Datasets
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Activity coefficient (4)
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Henry's Law constant (mole fraction scale), kPa (22)
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γ - Surface tension liquid-gas, N/m (2)
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Vapor or sublimation pressure, kPa (6)
Activity coefficient of 2-Butanone (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 2-Butanone (1) - Liquid |
| 297.85 |
25.8 |
| 298.15 |
26.1 |
Activity coefficient of 2-Butanone (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 2-Butanone (1) - Liquid |
| 303.25 |
29.5 |
| 313.25 |
33.8 |
| 323.25 |
35.9 |
| 333.25 |
38.9 |
Activity coefficient of 2-Butanone (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 2-Butanone (1) - Liquid |
| 297.85 |
25.8 |
| 298.15 |
26.1 |
Activity coefficient of 2-Butanone (1)
[ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid |
Activity coefficient of 2-Butanone (1) - Liquid |
| 303.25 |
29.5 |
| 313.25 |
33.8 |
| 323.25 |
35.9 |
| 333.25 |
38.9 |
Henry's Law constant (mole fraction scale), kPa of 2-Butanone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Butanone (1) - Liquid |
| 323.15 |
1175.4 |
| 333.15 |
1803.6 |
| 343.15 |
2745.9 |
| 353.15 |
3850.3 |
Molality, mol/kg of 2-Butanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Molality, mol/kg of 2-Butanone (1) - Liquid mixture 1 |
| 283.15 |
4.811 |
| 288.15 |
4.354 |
| 293.15 |
3.785 |
| 298.15 |
3.12 |
| 303.15 |
2.385 |
Molality, mol/kg of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Molality, mol/kg of Water (2) - Liquid mixture 2 |
| 293.15 |
7.06 |
| 298.15 |
6.83 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.3164 |
| 303.15 |
0.3273 |
| 293.15 |
0.3209 |
| 313.15 |
0.3220 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 298.15 |
0.9226 |
| 303.15 |
0.9312 |
| 293.15 |
0.9115 |
| 313.15 |
0.9352 |
Mole fraction of 2-Butanone (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of 2-Butanone (1) - Liquid mixture 2 |
| 346.73 |
0.0464 |
Mole fraction of 2-Butanone (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of 2-Butanone (1) - Liquid mixture 1 |
| 346.73 |
0.5839 |
Mole fraction of 2-Butanone (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of 2-Butanone (1) - Gas |
| 346.73 |
0.6480 |
Henry's Law constant (amount concentration scale), kPa*dm3/mol of 2-Butanone (1)
[ref]
Operational condition: Amount concentration (molarity), mol/dm3 =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (amount concentration scale), kPa*dm3/mol of 2-Butanone (1) - Liquid |
| 275.00 |
8207.0 |
| 278.00 |
7397.0 |
| 281.00 |
4762.0 |
| 283.00 |
2533.0 |
| 283.00 |
2229.0 |
| 288.00 |
1723.0 |
| 293.00 |
800.5 |
| 293.00 |
658.6 |
| 298.00 |
233.0 |
| 298.00 |
263.4 |
| 298.00 |
293.8 |
Henry's Law constant (mole fraction scale), kPa of 2-Butanone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Butanone (1) - Liquid |
| 297.85 |
322.0 |
| 298.15 |
330.0 |
Henry's Law constant (molality scale), kPa*kg/mol of 2-Butanone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of 2-Butanone (1) - Liquid |
| 274.15 |
0.4156 |
| 294.65 |
1.7242 |
| 294.65 |
2.365 |
| 296.15 |
2.6247 |
| 310.15 |
8.1284 |
| 320.15 |
15.283 |
| 331.15 |
43.902 |
| 333.15 |
61.959 |
Henry's Law constant (mole fraction scale), kPa of 2-Butanone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Butanone (1) - Liquid |
| 323.15 |
1175.4 |
| 333.15 |
1803.6 |
| 343.15 |
2745.9 |
| 353.15 |
3850.3 |
Molality, mol/kg of 2-Butanone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Molality, mol/kg of 2-Butanone (1) - Liquid mixture 1 |
| 283.15 |
4.811 |
| 288.15 |
4.354 |
| 293.15 |
3.785 |
| 298.15 |
3.12 |
| 303.15 |
2.385 |
Molality, mol/kg of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
| Temperature, K - Liquid mixture 1 |
Molality, mol/kg of Water (2) - Liquid mixture 2 |
| 293.15 |
7.06 |
| 298.15 |
6.83 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 1 |
| 298.15 |
0.3164 |
| 303.15 |
0.3273 |
| 293.15 |
0.3209 |
| 313.15 |
0.3220 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
100 (Liquid mixture 2)
| Temperature, K - Liquid mixture 2 |
Mole fraction of Water (2) - Liquid mixture 2 |
| 298.15 |
0.9226 |
| 303.15 |
0.9312 |
| 293.15 |
0.9115 |
| 313.15 |
0.9352 |
Mole fraction of 2-Butanone (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of 2-Butanone (1) - Liquid mixture 2 |
| 346.73 |
0.0464 |
Mole fraction of 2-Butanone (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of 2-Butanone (1) - Liquid mixture 1 |
| 346.73 |
0.5839 |
Mole fraction of 2-Butanone (1)
[ref]
| Temperature, K - Liquid mixture 1 |
Mole fraction of 2-Butanone (1) - Gas |
| 346.73 |
0.6480 |
Henry's Law constant (amount concentration scale), kPa*dm3/mol of 2-Butanone (1)
[ref]
Operational condition: Amount concentration (molarity), mol/dm3 =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (amount concentration scale), kPa*dm3/mol of 2-Butanone (1) - Liquid |
| 275.00 |
8207.0 |
| 278.00 |
7397.0 |
| 281.00 |
4762.0 |
| 283.00 |
2533.0 |
| 283.00 |
2229.0 |
| 288.00 |
1723.0 |
| 293.00 |
800.5 |
| 293.00 |
658.6 |
| 298.00 |
233.0 |
| 298.00 |
263.4 |
| 298.00 |
293.8 |
Henry's Law constant (mole fraction scale), kPa of 2-Butanone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (mole fraction scale), kPa of 2-Butanone (1) - Liquid |
| 297.85 |
322.0 |
| 298.15 |
330.0 |
Henry's Law constant (molality scale), kPa*kg/mol of 2-Butanone (1)
[ref]
Operational condition: Mole fraction =
0 (Liquid)
| Temperature, K - Liquid |
Henry's Law constant (molality scale), kPa*kg/mol of 2-Butanone (1) - Liquid |
| 274.15 |
0.4156 |
| 294.65 |
1.7242 |
| 294.65 |
2.365 |
| 296.15 |
2.6247 |
| 310.15 |
8.1284 |
| 320.15 |
15.283 |
| 331.15 |
43.902 |
| 333.15 |
61.959 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
| Mole fraction of 2-Butanone (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 0.0001 |
0.0718 |
| 0.0001 |
0.0717 |
| 0.0001 |
0.0715 |
| 0.0001 |
0.0713 |
| 0.0003 |
0.0700 |
| 0.0005 |
0.0689 |
| 0.0007 |
0.0678 |
| 0.0009 |
0.0673 |
| 0.0010 |
0.0668 |
| 0.0021 |
0.0631 |
| 0.0040 |
0.0586 |
| 0.0061 |
0.0551 |
| 0.0080 |
0.0527 |
| 0.0102 |
0.0504 |
| 0.0120 |
0.0488 |
| 0.0141 |
0.0474 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
| Mole fraction of 2-Butanone (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
| 0.0001 |
0.0718 |
| 0.0001 |
0.0717 |
| 0.0001 |
0.0715 |
| 0.0001 |
0.0713 |
| 0.0003 |
0.0700 |
| 0.0005 |
0.0689 |
| 0.0007 |
0.0678 |
| 0.0009 |
0.0673 |
| 0.0010 |
0.0668 |
| 0.0021 |
0.0631 |
| 0.0040 |
0.0586 |
| 0.0061 |
0.0551 |
| 0.0080 |
0.0527 |
| 0.0102 |
0.0504 |
| 0.0120 |
0.0488 |
| 0.0141 |
0.0474 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Gas |
| 346.73 |
101.30 |
Azeotropic temperature, K
[ref]
| Mole fraction of 2-Butanone (1) - Liquid |
Azeotropic temperature, K - Liquid |
| 0.6470 |
346.65 |
Azeotropic pressure, kPa
[ref]
| Mole fraction of 2-Butanone (1) - Liquid |
Azeotropic pressure, kPa - Liquid |
| 0.6470 |
101.30 |
Vapor or sublimation pressure, kPa
[ref]
| Temperature, K - Liquid mixture 1 |
Vapor or sublimation pressure, kPa - Gas |
| 346.73 |
101.30 |
Azeotropic temperature, K
[ref]
| Mole fraction of 2-Butanone (1) - Liquid |
Azeotropic temperature, K - Liquid |
| 0.6470 |
346.65 |
Azeotropic pressure, kPa
[ref]
| Mole fraction of 2-Butanone (1) - Liquid |
Azeotropic pressure, kPa - Liquid |
| 0.6470 |
101.30 |
Sources
-
A relative headspace method for Henry s constants of volatile organic compounds
-
Combined effects of salinity and temperature on the solubility of organic compounds
-
Phase equilibria of the ternary systems of (water + diethyl carbonate) with acetone, or 2-butanone at four temperatures
-
Isobaric Vapor Liquid Liquid Phase Equilibria Measurements of Three Ternary Water + 2-Butanone + Aliphatic Alcohol (Ethanol, 1-Propanol, 2-Propanol) Systems at 101.3 kPa
-
Measurement of Henry s Law Constants for Acetone, 2-Butanone, 2,3-Butanedione, and Isobutyraldehyde Using a Horizontal Flow Reactor
-
Determination of Henry s Law Constants and Activity Coefficients at Infinite Dilution of Flavor Compounds in Water at 298 K with a Gas-Chromatographic Method
-
Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
-
Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
-
Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
