- Name
- Acetone
- InChI
- InChI=1S/C3H6O/c1-3(2)4/h1-2H3
- InChI Key
- CSCPPACGZOOCGX-UHFFFAOYSA-N
- Formula
- C3H6O
- SMILES
- CC(C)=O
- Mol. Weight (g/mol)
- 58.08
- CAS
- 67-64-1
- 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
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Datasets
- Activity coefficient (4)
- Henry's Law constant (mole fraction scale), kPa (10)
- n0 - Refractive index (Na D-line) (2)
- ρl - Mass density, kg/m3 (6)
- γ - Surface tension liquid-gas, N/m (2)
- Binary diffusion coefficient, m2/s (6)
- Vapor Liquid Equilibrium at Constant Pressure (3)
Activity coefficient of Acetone (1) [ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Acetone (1) - Liquid |
|---|---|
| 298.01 | 7.62 |
| 298.01 | 7.68 |
| 298.03 | 7.64 |
| 298.03 | 7.7 |
| 298.04 | 7.68 |
| 298.04 | 7.74 |
| 298.17 | 7.7 |
Activity coefficient of Acetone (1) [ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Acetone (1) - Liquid |
|---|---|
| 303.25 | 8.02 |
| 313.25 | 9.2 |
| 323.25 | 9.81 |
| 333.25 | 10.3 |
Activity coefficient of Acetone (1) [ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Acetone (1) - Liquid |
|---|---|
| 298.01 | 7.62 |
| 298.01 | 7.68 |
| 298.03 | 7.64 |
| 298.03 | 7.7 |
| 298.04 | 7.68 |
| 298.04 | 7.74 |
| 298.17 | 7.7 |
Activity coefficient of Acetone (1) [ref]
Operational conditions:
- Pressure, kPa = 101.325 (Liquid)
- Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Activity coefficient of Acetone (1) - Liquid |
|---|---|
| 303.25 | 8.02 |
| 313.25 | 9.2 |
| 323.25 | 9.81 |
| 333.25 | 10.3 |
Henry's Law constant (mole fraction scale), kPa of Acetone (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of Acetone (1) - Liquid |
|---|---|
| 323.15 | 699.1 |
| 333.15 | 1033.5 |
| 343.15 | 1519.9 |
| 353.15 | 2148.1 |
Henry's Law constant (amount concentration scale), kPa*dm3/mol of Acetone (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 Acetone (1) - Liquid |
|---|---|
| 276.00 | 14591.0 |
| 279.00 | 11044.0 |
| 283.00 | 8511.0 |
| 288.00 | 6991.0 |
| 293.00 | 3749.0 |
Henry's Law constant (mole fraction scale), kPa of Acetone (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of Acetone (1) - Liquid |
|---|---|
| 298.01 | 233.0 |
| 298.01 | 235.0 |
| 298.03 | 234.0 |
| 298.03 | 236.0 |
| 298.04 | 236.0 |
| 298.04 | 237.0 |
| 298.17 | 237.0 |
Henry's Law constant (molality scale), kPa*kg/mol of Acetone (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (molality scale), kPa*kg/mol of Acetone (1) - Liquid |
|---|---|
| 274.15 | 0.2310 |
| 294.65 | 1.442 |
| 294.65 | 1.263 |
| 296.15 | 1.133 |
| 310.15 | 7.555 |
| 320.15 | 11.46 |
| 331.15 | 16.01 |
| 333.15 | 41.15 |
Henry's Law constant (mole fraction scale), kPa of Acetone (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of Acetone (1) - Liquid |
|---|---|
| 278.20 | 56.0 |
| 283.20 | 75.0 |
| 288.20 | 100.0 |
| 293.20 | 130.0 |
| 298.20 | 170.0 |
Henry's Law constant (mole fraction scale), kPa of Acetone (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of Acetone (1) - Liquid |
|---|---|
| 323.15 | 699.1 |
| 333.15 | 1033.5 |
| 343.15 | 1519.9 |
| 353.15 | 2148.1 |
Henry's Law constant (amount concentration scale), kPa*dm3/mol of Acetone (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 Acetone (1) - Liquid |
|---|---|
| 276.00 | 14591.0 |
| 279.00 | 11044.0 |
| 283.00 | 8511.0 |
| 288.00 | 6991.0 |
| 293.00 | 3749.0 |
Henry's Law constant (mole fraction scale), kPa of Acetone (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of Acetone (1) - Liquid |
|---|---|
| 298.01 | 233.0 |
| 298.01 | 235.0 |
| 298.03 | 234.0 |
| 298.03 | 236.0 |
| 298.04 | 236.0 |
| 298.04 | 237.0 |
| 298.17 | 237.0 |
Henry's Law constant (molality scale), kPa*kg/mol of Acetone (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (molality scale), kPa*kg/mol of Acetone (1) - Liquid |
|---|---|
| 274.15 | 0.2310 |
| 294.65 | 1.442 |
| 294.65 | 1.263 |
| 296.15 | 1.133 |
| 310.15 | 7.555 |
| 320.15 | 11.46 |
| 331.15 | 16.01 |
| 333.15 | 41.15 |
Henry's Law constant (mole fraction scale), kPa of Acetone (1) [ref]
Operational condition: Mole fraction = 0 (Liquid)
| Temperature, K - Liquid | Henry's Law constant (mole fraction scale), kPa of Acetone (1) - Liquid |
|---|---|
| 278.20 | 56.0 |
| 283.20 | 75.0 |
| 288.20 | 100.0 |
| 293.20 | 130.0 |
| 298.20 | 170.0 |
Refractive index (Na D-line) [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Acetone (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0502 | 1.3422 |
| 0.0993 | 1.3499 |
| 0.1502 | 1.3549 |
| 0.1996 | 1.3583 |
| 0.2496 | 1.3604 |
| 0.3007 | 1.3616 |
| 0.3507 | 1.3621 |
| 0.4003 | 1.3623 |
| 0.4509 | 1.3621 |
| 0.4992 | 1.3618 |
| 0.5489 | 1.3614 |
| 0.5990 | 1.3609 |
| 0.6506 | 1.3603 |
| 0.6996 | 1.3602 |
| 0.7014 | 1.3597 |
| 0.7467 | 1.3591 |
| 0.8011 | 1.3592 |
| 0.8015 | 1.3583 |
| 0.8460 | 1.3577 |
| 0.8969 | 1.3569 |
| 0.9005 | 1.3572 |
| 0.9451 | 1.3564 |
Refractive index (Na D-line) [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Acetone (1) - Liquid | Refractive index (Na D-line) - Liquid |
|---|---|
| 0.0502 | 1.3422 |
| 0.0993 | 1.3499 |
| 0.1502 | 1.3549 |
| 0.1996 | 1.3583 |
| 0.2496 | 1.3604 |
| 0.3007 | 1.3616 |
| 0.3507 | 1.3621 |
| 0.4003 | 1.3623 |
| 0.4509 | 1.3621 |
| 0.4992 | 1.3618 |
| 0.5489 | 1.3614 |
| 0.5990 | 1.3609 |
| 0.6506 | 1.3603 |
| 0.6996 | 1.3602 |
| 0.7014 | 1.3597 |
| 0.7467 | 1.3591 |
| 0.8011 | 1.3592 |
| 0.8015 | 1.3583 |
| 0.8460 | 1.3577 |
| 0.8969 | 1.3569 |
| 0.9005 | 1.3572 |
| 0.9451 | 1.3564 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Acetone (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0502 | 977.0 |
| 0.0993 | 959.3 |
| 0.1502 | 942.2 |
| 0.1996 | 926.6 |
| 0.2496 | 911.8 |
| 0.3007 | 897.6 |
| 0.3507 | 884.8 |
| 0.4003 | 873.1 |
| 0.4509 | 862.1 |
| 0.4992 | 852.5 |
| 0.5489 | 843.5 |
| 0.5990 | 835.0 |
| 0.6506 | 827.0 |
| 0.6996 | 819.9 |
| 0.7014 | 819.6 |
| 0.7467 | 813.4 |
| 0.8011 | 806.2 |
| 0.8015 | 806.3 |
| 0.8460 | 800.8 |
| 0.8969 | 794.9 |
| 0.9005 | 794.5 |
| 0.9451 | 789.9 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Acetone (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.0000 | 283.15 | 999.691 |
| 0.0000 | 288.15 | 999.083 |
| 0.0000 | 293.14 | 998.181 |
| 0.0000 | 298.15 | 997.019 |
| 0.0000 | 303.14 | 995.617 |
| 0.0000 | 308.15 | 994.001 |
| 0.0000 | 313.15 | 992.181 |
| 0.0000 | 318.14 | 990.13 |
| 0.0000 | 323.14 | 988.003 |
| 0.0988 | 283.15 | 966.507 |
| 0.0988 | 288.15 | 963.567 |
| 0.0988 | 293.15 | 960.497 |
| 0.0988 | 298.14 | 957.313 |
| 0.0988 | 303.15 | 954.01 |
| 0.0988 | 308.15 | 950.61 |
| 0.0988 | 313.14 | 947.117 |
| 0.0988 | 318.15 | 943.497 |
| 0.0988 | 323.15 | 939.767 |
| 0.2193 | 283.15 | 932.823 |
| 0.2193 | 288.15 | 928.61 |
| 0.2193 | 293.14 | 924.322 |
| 0.2193 | 298.14 | 919.968 |
| 0.2193 | 303.14 | 915.544 |
| 0.2193 | 308.15 | 911.052 |
| 0.2193 | 313.14 | 906.488 |
| 0.2193 | 318.14 | 901.855 |
| 0.2193 | 323.15 | 897.151 |
| 0.2973 | 283.15 | 913.382 |
| 0.2973 | 288.15 | 908.777 |
| 0.2973 | 293.14 | 904.105 |
| 0.2973 | 298.14 | 899.375 |
| 0.2973 | 303.14 | 894.587 |
| 0.2973 | 308.15 | 889.735 |
| 0.2973 | 313.14 | 884.822 |
| 0.2973 | 318.14 | 879.849 |
| 0.2973 | 323.14 | 874.812 |
| 0.3998 | 283.15 | 889.08 |
| 0.3998 | 288.15 | 884.145 |
| 0.3998 | 293.14 | 879.148 |
| 0.3998 | 298.14 | 874.098 |
| 0.3998 | 303.14 | 868.996 |
| 0.3998 | 308.15 | 863.836 |
| 0.3998 | 313.14 | 858.617 |
| 0.3998 | 318.14 | 853.341 |
| 0.3998 | 323.14 | 848.021 |
| 0.4986 | 283.15 | 868.988 |
| 0.4986 | 288.15 | 863.861 |
| 0.4986 | 293.15 | 858.674 |
| 0.4986 | 298.15 | 853.436 |
| 0.4986 | 303.14 | 848.142 |
| 0.4986 | 308.15 | 842.791 |
| 0.4986 | 313.15 | 837.381 |
| 0.4986 | 318.14 | 831.924 |
| 0.4986 | 323.14 | 826.399 |
| 0.5903 | 283.15 | 853.092 |
| 0.5903 | 288.15 | 847.829 |
| 0.5903 | 293.15 | 842.508 |
| 0.5903 | 298.14 | 837.135 |
| 0.5903 | 303.14 | 831.707 |
| 0.5903 | 308.14 | 826.22 |
| 0.5903 | 313.14 | 820.677 |
| 0.5903 | 318.15 | 815.068 |
| 0.5903 | 323.15 | 809.395 |
| 0.6984 | 283.15 | 836.647 |
| 0.6984 | 288.15 | 831.252 |
| 0.6984 | 293.15 | 825.797 |
| 0.6984 | 298.14 | 820.292 |
| 0.6984 | 303.14 | 814.735 |
| 0.6984 | 308.15 | 809.12 |
| 0.6984 | 313.14 | 803.446 |
| 0.6984 | 318.15 | 797.707 |
| 0.6984 | 323.14 | 791.9 |
| 0.7934 | 283.15 | 824.028 |
| 0.7934 | 288.15 | 818.534 |
| 0.7934 | 293.15 | 812.982 |
| 0.7934 | 298.14 | 807.383 |
| 0.7934 | 303.14 | 801.735 |
| 0.7934 | 308.15 | 796.028 |
| 0.7934 | 313.14 | 790.262 |
| 0.7934 | 318.14 | 784.437 |
| 0.7934 | 323.14 | 778.546 |
| 0.8916 | 283.15 | 812.997 |
| 0.8916 | 288.15 | 807.424 |
| 0.8916 | 293.15 | 801.797 |
| 0.8916 | 298.14 | 796.13 |
| 0.8916 | 303.14 | 790.413 |
| 0.8916 | 308.15 | 784.645 |
| 0.8916 | 313.14 | 778.818 |
| 0.8916 | 318.14 | 772.936 |
| 0.8916 | 323.14 | 766.99 |
| 1.0000 | 283.15 | 801.669 |
| 1.0000 | 288.15 | 796.037 |
| 1.0000 | 293.15 | 790.355 |
| 1.0000 | 298.15 | 784.638 |
| 1.0000 | 303.14 | 778.876 |
| 1.0000 | 308.15 | 773.065 |
| 1.0000 | 313.14 | 767.205 |
| 1.0000 | 318.14 | 761.288 |
| 1.0000 | 323.14 | 755.314 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetone (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 999.12 |
| 288.15 | 0.0099 | 994.9 |
| 288.15 | 0.0500 | 981.27 |
| 288.15 | 0.1000 | 965.81 |
| 288.15 | 0.1500 | 950.41 |
| 288.15 | 0.2000 | 935.61 |
| 288.15 | 0.3000 | 907.7 |
| 288.15 | 0.4000 | 884.77 |
| 288.15 | 0.5000 | 863.71 |
| 288.15 | 0.6000 | 845.83 |
| 288.15 | 0.7000 | 830.7 |
| 288.15 | 0.8000 | 818.04 |
| 288.15 | 0.9000 | 805.86 |
| 288.15 | 1.0000 | 795.65 |
| 293.15 | 0.0000 | 998.22 |
| 293.15 | 0.0099 | 993.87 |
| 293.15 | 0.0500 | 979.34 |
| 293.15 | 0.1000 | 962.9 |
| 293.15 | 0.1500 | 946.79 |
| 293.15 | 0.2000 | 931.54 |
| 293.15 | 0.3000 | 903.09 |
| 293.15 | 0.4000 | 879.81 |
| 293.15 | 0.5000 | 858.56 |
| 293.15 | 0.6000 | 840.53 |
| 293.15 | 0.7000 | 825.3 |
| 293.15 | 0.8000 | 812.56 |
| 293.15 | 0.9000 | 800.27 |
| 293.15 | 1.0000 | 790.04 |
| 298.15 | 0.0000 | 997.06 |
| 298.15 | 0.0099 | 992.55 |
| 298.15 | 0.0500 | 977.21 |
| 298.15 | 0.1000 | 959.83 |
| 298.15 | 0.1500 | 943.05 |
| 298.15 | 0.2000 | 927.37 |
| 298.15 | 0.3000 | 898.35 |
| 298.15 | 0.4000 | 874.8 |
| 298.15 | 0.5000 | 853.35 |
| 298.15 | 0.6000 | 835.15 |
| 298.15 | 0.7000 | 819.8 |
| 298.15 | 0.8000 | 806.97 |
| 298.15 | 0.9000 | 794.6 |
| 298.15 | 1.0000 | 784.33 |
| 303.15 | 0.0000 | 995.67 |
| 303.15 | 0.0099 | 991.0 |
| 303.15 | 0.0500 | 974.89 |
| 303.15 | 0.1000 | 956.64 |
| 303.15 | 0.1500 | 939.23 |
| 303.15 | 0.2000 | 923.1 |
| 303.15 | 0.3000 | 893.54 |
| 303.15 | 0.4000 | 869.68 |
| 303.15 | 0.5000 | 848.07 |
| 303.15 | 0.6000 | 829.71 |
| 303.15 | 0.7000 | 814.25 |
| 303.15 | 0.8000 | 801.32 |
| 303.15 | 0.9000 | 788.88 |
| 303.15 | 1.0000 | 778.57 |
| 308.15 | 0.0000 | 994.04 |
| 308.15 | 0.0099 | 989.16 |
| 308.15 | 0.0500 | 972.41 |
| 308.15 | 0.1000 | 953.33 |
| 308.15 | 0.1500 | 935.32 |
| 308.15 | 0.2000 | 918.78 |
| 308.15 | 0.3000 | 888.68 |
| 308.15 | 0.4000 | 864.53 |
| 308.15 | 0.5000 | 842.72 |
| 308.15 | 0.6000 | 824.22 |
| 308.15 | 0.7000 | 808.63 |
| 308.15 | 0.8000 | 795.62 |
| 308.15 | 0.9000 | 783.11 |
| 308.15 | 1.0000 | 772.76 |
| 313.15 | 0.0000 | 992.23 |
| 313.15 | 0.0099 | 987.26 |
| 313.15 | 0.0500 | 969.77 |
| 313.15 | 0.1000 | 949.91 |
| 313.15 | 0.1500 | 931.31 |
| 313.15 | 0.2000 | 914.37 |
| 313.15 | 0.3000 | 883.75 |
| 313.15 | 0.4000 | 859.33 |
| 313.15 | 0.5000 | 837.31 |
| 313.15 | 0.6000 | 818.66 |
| 313.15 | 0.7000 | 802.96 |
| 313.15 | 0.8000 | 789.84 |
| 313.15 | 0.9000 | 777.29 |
| 313.15 | 1.0000 | 766.91 |
| 318.15 | 0.0000 | 990.23 |
| 318.15 | 0.0099 | 985.07 |
| 318.15 | 0.0500 | 966.73 |
| 318.15 | 0.1000 | 946.37 |
| 318.15 | 0.1500 | 927.21 |
| 318.15 | 0.2000 | 909.89 |
| 318.15 | 0.3000 | 878.76 |
| 318.15 | 0.4000 | 854.06 |
| 318.15 | 0.5000 | 831.85 |
| 318.15 | 0.6000 | 813.05 |
| 318.15 | 0.7000 | 797.22 |
| 318.15 | 0.8000 | 784.05 |
| 318.15 | 0.9000 | 771.4 |
| 318.15 | 1.0000 | 760.99 |
| 323.15 | 0.0000 | 988.01 |
| 323.15 | 0.0099 | 982.76 |
| 323.15 | 0.0500 | 963.1 |
| 323.15 | 0.1000 | 942.68 |
| 323.15 | 0.1500 | 923.0 |
| 323.15 | 0.2000 | 905.19 |
| 323.15 | 0.3000 | 873.7 |
| 323.15 | 0.4000 | 848.74 |
| 323.15 | 0.5000 | 826.32 |
| 323.15 | 0.6000 | 807.35 |
| 323.15 | 0.7000 | 791.42 |
| 323.15 | 0.8000 | 778.16 |
| 323.15 | 0.9000 | 765.46 |
| 323.15 | 1.0000 | 755.02 |
| 328.15 | 0.0000 | 985.69 |
| 328.15 | 0.0099 | 980.29 |
| 328.15 | 0.0500 | 959.94 |
| 328.15 | 0.1000 | 938.87 |
| 328.15 | 0.1500 | 918.72 |
| 328.15 | 0.2000 | 900.64 |
| 328.15 | 0.3000 | 868.56 |
| 328.15 | 0.4000 | 843.31 |
| 328.15 | 0.5000 | 820.73 |
| 328.15 | 0.6000 | 801.6 |
| 328.15 | 0.7000 | 785.55 |
| 328.15 | 0.8000 | 772.2 |
| 328.15 | 0.9000 | 759.81 |
| 328.15 | 1.0000 | 748.98 |
Mass density, kg/m3 [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101 (Liquid)
| Mole fraction of Acetone (1) - Liquid | Mass density, kg/m3 - Liquid |
|---|---|
| 0.0502 | 977.0 |
| 0.0993 | 959.3 |
| 0.1502 | 942.2 |
| 0.1996 | 926.6 |
| 0.2496 | 911.8 |
| 0.3007 | 897.6 |
| 0.3507 | 884.8 |
| 0.4003 | 873.1 |
| 0.4509 | 862.1 |
| 0.4992 | 852.5 |
| 0.5489 | 843.5 |
| 0.5990 | 835.0 |
| 0.6506 | 827.0 |
| 0.6996 | 819.9 |
| 0.7014 | 819.6 |
| 0.7467 | 813.4 |
| 0.8011 | 806.2 |
| 0.8015 | 806.3 |
| 0.8460 | 800.8 |
| 0.8969 | 794.9 |
| 0.9005 | 794.5 |
| 0.9451 | 789.9 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101.325 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Mole fraction of Acetone (1) - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 0.0000 | 283.15 | 999.691 |
| 0.0000 | 288.15 | 999.083 |
| 0.0000 | 293.14 | 998.181 |
| 0.0000 | 298.15 | 997.019 |
| 0.0000 | 303.14 | 995.617 |
| 0.0000 | 308.15 | 994.001 |
| 0.0000 | 313.15 | 992.181 |
| 0.0000 | 318.14 | 990.13 |
| 0.0000 | 323.14 | 988.003 |
| 0.0988 | 283.15 | 966.507 |
| 0.0988 | 288.15 | 963.567 |
| 0.0988 | 293.15 | 960.497 |
| 0.0988 | 298.14 | 957.313 |
| 0.0988 | 303.15 | 954.01 |
| 0.0988 | 308.15 | 950.61 |
| 0.0988 | 313.14 | 947.117 |
| 0.0988 | 318.15 | 943.497 |
| 0.0988 | 323.15 | 939.767 |
| 0.2193 | 283.15 | 932.823 |
| 0.2193 | 288.15 | 928.61 |
| 0.2193 | 293.14 | 924.322 |
| 0.2193 | 298.14 | 919.968 |
| 0.2193 | 303.14 | 915.544 |
| 0.2193 | 308.15 | 911.052 |
| 0.2193 | 313.14 | 906.488 |
| 0.2193 | 318.14 | 901.855 |
| 0.2193 | 323.15 | 897.151 |
| 0.2973 | 283.15 | 913.382 |
| 0.2973 | 288.15 | 908.777 |
| 0.2973 | 293.14 | 904.105 |
| 0.2973 | 298.14 | 899.375 |
| 0.2973 | 303.14 | 894.587 |
| 0.2973 | 308.15 | 889.735 |
| 0.2973 | 313.14 | 884.822 |
| 0.2973 | 318.14 | 879.849 |
| 0.2973 | 323.14 | 874.812 |
| 0.3998 | 283.15 | 889.08 |
| 0.3998 | 288.15 | 884.145 |
| 0.3998 | 293.14 | 879.148 |
| 0.3998 | 298.14 | 874.098 |
| 0.3998 | 303.14 | 868.996 |
| 0.3998 | 308.15 | 863.836 |
| 0.3998 | 313.14 | 858.617 |
| 0.3998 | 318.14 | 853.341 |
| 0.3998 | 323.14 | 848.021 |
| 0.4986 | 283.15 | 868.988 |
| 0.4986 | 288.15 | 863.861 |
| 0.4986 | 293.15 | 858.674 |
| 0.4986 | 298.15 | 853.436 |
| 0.4986 | 303.14 | 848.142 |
| 0.4986 | 308.15 | 842.791 |
| 0.4986 | 313.15 | 837.381 |
| 0.4986 | 318.14 | 831.924 |
| 0.4986 | 323.14 | 826.399 |
| 0.5903 | 283.15 | 853.092 |
| 0.5903 | 288.15 | 847.829 |
| 0.5903 | 293.15 | 842.508 |
| 0.5903 | 298.14 | 837.135 |
| 0.5903 | 303.14 | 831.707 |
| 0.5903 | 308.14 | 826.22 |
| 0.5903 | 313.14 | 820.677 |
| 0.5903 | 318.15 | 815.068 |
| 0.5903 | 323.15 | 809.395 |
| 0.6984 | 283.15 | 836.647 |
| 0.6984 | 288.15 | 831.252 |
| 0.6984 | 293.15 | 825.797 |
| 0.6984 | 298.14 | 820.292 |
| 0.6984 | 303.14 | 814.735 |
| 0.6984 | 308.15 | 809.12 |
| 0.6984 | 313.14 | 803.446 |
| 0.6984 | 318.15 | 797.707 |
| 0.6984 | 323.14 | 791.9 |
| 0.7934 | 283.15 | 824.028 |
| 0.7934 | 288.15 | 818.534 |
| 0.7934 | 293.15 | 812.982 |
| 0.7934 | 298.14 | 807.383 |
| 0.7934 | 303.14 | 801.735 |
| 0.7934 | 308.15 | 796.028 |
| 0.7934 | 313.14 | 790.262 |
| 0.7934 | 318.14 | 784.437 |
| 0.7934 | 323.14 | 778.546 |
| 0.8916 | 283.15 | 812.997 |
| 0.8916 | 288.15 | 807.424 |
| 0.8916 | 293.15 | 801.797 |
| 0.8916 | 298.14 | 796.13 |
| 0.8916 | 303.14 | 790.413 |
| 0.8916 | 308.15 | 784.645 |
| 0.8916 | 313.14 | 778.818 |
| 0.8916 | 318.14 | 772.936 |
| 0.8916 | 323.14 | 766.99 |
| 1.0000 | 283.15 | 801.669 |
| 1.0000 | 288.15 | 796.037 |
| 1.0000 | 293.15 | 790.355 |
| 1.0000 | 298.15 | 784.638 |
| 1.0000 | 303.14 | 778.876 |
| 1.0000 | 308.15 | 773.065 |
| 1.0000 | 313.14 | 767.205 |
| 1.0000 | 318.14 | 761.288 |
| 1.0000 | 323.14 | 755.314 |
Mass density, kg/m3 [ref]
Operational condition: Pressure, kPa = 101 (Liquid)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetone (1) - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 0.0000 | 999.12 |
| 288.15 | 0.0099 | 994.9 |
| 288.15 | 0.0500 | 981.27 |
| 288.15 | 0.1000 | 965.81 |
| 288.15 | 0.1500 | 950.41 |
| 288.15 | 0.2000 | 935.61 |
| 288.15 | 0.3000 | 907.7 |
| 288.15 | 0.4000 | 884.77 |
| 288.15 | 0.5000 | 863.71 |
| 288.15 | 0.6000 | 845.83 |
| 288.15 | 0.7000 | 830.7 |
| 288.15 | 0.8000 | 818.04 |
| 288.15 | 0.9000 | 805.86 |
| 288.15 | 1.0000 | 795.65 |
| 293.15 | 0.0000 | 998.22 |
| 293.15 | 0.0099 | 993.87 |
| 293.15 | 0.0500 | 979.34 |
| 293.15 | 0.1000 | 962.9 |
| 293.15 | 0.1500 | 946.79 |
| 293.15 | 0.2000 | 931.54 |
| 293.15 | 0.3000 | 903.09 |
| 293.15 | 0.4000 | 879.81 |
| 293.15 | 0.5000 | 858.56 |
| 293.15 | 0.6000 | 840.53 |
| 293.15 | 0.7000 | 825.3 |
| 293.15 | 0.8000 | 812.56 |
| 293.15 | 0.9000 | 800.27 |
| 293.15 | 1.0000 | 790.04 |
| 298.15 | 0.0000 | 997.06 |
| 298.15 | 0.0099 | 992.55 |
| 298.15 | 0.0500 | 977.21 |
| 298.15 | 0.1000 | 959.83 |
| 298.15 | 0.1500 | 943.05 |
| 298.15 | 0.2000 | 927.37 |
| 298.15 | 0.3000 | 898.35 |
| 298.15 | 0.4000 | 874.8 |
| 298.15 | 0.5000 | 853.35 |
| 298.15 | 0.6000 | 835.15 |
| 298.15 | 0.7000 | 819.8 |
| 298.15 | 0.8000 | 806.97 |
| 298.15 | 0.9000 | 794.6 |
| 298.15 | 1.0000 | 784.33 |
| 303.15 | 0.0000 | 995.67 |
| 303.15 | 0.0099 | 991.0 |
| 303.15 | 0.0500 | 974.89 |
| 303.15 | 0.1000 | 956.64 |
| 303.15 | 0.1500 | 939.23 |
| 303.15 | 0.2000 | 923.1 |
| 303.15 | 0.3000 | 893.54 |
| 303.15 | 0.4000 | 869.68 |
| 303.15 | 0.5000 | 848.07 |
| 303.15 | 0.6000 | 829.71 |
| 303.15 | 0.7000 | 814.25 |
| 303.15 | 0.8000 | 801.32 |
| 303.15 | 0.9000 | 788.88 |
| 303.15 | 1.0000 | 778.57 |
| 308.15 | 0.0000 | 994.04 |
| 308.15 | 0.0099 | 989.16 |
| 308.15 | 0.0500 | 972.41 |
| 308.15 | 0.1000 | 953.33 |
| 308.15 | 0.1500 | 935.32 |
| 308.15 | 0.2000 | 918.78 |
| 308.15 | 0.3000 | 888.68 |
| 308.15 | 0.4000 | 864.53 |
| 308.15 | 0.5000 | 842.72 |
| 308.15 | 0.6000 | 824.22 |
| 308.15 | 0.7000 | 808.63 |
| 308.15 | 0.8000 | 795.62 |
| 308.15 | 0.9000 | 783.11 |
| 308.15 | 1.0000 | 772.76 |
| 313.15 | 0.0000 | 992.23 |
| 313.15 | 0.0099 | 987.26 |
| 313.15 | 0.0500 | 969.77 |
| 313.15 | 0.1000 | 949.91 |
| 313.15 | 0.1500 | 931.31 |
| 313.15 | 0.2000 | 914.37 |
| 313.15 | 0.3000 | 883.75 |
| 313.15 | 0.4000 | 859.33 |
| 313.15 | 0.5000 | 837.31 |
| 313.15 | 0.6000 | 818.66 |
| 313.15 | 0.7000 | 802.96 |
| 313.15 | 0.8000 | 789.84 |
| 313.15 | 0.9000 | 777.29 |
| 313.15 | 1.0000 | 766.91 |
| 318.15 | 0.0000 | 990.23 |
| 318.15 | 0.0099 | 985.07 |
| 318.15 | 0.0500 | 966.73 |
| 318.15 | 0.1000 | 946.37 |
| 318.15 | 0.1500 | 927.21 |
| 318.15 | 0.2000 | 909.89 |
| 318.15 | 0.3000 | 878.76 |
| 318.15 | 0.4000 | 854.06 |
| 318.15 | 0.5000 | 831.85 |
| 318.15 | 0.6000 | 813.05 |
| 318.15 | 0.7000 | 797.22 |
| 318.15 | 0.8000 | 784.05 |
| 318.15 | 0.9000 | 771.4 |
| 318.15 | 1.0000 | 760.99 |
| 323.15 | 0.0000 | 988.01 |
| 323.15 | 0.0099 | 982.76 |
| 323.15 | 0.0500 | 963.1 |
| 323.15 | 0.1000 | 942.68 |
| 323.15 | 0.1500 | 923.0 |
| 323.15 | 0.2000 | 905.19 |
| 323.15 | 0.3000 | 873.7 |
| 323.15 | 0.4000 | 848.74 |
| 323.15 | 0.5000 | 826.32 |
| 323.15 | 0.6000 | 807.35 |
| 323.15 | 0.7000 | 791.42 |
| 323.15 | 0.8000 | 778.16 |
| 323.15 | 0.9000 | 765.46 |
| 323.15 | 1.0000 | 755.02 |
| 328.15 | 0.0000 | 985.69 |
| 328.15 | 0.0099 | 980.29 |
| 328.15 | 0.0500 | 959.94 |
| 328.15 | 0.1000 | 938.87 |
| 328.15 | 0.1500 | 918.72 |
| 328.15 | 0.2000 | 900.64 |
| 328.15 | 0.3000 | 868.56 |
| 328.15 | 0.4000 | 843.31 |
| 328.15 | 0.5000 | 820.73 |
| 328.15 | 0.6000 | 801.6 |
| 328.15 | 0.7000 | 785.55 |
| 328.15 | 0.8000 | 772.2 |
| 328.15 | 0.9000 | 759.81 |
| 328.15 | 1.0000 | 748.98 |
Surface tension liquid-gas, N/m [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetone (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
| 288.15 | 0.0000 | 0.0735 |
| 288.15 | 0.0099 | 0.0626 |
| 288.15 | 0.0500 | 0.0478 |
| 288.15 | 0.0999 | 0.0403 |
| 288.15 | 0.1500 | 0.0357 |
| 288.15 | 0.1999 | 0.0337 |
| 288.15 | 0.2999 | 0.0306 |
| 288.15 | 0.4000 | 0.0292 |
| 288.15 | 0.4999 | 0.0282 |
| 288.15 | 0.5999 | 0.0273 |
| 288.15 | 0.6999 | 0.0267 |
| 288.15 | 0.7999 | 0.0258 |
| 288.15 | 0.8999 | 0.0251 |
| 288.15 | 1.0000 | 0.0243 |
| 298.15 | 0.0000 | 0.0720 |
| 298.15 | 0.0099 | 0.0610 |
| 298.15 | 0.0500 | 0.0461 |
| 298.15 | 0.0999 | 0.0391 |
| 298.15 | 0.1500 | 0.0344 |
| 298.15 | 0.1999 | 0.0322 |
| 298.15 | 0.2999 | 0.0294 |
| 298.15 | 0.4000 | 0.0280 |
| 298.15 | 0.4999 | 0.0270 |
| 298.15 | 0.5999 | 0.0260 |
| 298.15 | 0.6999 | 0.0254 |
| 298.15 | 0.7999 | 0.0245 |
| 298.15 | 0.8999 | 0.0238 |
| 298.15 | 1.0000 | 0.0230 |
| 308.15 | 0.0000 | 0.0704 |
| 308.15 | 0.0099 | 0.0593 |
| 308.15 | 0.0500 | 0.0448 |
| 308.15 | 0.0999 | 0.0379 |
| 308.15 | 0.1500 | 0.0331 |
| 308.15 | 0.1999 | 0.0307 |
| 308.15 | 0.2999 | 0.0281 |
| 308.15 | 0.4000 | 0.0268 |
| 308.15 | 0.4999 | 0.0258 |
| 308.15 | 0.5999 | 0.0248 |
| 308.15 | 0.6999 | 0.0243 |
| 308.15 | 0.7999 | 0.0232 |
| 308.15 | 0.8999 | 0.0226 |
| 308.15 | 1.0000 | 0.0217 |
| 318.15 | 0.0000 | 0.0688 |
| 318.15 | 0.0099 | 0.0581 |
| 318.15 | 0.0500 | 0.0437 |
| 318.15 | 0.0999 | 0.0369 |
| 318.15 | 0.1500 | 0.0320 |
| 318.15 | 0.1999 | 0.0294 |
| 318.15 | 0.2999 | 0.0270 |
| 318.15 | 0.4000 | 0.0255 |
| 318.15 | 0.4999 | 0.0245 |
| 318.15 | 0.5999 | 0.0236 |
| 318.15 | 0.6999 | 0.0229 |
| 318.15 | 0.7999 | 0.0220 |
| 318.15 | 0.8999 | 0.0212 |
| 318.15 | 1.0000 | 0.0204 |
| 328.15 | 0.0000 | 0.0671 |
| 328.15 | 0.0099 | 0.0577 |
| 328.15 | 0.0500 | 0.0429 |
| 328.15 | 0.0999 | 0.0357 |
| 328.15 | 0.1500 | 0.0308 |
| 328.15 | 0.1999 | 0.0283 |
| 328.15 | 0.2999 | 0.0257 |
| 328.15 | 0.4000 | 0.0242 |
| 328.15 | 0.4999 | 0.0233 |
| 328.15 | 0.5999 | 0.0223 |
| 328.15 | 0.6999 | 0.0217 |
| 328.15 | 0.7999 | 0.0209 |
| 328.15 | 0.8999 | 0.0202 |
| 328.15 | 1.0000 | 0.0192 |
Surface tension liquid-gas, N/m [ref]
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Mole fraction of Acetone (1) - Liquid | Surface tension liquid-gas, N/m - Liquid |
| 288.15 | 0.0000 | 0.0735 |
| 288.15 | 0.0099 | 0.0626 |
| 288.15 | 0.0500 | 0.0478 |
| 288.15 | 0.0999 | 0.0403 |
| 288.15 | 0.1500 | 0.0357 |
| 288.15 | 0.1999 | 0.0337 |
| 288.15 | 0.2999 | 0.0306 |
| 288.15 | 0.4000 | 0.0292 |
| 288.15 | 0.4999 | 0.0282 |
| 288.15 | 0.5999 | 0.0273 |
| 288.15 | 0.6999 | 0.0267 |
| 288.15 | 0.7999 | 0.0258 |
| 288.15 | 0.8999 | 0.0251 |
| 288.15 | 1.0000 | 0.0243 |
| 298.15 | 0.0000 | 0.0720 |
| 298.15 | 0.0099 | 0.0610 |
| 298.15 | 0.0500 | 0.0461 |
| 298.15 | 0.0999 | 0.0391 |
| 298.15 | 0.1500 | 0.0344 |
| 298.15 | 0.1999 | 0.0322 |
| 298.15 | 0.2999 | 0.0294 |
| 298.15 | 0.4000 | 0.0280 |
| 298.15 | 0.4999 | 0.0270 |
| 298.15 | 0.5999 | 0.0260 |
| 298.15 | 0.6999 | 0.0254 |
| 298.15 | 0.7999 | 0.0245 |
| 298.15 | 0.8999 | 0.0238 |
| 298.15 | 1.0000 | 0.0230 |
| 308.15 | 0.0000 | 0.0704 |
| 308.15 | 0.0099 | 0.0593 |
| 308.15 | 0.0500 | 0.0448 |
| 308.15 | 0.0999 | 0.0379 |
| 308.15 | 0.1500 | 0.0331 |
| 308.15 | 0.1999 | 0.0307 |
| 308.15 | 0.2999 | 0.0281 |
| 308.15 | 0.4000 | 0.0268 |
| 308.15 | 0.4999 | 0.0258 |
| 308.15 | 0.5999 | 0.0248 |
| 308.15 | 0.6999 | 0.0243 |
| 308.15 | 0.7999 | 0.0232 |
| 308.15 | 0.8999 | 0.0226 |
| 308.15 | 1.0000 | 0.0217 |
| 318.15 | 0.0000 | 0.0688 |
| 318.15 | 0.0099 | 0.0581 |
| 318.15 | 0.0500 | 0.0437 |
| 318.15 | 0.0999 | 0.0369 |
| 318.15 | 0.1500 | 0.0320 |
| 318.15 | 0.1999 | 0.0294 |
| 318.15 | 0.2999 | 0.0270 |
| 318.15 | 0.4000 | 0.0255 |
| 318.15 | 0.4999 | 0.0245 |
| 318.15 | 0.5999 | 0.0236 |
| 318.15 | 0.6999 | 0.0229 |
| 318.15 | 0.7999 | 0.0220 |
| 318.15 | 0.8999 | 0.0212 |
| 318.15 | 1.0000 | 0.0204 |
| 328.15 | 0.0000 | 0.0671 |
| 328.15 | 0.0099 | 0.0577 |
| 328.15 | 0.0500 | 0.0429 |
| 328.15 | 0.0999 | 0.0357 |
| 328.15 | 0.1500 | 0.0308 |
| 328.15 | 0.1999 | 0.0283 |
| 328.15 | 0.2999 | 0.0257 |
| 328.15 | 0.4000 | 0.0242 |
| 328.15 | 0.4999 | 0.0233 |
| 328.15 | 0.5999 | 0.0223 |
| 328.15 | 0.6999 | 0.0217 |
| 328.15 | 0.7999 | 0.0209 |
| 328.15 | 0.8999 | 0.0202 |
| 328.15 | 1.0000 | 0.0192 |
Binary diffusion coefficient, m2/s [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetone (1) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0040 | 0.0000 |
| 0.1000 | 0.0000 |
| 0.3000 | 0.0000 |
| 0.5000 | 0.0000 |
| 0.7000 | 0.0000 |
| 0.9000 | 0.0000 |
| 0.9750 | 0.0000 |
Binary diffusion coefficient, m2/s [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetone (1) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0040 | 0.0000 |
| 0.1000 | 0.0000 |
| 0.3000 | 0.0000 |
| 0.5000 | 0.0000 |
| 0.7000 | 0.0000 |
| 0.9000 | 0.0000 |
| 0.9750 | 0.0000 |
Binary diffusion coefficient, m2/s [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Acetone (1) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0018 | 0.0000 |
| 0.0018 | 0.0000 |
| 0.0041 | 0.0000 |
| 0.0043 | 0.0000 |
| 0.0045 | 0.0000 |
| 0.0979 | 0.0000 |
| 0.1061 | 0.0000 |
| 0.2916 | 0.0000 |
| 0.3068 | 0.0000 |
| 0.4818 | 0.0000 |
| 0.5161 | 0.0000 |
| 0.5234 | 0.0000 |
| 0.5375 | 0.0000 |
| 0.6695 | 0.0000 |
| 0.6698 | 0.0000 |
| 0.7099 | 0.0000 |
| 0.8547 | 0.0000 |
| 0.9774 | 0.0000 |
Binary diffusion coefficient, m2/s [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetone (1) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0040 | 0.0000 |
| 0.1000 | 0.0000 |
| 0.3000 | 0.0000 |
| 0.5000 | 0.0000 |
| 0.7000 | 0.0000 |
| 0.9000 | 0.0000 |
| 0.9750 | 0.0000 |
Binary diffusion coefficient, m2/s [ref]
Operational conditions:
- Pressure, kPa = 101 (Liquid)
- Temperature, K = 298.15 (Liquid)
| Mole fraction of Acetone (1) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0040 | 0.0000 |
| 0.1000 | 0.0000 |
| 0.3000 | 0.0000 |
| 0.5000 | 0.0000 |
| 0.7000 | 0.0000 |
| 0.9000 | 0.0000 |
| 0.9750 | 0.0000 |
Binary diffusion coefficient, m2/s [ref]
Operational conditions:
- Temperature, K = 298.15 (Liquid)
- Pressure, kPa = 101.3 (Liquid)
| Mole fraction of Acetone (1) - Liquid | Binary diffusion coefficient, m2/s - Liquid |
|---|---|
| 0.0018 | 0.0000 |
| 0.0018 | 0.0000 |
| 0.0041 | 0.0000 |
| 0.0043 | 0.0000 |
| 0.0045 | 0.0000 |
| 0.0979 | 0.0000 |
| 0.1061 | 0.0000 |
| 0.2916 | 0.0000 |
| 0.3068 | 0.0000 |
| 0.4818 | 0.0000 |
| 0.5161 | 0.0000 |
| 0.5234 | 0.0000 |
| 0.5375 | 0.0000 |
| 0.6695 | 0.0000 |
| 0.6698 | 0.0000 |
| 0.7099 | 0.0000 |
| 0.8547 | 0.0000 |
| 0.9774 | 0.0000 |
Vapor Liquid Equilibrium at Constant Pressure [ref]
Operational condition: Pressure, kPa = 101.33 (VLE)
| Fixed | Measured | |
|---|---|---|
| T [K] - VLE | x1[mol/mol] of Acetone (1) - Liquid | y1[mol/mol] of Acetone (1) - Vapour |
| 368.25 | 0.0080 | 0.1380 |
| 363.25 | 0.0160 | 0.2770 |
| 355.25 | 0.0330 | 0.4790 |
| 349.35 | 0.0520 | 0.6040 |
| 345.35 | 0.0720 | 0.6750 |
| 342.65 | 0.0940 | 0.7190 |
| 340.75 | 0.1170 | 0.7380 |
| 338.15 | 0.1710 | 0.7760 |
| 336.45 | 0.2370 | 0.8000 |
| 335.15 | 0.3180 | 0.8220 |
| 334.15 | 0.4200 | 0.8390 |
| 333.05 | 0.5540 | 0.8630 |
| 331.35 | 0.7360 | 0.9090 |
Vapor Liquid Equilibrium at Constant Pressure [ref]
Operational condition: Pressure, kPa = 344.73 (VLE)
| Fixed | Measured | |
|---|---|---|
| T [K] - VLE | x1[mol/mol] of Acetone (1) - Liquid | y1[mol/mol] of Acetone (1) - Vapour |
| 395.65 | 0.0170 | 0.3490 |
| 393.15 | 0.0240 | 0.3980 |
| 385.15 | 0.0550 | 0.5180 |
| 379.15 | 0.1070 | 0.6080 |
| 375.95 | 0.1940 | 0.6700 |
| 374.45 | 0.2730 | 0.6950 |
| 373.05 | 0.3880 | 0.7180 |
| 372.15 | 0.5450 | 0.7470 |
| 371.95 | 0.6330 | 0.7680 |
| 371.75 | 0.7780 | 0.8300 |
| 371.55 | 0.8900 | 0.9030 |
| 371.35 | 0.9500 | 0.9510 |
Vapor Liquid Equilibrium at Constant Pressure [ref]
Operational condition: Pressure, kPa = 689.48 (VLE)
| Fixed | Measured | |
|---|---|---|
| T [K] - VLE | x1[mol/mol] of Acetone (1) - Liquid | y1[mol/mol] of Acetone (1) - Vapour |
| 423.85 | 0.0140 | 0.2490 |
| 415.45 | 0.0360 | 0.3950 |
| 409.55 | 0.0780 | 0.5070 |
| 404.25 | 0.1440 | 0.5820 |
| 402.75 | 0.2290 | 0.6180 |
| 402.15 | 0.3410 | 0.6500 |
| 401.45 | 0.4440 | 0.6650 |
| 399.75 | 0.5590 | 0.7000 |
| 398.85 | 0.7540 | 0.7810 |
| 398.55 | 0.8420 | 0.8450 |
| 399.15 | 0.9250 | 0.9120 |
Sources
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- A relative headspace method for Henry s constants of volatile organic compounds
- Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
- Physical properties and their corresponding changes of mixing for the ternary mixture acetone + n-hexane +water at 298.15K
- Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
- 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
- Ternary Diffusion Coefficients of Glycerol + Acetone + Water by Taylor Dispersion Measurements at 298.15 K
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Surface Tension of the Ternary System Water + Acetone + Toluene
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K