Datasets
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Activity coefficient (6)
-
Mass fraction (18)
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Cp/V - Heat capacity at constant pressure per volume, J/K/m3 (2)
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ρl - Mass density, kg/m3 (2)
Activity coefficient of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Propanol, 2-methyl- (1) - Liquid |
| 363.15 |
54.3 |
| 371.15 |
52.2 |
Activity coefficient of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Propanol, 2-methyl- (1) - Liquid |
| 273.35 |
31.6 |
| 283.15 |
36.8 |
| 298.15 |
47.4 |
Activity coefficient of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Propanol, 2-methyl- (1) - Liquid |
| 293.15 |
44.3 |
| 303.15 |
50.3 |
| 313.15 |
54.1 |
| 323.15 |
57.6 |
| 333.15 |
58.3 |
Activity coefficient of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Propanol, 2-methyl- (1) - Liquid |
| 363.15 |
54.3 |
| 371.15 |
52.2 |
Activity coefficient of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Propanol, 2-methyl- (1) - Liquid |
| 273.35 |
31.6 |
| 283.15 |
36.8 |
| 298.15 |
47.4 |
Activity coefficient of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Propanol, 2-methyl- (1) - Liquid |
| 293.15 |
44.3 |
| 303.15 |
50.3 |
| 313.15 |
54.1 |
| 323.15 |
57.6 |
| 333.15 |
58.3 |
Mass fraction of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100.41 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 1 |
| 288.20 |
0.8413 |
| 298.20 |
0.8278 |
| 308.20 |
0.8209 |
| 318.20 |
0.8133 |
Mass fraction of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100.41 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 2 |
| 288.20 |
0.0829 |
| 298.20 |
0.0786 |
| 308.20 |
0.0691 |
| 318.20 |
0.0683 |
Mass fraction of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
97 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 1 |
| 313.15 |
0.8176 |
| 323.15 |
0.8041 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 303.20 |
0.4500 |
| 323.20 |
0.4880 |
| 343.20 |
0.5420 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 303.20 |
0.9760 |
| 323.20 |
0.9760 |
| 343.20 |
0.9810 |
Mole fraction of 1-Propanol, 2-methyl- (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 2 |
| 293.15 |
101.00 |
0.0220 |
Mole fraction of 1-Propanol, 2-methyl- (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 1 |
| 101.00 |
293.15 |
0.5170 |
Mole fraction of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 2 |
| 303.15 |
0.0211 |
| 313.15 |
0.0242 |
Mole fraction of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 1 |
| 303.15 |
0.5410 |
| 313.15 |
0.5280 |
Mass fraction of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100.41 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 1 |
| 288.20 |
0.8413 |
| 298.20 |
0.8278 |
| 308.20 |
0.8209 |
| 318.20 |
0.8133 |
Mass fraction of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100.41 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 2 |
| 288.20 |
0.0829 |
| 298.20 |
0.0786 |
| 308.20 |
0.0691 |
| 318.20 |
0.0683 |
Mass fraction of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
97 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 1 |
| 313.15 |
0.8176 |
| 323.15 |
0.8041 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 303.20 |
0.4500 |
| 323.20 |
0.4880 |
| 343.20 |
0.5420 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 303.20 |
0.9760 |
| 323.20 |
0.9760 |
| 343.20 |
0.9810 |
Mole fraction of 1-Propanol, 2-methyl- (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 2 |
| 293.15 |
101.00 |
0.0220 |
Mole fraction of 1-Propanol, 2-methyl- (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 1 |
| 101.00 |
293.15 |
0.5170 |
Mole fraction of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 2 |
| 303.15 |
0.0211 |
| 313.15 |
0.0242 |
Mole fraction of 1-Propanol, 2-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid mixture 1 |
| 303.15 |
0.5410 |
| 313.15 |
0.5280 |
Heat capacity at constant pressure per volume, J/K/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid |
Heat capacity at constant pressure per volume, J/K/m3 - Liquid |
| 0.0016 |
4175200.00 |
| 0.0018 |
4176000.00 |
| 0.0036 |
4184200.00 |
| 0.0060 |
4195700.00 |
| 0.0091 |
4209900.00 |
| 0.0114 |
4220800.00 |
| 0.0165 |
4247000.00 |
Heat capacity at constant pressure per volume, J/K/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid |
Heat capacity at constant pressure per volume, J/K/m3 - Liquid |
| 0.0016 |
4175200.00 |
| 0.0018 |
4176000.00 |
| 0.0036 |
4184200.00 |
| 0.0060 |
4195700.00 |
| 0.0091 |
4209900.00 |
| 0.0114 |
4220800.00 |
| 0.0165 |
4247000.00 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0016 |
995.99 |
| 0.0018 |
995.84 |
| 0.0036 |
994.66 |
| 0.0060 |
993.15 |
| 0.0091 |
991.35 |
| 0.0114 |
989.99 |
| 0.0165 |
987.23 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Propanol, 2-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0016 |
995.99 |
| 0.0018 |
995.84 |
| 0.0036 |
994.66 |
| 0.0060 |
993.15 |
| 0.0091 |
991.35 |
| 0.0114 |
989.99 |
| 0.0165 |
987.23 |
Sources
-
Measurement and thermodynamic modelling of ternary liquid-liquid equilibrium for extraction of (1R,2R)-(-)-1,2-Diaminocyclohexane from aqueous solution with C4-C5 alcohols at different temperatures
-
Determination of Ternary Liquid Liquid Equilibria for Dimethyl Carbonate + 2-Methyl-1-propanol or 2-Methyl-2-propanol + Water Systems at T = 303.15 and 313.15 K
-
Design of a Salt-Free Aqueous Two-Phase System Containing Butanol, n-Butylpyridine Dicyanamide, and Water: Equilibrium Data and Correlation
-
Partial Molar Heat Capacities and Partial Molar Volumes of All of the Isomeric (C3 to C5) Alkanols at Infinite Dilution in Water at 298.15 K
-
Ternary Liquid Liquid Equilibrium Data for the Water + Acetonitrile + {Butan-1-ol or 2-Methylpropan-1-ol} Systems at (303.2, 323.2, 343.2) K and 1 atm
-
Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched (C3 and C4) Alkanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
-
Liquid Liquid Equilibria of the Ternary Systems 3-Methyl-1-butanol + Ethanol + Water and 2-Methyl-1-propanol + Ethanol + Water at 293.15 K
Note: These property values are available through the Cheméo API. A free account gives you an access key.
