- InChI
- InChI=1S/C5H10O/c1-3-5(6)4-2/h3-4H2,1-2H3
- InChI Key
- FDPIMTJIUBPUKL-UHFFFAOYSA-N
- Formula
- C5H10O
- SMILES
- CCC(=O)CC
- Molecular Weight1
- 86.13
- CAS
- 96-22-0
- Other Names
-
- (C2H5)2CO
- 1,3-Dimethylacetone
- DEK
- Diethyl ketone
- Diethylcetone
- Dimethylacetone
- Ethyl ketone
- Ethyl propionyl
- Metacetone
- Methacetone
- NSC 8653
- PROPIONE
- Pentan-3-one
- Pentanone-3
- UN 1156
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3440 | KDB | |
| PAff | 836.80 | kJ/mol | NIST |
| BasG | [802.60; 807.00] | kJ/mol |
|
| BasG | 807.00 | kJ/mol | NIST |
| BasG | 803.80 ± 0.30 | kJ/mol | NIST |
| BasG | 802.60 | kJ/mol | NIST |
| ΔcH°liquid | [-3104.70; -3100.20] | kJ/mol |
|
| ΔcH°liquid | -3104.70 ± 0.90 | kJ/mol | NIST |
| ΔcH°liquid | -3100.20 ± 1.00 | kJ/mol | NIST |
| μ | 2.70 | debye | KDB |
| ΔfG° | -135.40 | kJ/mol | KDB |
| ΔfH°gas | [-260.50; -253.40] | kJ/mol |
|
| ΔfH°gas | -258.80 | kJ/mol | KDB |
| ΔfH°gas | -253.40 ± 0.90 | kJ/mol | NIST |
| ΔfH°gas | -257.95 ± 0.84 | kJ/mol | NIST |
| ΔfH°gas | -260.50 ± 1.60 | kJ/mol | NIST |
| ΔfH°liquid | -296.51 ± 0.83 | kJ/mol | NIST |
| ΔfusH° | 10.30 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [38.50; 38.70] | kJ/mol |
|
| ΔvapH° | 38.68 | kJ/mol | NIST |
| ΔvapH° | 38.52 | kJ/mol | NIST |
| ΔvapH° | 38.50 | kJ/mol | NIST |
| ΔvapH° | 38.70 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 38.60 | kJ/mol | NIST |
| IE | [9.22; 9.37] | eV |
|
| IE | 9.31 ± 0.02 | eV | NIST |
| IE | 9.31 | eV | NIST |
| IE | 9.30 | eV | NIST |
| IE | Outlier 9.22 ± 0.02 | eV | NIST |
| IE | 9.31 ± 0.01 | eV | NIST |
| IE | 9.31 ± 0.01 | eV | NIST |
| IE | 9.37 ± 0.03 | eV | NIST |
| IE | 9.31 ± 0.02 | eV | NIST |
| IE | 9.32 ± 0.01 | eV | NIST |
| log10WS | [-0.28; -0.28] |
|
|
| log10WS | -0.28 | Aq. Sol... | |
| log10WS | -0.28 | Estimat... | |
| logPoct/wat | 1.375 | Crippen Calculated Property | |
| McVol | 82.880 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3729.00; 3740.00] | kPa |
|
| Pc | 3729.00 | kPa | KDB |
| Pc | 3729.00 ± 10.00 | kPa | NIST |
| Pc | 3740.00 ± 41.40 | kPa | NIST |
| ρc | 255.81 ± 30.15 | kg/m3 | NIST |
| Inp | [638.00; 707.00] |
|
|
| Inp | 676.40 | NIST | |
| Inp | 676.91 | NIST | |
| Inp | 675.75 | NIST | |
| Inp | 675.42 | NIST | |
| Inp | 675.52 | NIST | |
| Inp | 675.84 | NIST | |
| Inp | 677.74 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | Outlier 640.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | Outlier 638.00 | NIST | |
| Inp | 647.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 647.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 670.00 | NIST | |
| Inp | 659.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 707.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 703.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 697.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 701.30 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 669.92 | NIST | |
| Inp | 701.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 643.00 | NIST | |
| I | [956.00; 1011.30] |
|
|
| I | Outlier 1011.30 | NIST | |
| I | 996.90 | NIST | |
| I | 1001.50 | NIST | |
| I | Outlier 1006.30 | NIST | |
| I | 974.00 | NIST | |
| I | 976.00 | NIST | |
| I | 958.00 | NIST | |
| I | 983.00 | NIST | |
| I | 983.00 | NIST | |
| I | 983.00 | NIST | |
| I | 978.00 | NIST | |
| I | 977.00 | NIST | |
| I | 970.00 | NIST | |
| I | 956.00 | NIST | |
| I | 979.00 | NIST | |
| I | 979.00 | NIST | |
| I | 970.00 | NIST | |
| I | 981.00 | NIST | |
| I | 975.00 | NIST | |
| I | 964.00 | NIST | |
| I | 980.00 | NIST | |
| I | 971.00 | NIST | |
| I | 969.00 | NIST | |
| I | 1002.00 | NIST | |
| I | 983.00 | NIST | |
| I | 980.00 | NIST | |
| I | 997.00 | NIST | |
| I | 980.00 | NIST | |
| I | 986.00 | NIST | |
| I | 965.00 | NIST | |
| I | 977.00 | NIST | |
| I | 981.00 | NIST | |
| I | 965.00 | NIST | |
| I | 977.00 | NIST | |
| I | 970.00 | NIST | |
| I | 971.00 | NIST | |
| S°liquid | 266.00 | J/mol×K | NIST |
| Tboil | 375.11 | K | KDB |
| Tc | [560.90; 561.50] | K |
|
| Tc | 561.46 | K | KDB |
| Tc | 561.50 | K | NIST |
| Tc | 561.46 ± 0.20 | K | NIST |
| Tc | 560.90 ± 0.56 | K | NIST |
| Tfus | [231.15; 234.18] | K |
|
| Tfus | 234.00 | K | KDB |
| Tfus | 233.90 | K | Aq. Sol... |
| Tfus | 234.15 ± 0.02 | K | NIST |
| Tfus | 234.18 ± 0.01 | K | NIST |
| Tfus | 233.35 ± 0.40 | K | NIST |
| Tfus | 231.20 ± 1.50 | K | NIST |
| Tfus | 231.15 ± 0.50 | K | NIST |
| Ttriple | [234.16; 234.36] | K |
|
| Ttriple | 234.36 | K | Thermod... |
| Ttriple | 234.16 ± 0.03 | K | NIST |
| Ttriple | 234.16 ± 0.03 | K | NIST |
| Vc | 0.336 | m3/kmol | KDB |
| Zc | 0.2683960 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [146.31; 175.14] | J/mol×K | [364.15; 473.15] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 145 150 155 160 165 170 175 400 450 | ||||
| Cp,gas | 146.31 | J/mol×K | 364.15 | NIST |
| Cp,gas | 151.38 | J/mol×K | 383.15 | NIST |
| Cp,gas | 156.77 | J/mol×K | 403.15 | NIST |
| Cp,gas | 162.13 | J/mol×K | 423.15 | NIST |
| Cp,gas | 168.70 | J/mol×K | 448.15 | NIST |
| Cp,gas | 175.14 | J/mol×K | 473.15 | NIST |
| Cp,liquid | [190.00; 200.70] | J/mol×K | [298.15; 298.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 190 192 194 196 198 200 | ||||
| Cp,liquid | 196.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 195.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 190.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 190.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 200.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 190.90 | J/mol×K | 298.15 | NIST |
| η | [0.0003760; 0.0004714] | Pa×s | [293.15; 313.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 3.80e-4 4.00e-4 4.20e-4 4.40e-4 4.60e-4 4.80e-4 295 300 305 310 | ||||
| η | 0.0004714 | Pa×s | 293.15 | Viscosi... |
| η | 0.0004490 | Pa×s | 298.15 | Density... |
| η | 0.0004231 | Pa×s | 303.15 | Viscosi... |
| η | 0.0004290 | Pa×s | 303.15 | Densiti... |
| η | 0.0004190 | Pa×s | 303.15 | Density... |
| η | 0.0003960 | Pa×s | 308.15 | Density... |
| η | 0.0003970 | Pa×s | 308.15 | Densiti... |
| η | 0.0003880 | Pa×s | 313.15 | Densiti... |
| η | 0.0003799 | Pa×s | 313.15 | Viscosi... |
| η | 0.0003760 | Pa×s | 313.15 | Density... |
| ΔfusH | [0.01; 11.59] | kJ/mol | [118.50; 234.20] |
|
| ΔfusH | 0.11 | kJ/mol | 118.50 | NIST |
| ΔfusH | 0.01 | kJ/mol | 180.00 | NIST |
| ΔfusH | 11.59 | kJ/mol | 234.20 | NIST |
| ΔfusH | 11.59 | kJ/mol | 234.20 | NIST |
| ΔvapH | [33.30; 36.90] | kJ/mol | [303.00; 527.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 33 34 35 36 37 300 400 500 | ||||
| ΔvapH | 36.90 | kJ/mol | 303.00 | NIST |
| ΔvapH | 35.90 ± 0.20 | kJ/mol | 332.50 | NIST |
| ΔvapH | 36.10 ± 0.10 | kJ/mol | 335.00 | NIST |
| ΔvapH | 34.90 ± 0.10 | kJ/mol | 354.00 | NIST |
| ΔvapH | 36.60 | kJ/mol | 356.50 | NIST |
| ΔvapH | 33.50 ± 0.10 | kJ/mol | 375.00 | NIST |
| ΔvapH | 33.45 | kJ/mol | 375.20 | NIST |
| ΔvapH | 36.60 | kJ/mol | 377.50 | NIST |
| ΔvapH | 33.70 | kJ/mol | 461.50 | NIST |
| ΔvapH | 33.30 | kJ/mol | 527.50 | NIST |
| n0 | [1.39000; 1.39020] | [298.15; 298.15] |
|
|
| n0 | 1.39020 | 298.15 | Excess ... | |
| n0 | 1.39000 | 298.15 | Phase E... | |
| ρl | [789.41; 818.90] | kg/m3 | [288.15; 318.15] |
|
|
T(K) Liquid Density (kg/m3) 790 795 800 805 810 815 820 290 300 310 | ||||
| ρl | 818.90 | kg/m3 | 288.15 | Thermal... |
| ρl | 814.00 | kg/m3 | 293.00 | KDB |
| ρl | 809.09 | kg/m3 | 298.15 | Excess ... |
| ρl | 809.38 | kg/m3 | 298.15 | Excess ... |
| ρl | 809.16 | kg/m3 | 298.15 | Thermal... |
| ρl | 804.62 | kg/m3 | 303.15 | Excess ... |
| ρl | 799.55 | kg/m3 | 308.15 | Excess ... |
| ρl | 799.32 | kg/m3 | 308.15 | Thermal... |
| ρl | 789.63 | kg/m3 | 318.15 | Excess ... |
| ρl | 789.41 | kg/m3 | 318.15 | Thermal... |
| ΔfusS | [0.04; 49.50] | J/mol×K | [118.50; 234.20] |
|
| ΔfusS | 0.96 | J/mol×K | 118.50 | NIST |
| ΔfusS | 0.04 | J/mol×K | 180.00 | NIST |
| ΔfusS | 49.50 | J/mol×K | 234.20 | NIST |
| csound,fluid | [1160.00; 1197.00] | m/s | [303.15; 313.15] |
|
| csound,fluid | 1197.00 | m/s | 303.15 | Densiti... |
| csound,fluid | 1179.00 | m/s | 308.15 | Densiti... |
| csound,fluid | 1160.00 | m/s | 313.15 | Densiti... |
| γ | [0.02; 0.03] | N/m | [283.15; 329.15] |
|
|
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.03 0.03 300 320 | ||||
| γ | 0.03 | N/m | 283.15 | Thermod... |
| γ | 0.03 | N/m | 285.15 | Thermod... |
| γ | 0.03 | N/m | 287.15 | Thermod... |
| γ | 0.03 | N/m | 289.15 | Thermod... |
| γ | 0.03 | N/m | 291.15 | Thermod... |
| γ | 0.03 | N/m | 293.15 | Thermod... |
| γ | 0.03 | N/m | 295.15 | Thermod... |
| γ | 0.03 | N/m | 297.15 | Thermod... |
| γ | 0.03 | N/m | 299.15 | Thermod... |
| γ | 0.02 | N/m | 301.15 | Thermod... |
| γ | 0.02 | N/m | 303.15 | Thermod... |
| γ | 0.02 | N/m | 305.15 | Thermod... |
| γ | 0.02 | N/m | 307.15 | Thermod... |
| γ | 0.02 | N/m | 309.15 | Thermod... |
| γ | 0.02 | N/m | 311.15 | Thermod... |
| γ | 0.02 | N/m | 313.15 | Thermod... |
| γ | 0.02 | N/m | 315.15 | Thermod... |
| γ | 0.02 | N/m | 317.15 | Thermod... |
| γ | 0.02 | N/m | 319.15 | Thermod... |
| γ | 0.02 | N/m | 321.15 | Thermod... |
| γ | 0.02 | N/m | 323.15 | Thermod... |
| γ | 0.02 | N/m | 325.15 | Thermod... |
| γ | 0.02 | N/m | 327.15 | Thermod... |
| γ | 0.02 | N/m | 329.15 | Thermod... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 308.15 | 101.30 | 0.0004 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [274.94; 399.57] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.47173e+01 | |||
| Coefficient B | -3.36681e+03 | |||
| Coefficient C | -4.16190e+01 | |||
| Temperature range, min. | 274.94 | |||
| Temperature range, max. | 399.57 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 274.94 | Calculated Property |
| Pvap | 2.99 | kPa | 288.79 | Calculated Property |
| Pvap | 6.16 | kPa | 302.64 | Calculated Property |
| Pvap | 11.80 | kPa | 316.48 | Calculated Property |
| Pvap | 21.24 | kPa | 330.33 | Calculated Property |
| Pvap | 36.22 | kPa | 344.18 | Calculated Property |
| Pvap | 58.94 | kPa | 358.03 | Calculated Property |
| Pvap | 92.09 | kPa | 371.87 | Calculated Property |
| Pvap | 138.80 | kPa | 385.72 | Calculated Property |
| Pvap | 202.66 | kPa | 399.57 | Calculated Property |
| Pvap | [0.06; 3708.73] | kPa | [234.18; 561.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.00329e+01 | |||
| Coefficient B | -6.68960e+03 | |||
| Coefficient C | -8.16282e+00 | |||
| Coefficient D | 5.65048e-06 | |||
| Temperature range, min. | 234.18 | |||
| Temperature range, max. | 561.00 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 | ||||
| Pvap | 0.06 | kPa | 234.18 | Calculated Property |
| Pvap | 1.00 | kPa | 270.49 | Calculated Property |
| Pvap | 7.53 | kPa | 306.81 | Calculated Property |
| Pvap | 34.69 | kPa | 343.12 | Calculated Property |
| Pvap | 114.38 | kPa | 379.43 | Calculated Property |
| Pvap | 297.85 | kPa | 415.75 | Calculated Property |
| Pvap | 654.34 | kPa | 452.06 | Calculated Property |
| Pvap | 1269.29 | kPa | 488.37 | Calculated Property |
| Pvap | 2245.41 | kPa | 524.69 | Calculated Property |
| Pvap | 3708.73 | kPa | 561.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 3-Pentanone.
Mixtures
- 3-Pentanone + 2-Pyrrolidinone, 1-methyl-
- 3-Pentanone + Dimethyl Sulfoxide
- Acetic acid, chloro-, ethyl ester + 3-Pentanone
- 3-Pentanone + Water
- 2-Pentanone + 3-Pentanone
- 3-Pentanone + 3-Pentanol
- 2-Pentanone + 3-Pentanone + 3-Pentanol
- 3-Pentanone + Ethylbenzene
- 3-Pentanone + o-Xylene
- Ethanedioic acid, diethyl ester + 3-Pentanone
- 3-Pentanone + Acetic acid, butyl ester
- 3-Pentanone + Benzyl nitrile
- 3-Pentanone + Thiophene, tetrahydro-, 1,1-dioxide
- 3-Pentanone + Dodecanedioic acid
- 3-Pentanone + 1-Octanol
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
- Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
- (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
- Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ketones at T = 298.15 K
- Thermodynamic investigation of methyl salicylate/1-pentanol binary system in the temperature range from 278.15 K to 303.15 K
- Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
- Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
- Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
- Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Measurement and correlation of solubility of dodecanedioic acid in different pure solvents from T = (288.15 to 323.15) K
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Solubility measurement, model evaluation and thermodynamic analysis of rivaroxaban polymorphs in organic solvents
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Excess molar volumes, viscosity deviations and excess thermal expansion coefficients for binary and ternary mixtures consist of diethylketone + 2-butanol + ethylchloroacetate at (298.15, 308.15 and 318.15) K
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
- Air-Water Partitioning of C5 and C6 Alkanones: Measurement, Critical Compilation, Correlation, and Recommended Data
- Phase Equilibria in the Binary and Ternary Systems Composed of Diethyl ketone, 2-Pentanone and 3-Pentanol at 101.3 kPa
- Viscosities, Densities, and Ultrasonic Velocities of 3-Pentanone + Ethylbenzene and 3-Pentanone + o-Xylene at (293.15, 303.15, and 313.15) K
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Diethyl Oxalate with Some Ketones at (303.15, 308.15, and 313.15) K
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Density and Viscosity of Binary Mixtures of n-Butyl Acetate with Ketones at (298.15, 303.15, 308.15, and 313.15) K
- Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
- Volumetric and Transport Properties of Binary Liquid Mixtures of Aliphatic Ketones with Phenylacetonitrile at T = 308.15 K
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Densities and Speeds of Sound for Binary Liquid Mixtures of Thiolane-l,l-dioxide with Butanone, Pentan-2-one, Pentan-3-one, and 4-Methyl-pentan-2-one at T = (303.15 or 308.15 or 313.15) K
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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