Datasets
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Mass fraction (10)
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Excess molar enthalpy (molar enthalpy (2)
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γ - Surface tension liquid-gas, N/m (2)
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Tboil - Boiling temperature at pressure P, K (2)
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Azeotropic pressure, kPa (4)
Mass fraction of Acetylacetone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mass fraction of Acetylacetone (1) - Liquid mixture 1 |
288.15 |
0.1364 |
298.15 |
0.1578 |
313.15 |
0.9414 |
313.15 |
0.1695 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
288.15 |
0.0304 |
313.15 |
0.0586 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
283.15 |
0.1104 |
293.15 |
0.1197 |
298.15 |
0.1245 |
303.15 |
0.1397 |
313.15 |
0.1673 |
323.15 |
0.1956 |
333.15 |
0.2428 |
343.15 |
0.2907 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
283.15 |
0.9782 |
293.15 |
0.9716 |
298.15 |
0.9651 |
303.15 |
0.9614 |
313.15 |
0.9585 |
323.15 |
0.9549 |
333.15 |
0.9477 |
343.15 |
0.9376 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Water (2) - Liquid |
Mole fraction of Water (2) - Gas |
0.0280 |
0.2640 |
0.0450 |
0.3860 |
0.0960 |
0.5930 |
0.1250 |
0.6650 |
0.2160 |
0.7480 |
0.3110 |
0.7630 |
0.3620 |
0.7740 |
0.4880 |
0.7740 |
0.6060 |
0.7760 |
0.7120 |
0.7760 |
0.7770 |
0.7780 |
0.8210 |
0.7940 |
0.8720 |
0.8010 |
0.9130 |
0.8210 |
0.9400 |
0.8430 |
0.9580 |
0.8820 |
0.9680 |
0.9070 |
0.9800 |
0.9380 |
Mass fraction of Acetylacetone (1)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mass fraction of Acetylacetone (1) - Liquid mixture 1 |
288.15 |
0.1364 |
298.15 |
0.1578 |
313.15 |
0.9414 |
313.15 |
0.1695 |
Mass fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 2)
Temperature, K - Liquid mixture 1 |
Mass fraction of Water (2) - Liquid mixture 2 |
288.15 |
0.0304 |
313.15 |
0.0586 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 2 |
283.15 |
0.1104 |
293.15 |
0.1197 |
298.15 |
0.1245 |
303.15 |
0.1397 |
313.15 |
0.1673 |
323.15 |
0.1956 |
333.15 |
0.2428 |
343.15 |
0.2907 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 |
Mole fraction of Water (2) - Liquid mixture 1 |
283.15 |
0.9782 |
293.15 |
0.9716 |
298.15 |
0.9651 |
303.15 |
0.9614 |
313.15 |
0.9585 |
323.15 |
0.9549 |
333.15 |
0.9477 |
343.15 |
0.9376 |
Mole fraction of Water (2)
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Water (2) - Liquid |
Mole fraction of Water (2) - Gas |
0.0280 |
0.2640 |
0.0450 |
0.3860 |
0.0960 |
0.5930 |
0.1250 |
0.6650 |
0.2160 |
0.7480 |
0.3110 |
0.7630 |
0.3620 |
0.7740 |
0.4880 |
0.7740 |
0.6060 |
0.7760 |
0.7120 |
0.7760 |
0.7770 |
0.7780 |
0.8210 |
0.7940 |
0.8720 |
0.8010 |
0.9130 |
0.8210 |
0.9400 |
0.8430 |
0.9580 |
0.8820 |
0.9680 |
0.9070 |
0.9800 |
0.9380 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Acetylacetone (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 |
0.2004 |
0.1562 |
298.15 |
0.4007 |
0.3191 |
298.15 |
0.5985 |
0.4905 |
298.15 |
0.6486 |
0.5327 |
298.15 |
0.7007 |
0.5778 |
298.15 |
0.7492 |
0.6211 |
298.15 |
0.7974 |
0.6650 |
298.15 |
0.8507 |
0.6904 |
298.15 |
0.9030 |
0.5691 |
298.15 |
0.9532 |
0.3312 |
313.15 |
0.2004 |
0.3060 |
313.15 |
0.4007 |
0.5056 |
313.15 |
0.5985 |
0.7235 |
313.15 |
0.6486 |
0.7755 |
313.15 |
0.7007 |
0.8322 |
313.15 |
0.7492 |
0.8901 |
313.15 |
0.7974 |
0.9380 |
313.15 |
0.8507 |
0.8439 |
313.15 |
0.9030 |
0.6411 |
313.15 |
0.9532 |
0.3680 |
328.15 |
0.2004 |
0.5153 |
328.15 |
0.4007 |
0.8388 |
328.15 |
0.5985 |
1.1138 |
328.15 |
0.6486 |
1.1879 |
328.15 |
0.7007 |
1.2707 |
328.15 |
0.7492 |
1.307 |
328.15 |
0.7974 |
1.2127 |
328.15 |
0.8507 |
1.0296 |
328.15 |
0.9030 |
0.7421 |
328.15 |
0.9532 |
0.3796 |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol
[ref]
Operational condition: Pressure, kPa =
100 (Liquid)
Fixed |
Measured |
Temperature, K - Liquid |
Mole fraction of Acetylacetone (1) - Liquid |
Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
298.15 |
0.2004 |
0.1562 |
298.15 |
0.4007 |
0.3191 |
298.15 |
0.5985 |
0.4905 |
298.15 |
0.6486 |
0.5327 |
298.15 |
0.7007 |
0.5778 |
298.15 |
0.7492 |
0.6211 |
298.15 |
0.7974 |
0.6650 |
298.15 |
0.8507 |
0.6904 |
298.15 |
0.9030 |
0.5691 |
298.15 |
0.9532 |
0.3312 |
313.15 |
0.2004 |
0.3060 |
313.15 |
0.4007 |
0.5056 |
313.15 |
0.5985 |
0.7235 |
313.15 |
0.6486 |
0.7755 |
313.15 |
0.7007 |
0.8322 |
313.15 |
0.7492 |
0.8901 |
313.15 |
0.7974 |
0.9380 |
313.15 |
0.8507 |
0.8439 |
313.15 |
0.9030 |
0.6411 |
313.15 |
0.9532 |
0.3680 |
328.15 |
0.2004 |
0.5153 |
328.15 |
0.4007 |
0.8388 |
328.15 |
0.5985 |
1.1138 |
328.15 |
0.6486 |
1.1879 |
328.15 |
0.7007 |
1.2707 |
328.15 |
0.7492 |
1.307 |
328.15 |
0.7974 |
1.2127 |
328.15 |
0.8507 |
1.0296 |
328.15 |
0.9030 |
0.7421 |
328.15 |
0.9532 |
0.3796 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Mole fraction of Acetylacetone (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0002 |
0.0707 |
0.0004 |
0.0701 |
0.0005 |
0.0699 |
0.0006 |
0.0695 |
0.0008 |
0.0691 |
0.0010 |
0.0683 |
0.0020 |
0.0655 |
0.0040 |
0.0614 |
0.0050 |
0.0598 |
0.0061 |
0.0583 |
0.0081 |
0.0556 |
0.0103 |
0.0533 |
Surface tension liquid-gas, N/m
[ref]
Operational condition: Temperature, K =
298.15 (Liquid)
Mole fraction of Acetylacetone (1) - Liquid |
Surface tension liquid-gas, N/m - Liquid |
0.0002 |
0.0707 |
0.0004 |
0.0701 |
0.0005 |
0.0699 |
0.0006 |
0.0695 |
0.0008 |
0.0691 |
0.0010 |
0.0683 |
0.0020 |
0.0655 |
0.0040 |
0.0614 |
0.0050 |
0.0598 |
0.0061 |
0.0583 |
0.0081 |
0.0556 |
0.0103 |
0.0533 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0280 |
407.29 |
0.0450 |
401.46 |
0.0960 |
388.41 |
0.1250 |
383.35 |
0.2160 |
372.38 |
0.3110 |
370.46 |
0.3620 |
369.19 |
0.4880 |
368.21 |
0.6060 |
367.89 |
0.7120 |
367.81 |
0.7770 |
367.69 |
0.8210 |
367.77 |
0.8720 |
367.89 |
0.9130 |
368.13 |
0.9400 |
368.33 |
0.9580 |
368.96 |
0.9680 |
369.51 |
0.9800 |
370.47 |
Boiling temperature at pressure P, K
[ref]
Operational condition: Pressure, kPa =
101.3 (Liquid)
Mole fraction of Water (2) - Liquid |
Boiling temperature at pressure P, K - Liquid |
0.0280 |
407.29 |
0.0450 |
401.46 |
0.0960 |
388.41 |
0.1250 |
383.35 |
0.2160 |
372.38 |
0.3110 |
370.46 |
0.3620 |
369.19 |
0.4880 |
368.21 |
0.6060 |
367.89 |
0.7120 |
367.81 |
0.7770 |
367.69 |
0.8210 |
367.77 |
0.8720 |
367.89 |
0.9130 |
368.13 |
0.9400 |
368.33 |
0.9580 |
368.96 |
0.9680 |
369.51 |
0.9800 |
370.47 |
Azeotropic pressure, kPa
[ref]
Mole fraction of Water (2) - Liquid |
Azeotropic pressure, kPa - Liquid |
0.7820 |
101.30 |
Azeotropic temperature, K
[ref]
Mole fraction of Water (2) - Liquid |
Azeotropic temperature, K - Liquid |
0.7820 |
367.71 |
Azeotropic pressure, kPa
[ref]
Mole fraction of Water (2) - Liquid |
Azeotropic pressure, kPa - Liquid |
0.7820 |
101.30 |
Azeotropic temperature, K
[ref]
Mole fraction of Water (2) - Liquid |
Azeotropic temperature, K - Liquid |
0.7820 |
367.71 |
Sources
-
Determination and correlation of molar excess enthalpies of binary systems 2,4-pentanedione + (1-butanol, + 2-methyl-1-propanol, + 1-pentanol, + 1-heptane, + ethyl acetate, and + water)
-
Liquid-liquid equilibrium for the ternary systems of water + acetyl acetone + propyl acetate at several temperatures
-
Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
-
Liquid-Liquid Equilibrium, Solid-Liquid Equilibrium, Densities, and Refractivity of a Water, Chloroform, and Acetylacetone Mixture
-
Isobaric Vapor-Liquid Equilibria for the Binary Systems of Acetic Acid + Isopropenyl Acetate, Acetic Acid + Acetylacetone, and Water + Acetylacetone