 | 0.0060 |
| 342.20 | 0.0050 |
Mole fraction of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mole fraction of Butane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
|---|---|
| 288.15 | 0.0014 |
| 293.15 | 0.0013 |
| 298.15 | 0.0016 |
| 303.15 | 0.0021 |
| 308.15 | 0.0024 |
| 313.15 | 0.0060 |
Mole fraction of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Butane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
|---|---|
| 288.15 | 0.9833 |
| 293.15 | 0.9706 |
| 298.15 | 0.9573 |
| 303.15 | 0.9306 |
| 308.15 | 0.9144 |
| 313.15 | 0.8884 |
Mass fraction of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass fraction of Butane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
|---|---|
| 298.20 | 0.9910 |
| 298.20 | 0.9920 |
| 321.70 | 0.9890 |
| 341.10 | 0.9880 |
| 322.40 | 0.9900 |
| 342.20 | 0.9890 |
Mass fraction of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass fraction of Butane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
|---|---|
| 298.20 | 0.0100 |
| 298.20 | 0.0110 |
| 321.70 | 0.0060 |
| 341.10 | 0.0050 |
| 322.40 | 0.0060 |
| 342.20 | 0.0050 |
Mole fraction of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 2 | Mole fraction of Butane, 2-methoxy-2-methyl- (1) - Liquid mixture 2 |
|---|---|
| 288.15 | 0.0014 |
| 293.15 | 0.0013 |
| 298.15 | 0.0016 |
| 303.15 | 0.0021 |
| 308.15 | 0.0024 |
| 313.15 | 0.0060 |
Mole fraction of Butane, 2-methoxy-2-methyl- (1) [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mole fraction of Butane, 2-methoxy-2-methyl- (1) - Liquid mixture 1 |
|---|---|
| 288.15 | 0.9833 |
| 293.15 | 0.9706 |
| 298.15 | 0.9573 |
| 303.15 | 0.9306 |
| 308.15 | 0.9144 |
| 313.15 | 0.8884 |
Interfacial tension, N/m [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Interfacial tension, N/m - Liquid mixture 1 |
|---|---|
| 278.15 | 0.0122 |
| 288.15 | 0.0132 |
| 298.15 | 0.0145 |
| 308.15 | 0.0155 |
| 318.15 | 0.0163 |
| 328.15 | 0.0170 |
| 338.15 | 0.0175 |
Interfacial tension, N/m [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Interfacial tension, N/m - Liquid mixture 1 |
|---|---|
| 278.15 | 0.0122 |
| 288.15 | 0.0132 |
| 298.15 | 0.0145 |
| 308.15 | 0.0155 |
| 318.15 | 0.0163 |
| 328.15 | 0.0170 |
| 338.15 | 0.0175 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass density, kg/m3 - Liquid mixture 1 |
|---|---|
| 278.15 | 997.06 |
| 288.15 | 996.93 |
| 298.15 | 995.49 |
| 308.15 | 992.83 |
| 318.15 | 989.28 |
| 328.15 | 985.19 |
| 338.15 | 979.14 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mass density, kg/m3 - Liquid mixture 2 |
|---|---|
| 278.15 | 786.3 |
| 288.15 | 777.01 |
| 298.15 | 767.6 |
| 308.15 | 758.19 |
| 318.15 | 748.67 |
| 328.15 | 739.12 |
| 338.15 | 729.32 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 | Mass density, kg/m3 - Liquid mixture 1 |
|---|---|
| 278.15 | 997.06 |
| 288.15 | 996.93 |
| 298.15 | 995.49 |
| 308.15 | 992.83 |
| 318.15 | 989.28 |
| 328.15 | 985.19 |
| 338.15 | 979.14 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 | Mass density, kg/m3 - Liquid mixture 2 |
|---|---|
| 278.15 | 786.3 |
| 288.15 | 777.01 |
| 298.15 | 767.6 |
| 308.15 | 758.19 |
| 318.15 | 748.67 |
| 328.15 | 739.12 |
| 338.15 | 729.32 |
Sources
- Infinite dilution activity coefficient measurements by inert gas stripping method
- Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
- Quaternary, Ternary and Binary LLE Measurements for 2-Methoxy-2-methylbutane + Furfural + Acetic Acid + Water at Temperatures between 298 and 341 K
- Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
- Binary Liquid-Liquid Equilibrium (LLE) for Methyl tert-Amyl Ether (TAME) + Water from (288.15 to 313.15) K and Ternary LLE for Systems of TAME + C1-C4 Alcohols + Water at 298.15 K