Datasets
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Activity coefficient (2)
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Mass fraction (14)
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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)
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Tboil - Boiling temperature at pressure P, K (4)
Activity coefficient of 1-Butanol, 3-methyl- (1)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Butanol, 3-methyl- (1) - Liquid |
| 273.35 |
94.9 |
| 283.15 |
126.0 |
| 293.15 |
148.0 |
| 293.15 |
146.0 |
| 303.15 |
161.0 |
| 303.15 |
164.0 |
| 313.15 |
173.0 |
| 313.15 |
175.0 |
| 323.15 |
179.0 |
| 323.15 |
184.0 |
| 333.15 |
182.0 |
| 333.15 |
178.0 |
| 343.15 |
179.0 |
| 353.15 |
164.0 |
| 371.15 |
149.0 |
Activity coefficient of 1-Butanol, 3-methyl- (1)
[ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 1-Butanol, 3-methyl- (1) - Liquid |
| 273.35 |
94.9 |
| 283.15 |
126.0 |
| 293.15 |
148.0 |
| 293.15 |
146.0 |
| 303.15 |
161.0 |
| 303.15 |
164.0 |
| 313.15 |
173.0 |
| 313.15 |
175.0 |
| 323.15 |
179.0 |
| 323.15 |
184.0 |
| 333.15 |
182.0 |
| 333.15 |
178.0 |
| 343.15 |
179.0 |
| 353.15 |
164.0 |
| 371.15 |
149.0 |
Mass fraction of 1-Butanol, 3-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100.41 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 1-Butanol, 3-methyl- (1) - Liquid mixture 1 |
| 288.20 |
0.9022 |
| 298.20 |
0.9019 |
| 308.20 |
0.8953 |
| 318.20 |
0.8835 |
Mass fraction of 1-Butanol, 3-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100.41 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 1-Butanol, 3-methyl- (1) - Liquid mixture 2 |
| 288.20 |
0.0253 |
| 298.20 |
0.0219 |
| 308.20 |
0.0202 |
| 318.20 |
0.0184 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 293.20 |
0.3283 |
| 293.20 |
0.9941 |
| 313.20 |
0.3461 |
| 313.20 |
0.9950 |
Mole fraction of 1-Butanol, 3-methyl- (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid mixture 1 |
| 101.00 |
293.15 |
0.6620 |
Mole fraction of 1-Butanol, 3-methyl- (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid mixture 2 |
| 293.15 |
101.00 |
0.0060 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 303.15 |
0.2990 |
| 313.15 |
0.3080 |
| 368.06 |
0.4460 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 303.15 |
0.9950 |
| 313.15 |
0.9950 |
| 368.06 |
0.9950 |
Mass fraction of 1-Butanol, 3-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100.41 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 1-Butanol, 3-methyl- (1) - Liquid mixture 1 |
| 288.20 |
0.9022 |
| 298.20 |
0.9019 |
| 308.20 |
0.8953 |
| 318.20 |
0.8835 |
Mass fraction of 1-Butanol, 3-methyl- (1)
[ref]
Operational condition: Pressure, kPa =
100.41 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mass fraction of 1-Butanol, 3-methyl- (1) - Liquid mixture 2 |
| 288.20 |
0.0253 |
| 298.20 |
0.0219 |
| 308.20 |
0.0202 |
| 318.20 |
0.0184 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
95 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 293.20 |
0.3283 |
| 293.20 |
0.9941 |
| 313.20 |
0.3461 |
| 313.20 |
0.9950 |
Mole fraction of 1-Butanol, 3-methyl- (1)
[ref]
| Fixed |
Measured |
| Pressure, kPa - Liquid mixture 1 |
Temperature, K - Liquid mixture 1 |
Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid mixture 1 |
| 101.00 |
293.15 |
0.6620 |
Mole fraction of 1-Butanol, 3-methyl- (1)
[ref]
| Fixed |
Measured |
| Temperature, K - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid mixture 2 |
| 293.15 |
101.00 |
0.0060 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 303.15 |
0.2990 |
| 313.15 |
0.3080 |
| 368.06 |
0.4460 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 303.15 |
0.9950 |
| 313.15 |
0.9950 |
| 368.06 |
0.9950 |
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-Butanol, 3-methyl- (1) - Liquid |
Heat capacity at constant pressure per volume, J/K/m3 - Liquid |
| 0.0005 |
4170700.00 |
| 0.0007 |
4171700.00 |
| 0.0010 |
4173400.00 |
| 0.0010 |
4173600.00 |
| 0.0012 |
4174300.00 |
| 0.0012 |
4174400.00 |
| 0.0014 |
4175200.00 |
| 0.0017 |
4177100.00 |
| 0.0020 |
4178600.00 |
| 0.0021 |
4178800.00 |
| 0.0022 |
4179800.00 |
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-Butanol, 3-methyl- (1) - Liquid |
Heat capacity at constant pressure per volume, J/K/m3 - Liquid |
| 0.0005 |
4170700.00 |
| 0.0007 |
4171700.00 |
| 0.0010 |
4173400.00 |
| 0.0010 |
4173600.00 |
| 0.0012 |
4174300.00 |
| 0.0012 |
4174400.00 |
| 0.0014 |
4175200.00 |
| 0.0017 |
4177100.00 |
| 0.0020 |
4178600.00 |
| 0.0021 |
4178800.00 |
| 0.0022 |
4179800.00 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0005 |
996.67 |
| 0.0007 |
996.51 |
| 0.0010 |
996.29 |
| 0.0010 |
996.22 |
| 0.0012 |
996.13 |
| 0.0012 |
996.13 |
| 0.0014 |
995.99 |
| 0.0017 |
995.68 |
| 0.0020 |
995.47 |
| 0.0021 |
995.45 |
| 0.0022 |
995.36 |
Mass density, kg/m3
[ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of 1-Butanol, 3-methyl- (1) - Liquid |
Mass density, kg/m3 - Liquid |
| 0.0005 |
996.67 |
| 0.0007 |
996.51 |
| 0.0010 |
996.29 |
| 0.0010 |
996.22 |
| 0.0012 |
996.13 |
| 0.0012 |
996.13 |
| 0.0014 |
995.99 |
| 0.0017 |
995.68 |
| 0.0020 |
995.47 |
| 0.0021 |
995.45 |
| 0.0022 |
995.36 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of Water (2) - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Boiling temperature at pressure P, K - Liquid mixture 1 |
| 0.4460 |
101.30 |
368.06 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of Water (2) - Gas |
Pressure, kPa - Liquid mixture 1 |
Boiling temperature at pressure P, K - Liquid mixture 1 |
| 0.8080 |
101.30 |
368.06 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of Water (2) - Liquid mixture 1 |
Pressure, kPa - Liquid mixture 1 |
Boiling temperature at pressure P, K - Liquid mixture 1 |
| 0.4460 |
101.30 |
368.06 |
Boiling temperature at pressure P, K
[ref]
| Fixed |
Measured |
| Mole fraction of Water (2) - Gas |
Pressure, kPa - Liquid mixture 1 |
Boiling temperature at pressure P, K - Liquid mixture 1 |
| 0.8080 |
101.30 |
368.06 |
Sources
-
Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
-
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
-
Study of the LLE, VLE, and VLLE of the Ternary System Water + 1-Butanol + Isoamyl Alcohol at 101.3 kPa
-
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
-
Liquid Liquid Equilibria of the Ternary Systems 3-Methyl-1-butanol + Ethanol + Water and 2-Methyl-1-propanol + Ethanol + Water at 293.15 K
-
Temperature Dependence of Limiting Activity Coefficients, Henry s Law Constants, and Related Infinite Dilution Properties of Branched Pentanols in Water. Measurement, Critical Compilation, Correlation, and Recommended Data
Note: These property values are available through the Cheméo API. A free account gives you an access key.
