- InChI
- InChI=1S/C4H8O/c1-3-4(2)5/h3H2,1-2H3
- InChI Key
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N
- Formula
- C4H8O
- SMILES
- CCC(C)=O
- Molecular Weight1
- 72.11
- CAS
- 78-93-3
- Other Names
-
- 2-Butanal
- 2-Oxobutane
- 2-butanone (MEK)
- 2-butanone (MEK; methyl ethyl ketone)
- 3-Butanone
- Acetone, methyl-
- Aethylmethylketon
- Butan-2-one
- Butanone
- Butanone 2
- C2H5COCH3
- Ethyl methyl cetone
- Ethyl methyl ketone
- Ethylmethylketon
- Ketone, ethyl methyl
- Ketone, methyl ethyl
- MEK
- METHYL ACETONE
- Meetco
- Methyl ethyl ketone
- Metiletilchetone
- Metyloetyloketon
- Rcra waste number U159
- UN 1193
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- 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).
- EA : Electron affinity (eV).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- 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).
- λ : Liquid thermal conductivity (W/m×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 | 0.3200 | KDB | |
| PAff | 827.30 | kJ/mol | NIST |
| Tig | 789.26 | K | KDB |
| BasG | 795.50 | kJ/mol | NIST |
| ΔcH°liquid | [-2444.20; -2436.30] | kJ/mol |
|
| ΔcH°liquid | -2444.20 | kJ/mol | NIST |
| ΔcH°liquid | -2438.40 | kJ/mol | NIST |
| ΔcH°liquid | -2436.30 ± 1.50 | kJ/mol | NIST |
| μ | 3.30 | debye | KDB |
| η | [0.0003730; 0.0004011] | Pa×s |
|
| η | 0.0003880 | Pa×s | A volum... |
| η | 0.0004011 | Pa×s | Densiti... |
| η | 0.0003760 | Pa×s | Viscosi... |
| η | 0.0003730 | Pa×s | Excess ... |
| EA | 9.99e-04 | eV | NIST |
| LFL | 1.80 | % in Air | KDB |
| UFL | 11.50 | % in Air | KDB |
| Tflash,cc | 267.59 | K | KDB |
| Tflash,oc | 266.48 | K | KDB |
| ΔfG° | -146.20 | kJ/mol | KDB |
| ΔfH°gas | [-238.70; -238.10] | kJ/mol |
|
| ΔfH°gas | -238.50 | kJ/mol | KDB |
| ΔfH°gas | -238.60 ± 0.84 | kJ/mol | NIST |
| ΔfH°gas | -238.70 ± 0.96 | kJ/mol | NIST |
| ΔfH°gas | -238.10 | kJ/mol | NIST |
| ΔfH°liquid | [-279.00; -273.30] | kJ/mol |
|
| ΔfH°liquid | -273.30 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -279.00 | kJ/mol | NIST |
| ΔfusH° | 7.71 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [32.00; 35.51] | kJ/mol |
|
| ΔvapH° | 34.92 | kJ/mol | NIST |
| ΔvapH° | 34.73 | kJ/mol | NIST |
| ΔvapH° | 34.80 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 35.51 ± 0.08 | kJ/mol | NIST |
| ΔvapH° | 34.50 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | Outlier 32.00 ± 0.01 | kJ/mol | NIST |
| IE | [9.46; 9.70] | eV |
|
| IE | 9.52 ± 0.04 | eV | NIST |
| IE | 9.52 | eV | NIST |
| IE | Outlier 9.70 | eV | NIST |
| IE | 9.52 | eV | NIST |
| IE | 9.53 ± 0.01 | eV | NIST |
| IE | 9.53 ± 0.01 | eV | NIST |
| IE | 9.54 ± 0.03 | eV | NIST |
| IE | 9.52 | eV | NIST |
| IE | 9.54 ± 0.01 | eV | NIST |
| IE | 9.54 ± 0.01 | eV | NIST |
| IE | 9.51 | eV | NIST |
| IE | 9.48 ± 0.02 | eV | NIST |
| IE | 9.53 ± 0.01 | eV | NIST |
| IE | 9.54 ± 0.03 | eV | NIST |
| IE | 9.50 ± 0.10 | eV | NIST |
| IE | 9.55 ± 0.03 | eV | NIST |
| IE | 9.46 | eV | NIST |
| IE | 9.49 | eV | NIST |
| IE | 9.56 | eV | NIST |
| log10WS | [0.52; 0.52] |
|
|
| log10WS | 0.52 | Aq. Sol... | |
| log10WS | 0.52 | Estimat... | |
| logPoct/wat | 0.985 | Crippen Calculated Property | |
| McVol | 68.790 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3998.00; 4390.00] | kPa |
|
| Pc | 4207.00 | kPa | KDB |
| Pc | 4166.00 ± 15.00 | kPa | NIST |
| Pc | 4166.00 ± 3.00 | kPa | NIST |
| Pc | 4166.00 ± 3.00 | kPa | NIST |
| Pc | 4207.00 ± 10.00 | kPa | NIST |
| Pc | 4165.80 ± 20.68 | kPa | NIST |
| Pc | 4150.00 ± 34.50 | kPa | NIST |
| Pc | 3998.00 ± 202.65 | kPa | NIST |
| Pc | Outlier 4390.00 ± 202.65 | kPa | NIST |
| ρc | [251.65; 269.68] | kg/m3 |
|
| ρc | 269.68 ± 15.14 | kg/m3 | NIST |
| ρc | 251.65 ± 4.33 | kg/m3 | NIST |
| Inp | [533.00; 622.00] |
|
|
| Inp | 549.00 | NIST | |
| Inp | 575.92 | NIST | |
| Inp | 574.45 | NIST | |
| Inp | 572.75 | NIST | |
| Inp | 572.34 | NIST | |
| Inp | 571.45 | NIST | |
| Inp | 572.61 | NIST | |
| Inp | 572.88 | NIST | |
| Inp | 573.87 | NIST | |
| Inp | 575.19 | NIST | |
| Inp | 576.69 | NIST | |
| Inp | 578.90 | NIST | |
| Inp | 581.30 | NIST | |
| Inp | 603.27 | NIST | |
| Inp | 602.14 | NIST | |
| Inp | 601.20 | NIST | |
| Inp | 599.13 | NIST | |
| Inp | 596.14 | NIST | |
| Inp | 598.30 | NIST | |
| Inp | 601.92 | NIST | |
| Inp | 602.60 | NIST | |
| Inp | 603.82 | NIST | |
| Inp | 605.54 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 578.66 | NIST | |
| Inp | 578.89 | NIST | |
| Inp | 570.79 | NIST | |
| Inp | Outlier 538.30 | NIST | |
| Inp | 607.25 | NIST | |
| Inp | 598.20 | NIST | |
| Inp | 609.38 | NIST | |
| Inp | 548.59 | NIST | |
| Inp | 575.77 | NIST | |
| Inp | 575.30 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 574.90 | NIST | |
| Inp | 574.71 | NIST | |
| Inp | 574.80 | NIST | |
| Inp | 574.97 | NIST | |
| Inp | 574.76 | NIST | |
| Inp | 576.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 585.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | 583.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | Outlier 537.50 | NIST | |
| Inp | 597.80 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 599.60 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 581.00 | NIST | |
| Inp | Outlier 538.00 | NIST | |
| Inp | 591.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | Outlier 541.00 | NIST | |
| Inp | Outlier 542.00 | NIST | |
| Inp | Outlier 533.00 | NIST | |
| Inp | Outlier 534.00 | NIST | |
| Inp | 544.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 556.00 | NIST | |
| Inp | 543.00 | NIST | |
| Inp | 557.00 | NIST | |
| Inp | 552.30 | NIST | |
| Inp | 574.00 | NIST | |
| Inp | 552.00 | NIST | |
| Inp | 553.00 | NIST | |
| Inp | 551.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | Outlier 533.00 | NIST | |
| Inp | 551.00 | NIST | |
| Inp | 554.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 551.00 | NIST | |
| Inp | 547.00 | NIST | |
| Inp | 548.00 | NIST | |
| Inp | 549.00 | NIST | |
| Inp | 554.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 543.00 | NIST | |
| Inp | 543.00 | NIST | |
| Inp | 582.70 | NIST | |
| Inp | Outlier 622.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 581.60 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 560.00 | NIST | |
| Inp | 594.70 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 585.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 576.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 576.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 576.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 555.00 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 560.00 | NIST | |
| Inp | 573.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 591.00 | NIST | |
| Inp | 601.80 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 570.06 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 564.00 | NIST | |
| Inp | 576.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | Outlier 622.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 583.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 551.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 551.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | 591.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 559.00 | NIST | |
| Inp | 560.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 567.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 552.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 573.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 601.80 | NIST | |
| Inp | 571.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 582.70 | NIST | |
| Inp | Outlier 622.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 579.00 | NIST | |
| I | [866.00; 953.00] |
|
|
| I | 917.39 | NIST | |
| I | 922.33 | NIST | |
| I | 925.59 | NIST | |
| I | 928.27 | NIST | |
| I | 931.34 | NIST | |
| I | 935.77 | NIST | |
| I | 940.31 | NIST | |
| I | 943.44 | NIST | |
| I | Outlier 946.71 | NIST | |
| I | Outlier 949.95 | NIST | |
| I | 937.60 | NIST | |
| I | 938.60 | NIST | |
| I | Outlier 947.76 | NIST | |
| I | 932.30 | NIST | |
| I | 919.80 | NIST | |
| I | 923.70 | NIST | |
| I | 927.80 | NIST | |
| I | 919.00 | NIST | |
| I | 930.00 | NIST | |
| I | 905.00 | NIST | |
| I | 881.00 | NIST | |
| I | 900.00 | NIST | |
| I | 900.00 | NIST | |
| I | 893.00 | NIST | |
| I | 908.00 | NIST | |
| I | 891.00 | NIST | |
| I | 923.30 | NIST | |
| I | 897.00 | NIST | |
| I | 903.00 | NIST | |
| I | 905.00 | NIST | |
| I | 926.00 | NIST | |
| I | 912.70 | NIST | |
| I | 885.00 | NIST | |
| I | 915.00 | NIST | |
| I | 894.00 | NIST | |
| I | 908.00 | NIST | |
| I | 888.00 | NIST | |
| I | 875.00 | NIST | |
| I | 905.00 | NIST | |
| I | 900.00 | NIST | |
| I | 893.00 | NIST | |
| I | 882.00 | NIST | |
| I | 905.00 | NIST | |
| I | 901.00 | NIST | |
| I | 907.00 | NIST | |
| I | 905.00 | NIST | |
| I | 908.00 | NIST | |
| I | 903.00 | NIST | |
| I | 904.00 | NIST | |
| I | 882.00 | NIST | |
| I | 924.00 | NIST | |
| I | 914.00 | NIST | |
| I | 908.00 | NIST | |
| I | 918.00 | NIST | |
| I | 893.00 | NIST | |
| I | 906.00 | NIST | |
| I | 906.00 | NIST | |
| I | 906.00 | NIST | |
| I | 918.00 | NIST | |
| I | 945.00 | NIST | |
| I | 920.00 | NIST | |
| I | 907.00 | NIST | |
| I | 899.00 | NIST | |
| I | 901.00 | NIST | |
| I | 914.00 | NIST | |
| I | 888.00 | NIST | |
| I | Outlier 866.00 | NIST | |
| I | 901.00 | NIST | |
| I | Outlier 866.00 | NIST | |
| I | Outlier 866.00 | NIST | |
| I | 906.00 | NIST | |
| I | 912.00 | NIST | |
| I | 890.00 | NIST | |
| I | 923.00 | NIST | |
| I | 911.00 | NIST | |
| I | Outlier 953.00 | NIST | |
| I | 912.00 | NIST | |
| I | 888.00 | NIST | |
| I | 888.00 | NIST | |
| I | 889.00 | NIST | |
| I | 903.00 | NIST | |
| I | 910.00 | NIST | |
| I | 894.00 | NIST | |
| I | 906.00 | NIST | |
| I | 909.00 | NIST | |
| I | 882.00 | NIST | |
| I | 901.00 | NIST | |
| I | 907.00 | NIST | |
| I | 909.00 | NIST | |
| I | 908.00 | NIST | |
| I | 894.00 | NIST | |
| I | 875.00 | NIST | |
| I | 881.00 | NIST | |
| I | 920.00 | NIST | |
| I | 904.00 | NIST | |
| I | 908.00 | NIST | |
| I | 908.00 | NIST | |
| I | 908.00 | NIST | |
| I | 930.00 | NIST | |
| I | 908.00 | NIST | |
| I | 891.00 | NIST | |
| I | 905.00 | NIST | |
| I | 903.00 | NIST | |
| I | 924.00 | NIST | |
| I | 914.00 | NIST | |
| I | 906.00 | NIST | |
| I | 907.00 | NIST | |
| I | Outlier 866.00 | NIST | |
| I | 912.00 | NIST | |
| I | 917.39 | NIST | |
| I | 935.77 | NIST | |
| I | 937.60 | NIST | |
| I | 923.70 | NIST | |
| I | 897.00 | NIST | |
| I | 885.00 | NIST | |
| I | 875.00 | NIST | |
| S°liquid | [238.82; 241.40] | J/mol×K |
|
| S°liquid | 239.00 | J/mol×K | NIST |
| S°liquid | 238.82 | J/mol×K | NIST |
| S°liquid | 241.40 | J/mol×K | NIST |
| Tboil | [350.15; 354.15] | K |
|
| Tboil | 352.74 | K | KDB |
| Tboil | 352.85 | K | Excess ... |
| Tboil | 352.68 | K | Measure... |
| Tboil | 352.72 | K | Isobari... |
| Tboil | 352.69 | K | Excess ... |
| Tboil | 352.72 | K | Isobari... |
| Tboil | 352.78 | K | Measure... |
| Tboil | 352.68 | K | Liquid-... |
| Tboil | 352.71 ± 0.10 | K | NIST |
| Tboil | 352.75 ± 0.20 | K | NIST |
| Tboil | 352.67 ± 0.20 | K | NIST |
| Tboil | 352.75 ± 0.20 | K | NIST |
| Tboil | 352.72 ± 0.10 | K | NIST |
| Tboil | 352.71 ± 0.20 | K | NIST |
| Tboil | 352.35 ± 0.50 | K | NIST |
| Tboil | 352.80 | K | NIST |
| Tboil | 352.60 ± 0.40 | K | NIST |
| Tboil | 352.15 ± 0.40 | K | NIST |
| Tboil | 352.60 ± 0.30 | K | NIST |
| Tboil | 352.15 ± 0.50 | K | NIST |
| Tboil | 352.15 ± 0.40 | K | NIST |
| Tboil | 352.65 ± 0.50 | K | NIST |
| Tboil | 352.80 | K | NIST |
| Tboil | 352.71 ± 0.20 | K | NIST |
| Tboil | 352.71 ± 0.30 | K | NIST |
| Tboil | 353.20 ± 0.40 | K | NIST |
| Tboil | 352.50 ± 0.50 | K | NIST |
| Tboil | 352.73 ± 0.30 | K | NIST |
| Tboil | 352.71 ± 0.20 | K | NIST |
| Tboil | 352.83 ± 0.20 | K | NIST |
| Tboil | 353.00 ± 0.40 | K | NIST |
| Tboil | 353.00 ± 0.20 | K | NIST |
| Tboil | 352.70 ± 0.30 | K | NIST |
| Tboil | 352.75 | K | NIST |
| Tboil | 352.65 ± 0.30 | K | NIST |
| Tboil | 352.70 ± 0.30 | K | NIST |
| Tboil | 352.50 ± 0.50 | K | NIST |
| Tboil | 353.15 ± 1.50 | K | NIST |
| Tboil | 352.65 ± 1.00 | K | NIST |
| Tboil | 352.55 ± 1.00 | K | NIST |
| Tboil | 352.75 ± 1.00 | K | NIST |
| Tboil | 352.85 ± 1.00 | K | NIST |
| Tboil | 352.75 ± 1.00 | K | NIST |
| Tboil | 352.65 ± 1.00 | K | NIST |
| Tboil | 352.75 ± 1.00 | K | NIST |
| Tboil | 352.75 ± 1.00 | K | NIST |
| Tboil | 353.15 ± 1.00 | K | NIST |
| Tboil | 352.35 ± 0.50 | K | NIST |
| Tboil | 352.55 ± 0.50 | K | NIST |
| Tboil | 351.75 ± 0.50 | K | NIST |
| Tboil | 352.77 ± 0.30 | K | NIST |
| Tboil | 352.75 ± 1.00 | K | NIST |
| Tboil | 352.40 ± 1.00 | K | NIST |
| Tboil | 352.72 ± 0.30 | K | NIST |
| Tboil | Outlier 350.65 ± 2.00 | K | NIST |
| Tboil | 352.80 ± 1.00 | K | NIST |
| Tboil | 352.65 ± 0.20 | K | NIST |
| Tboil | 352.75 ± 0.50 | K | NIST |
| Tboil | 353.15 ± 1.00 | K | NIST |
| Tboil | 352.65 ± 2.00 | K | NIST |
| Tboil | 351.65 ± 1.00 | K | NIST |
| Tboil | 352.75 ± 1.00 | K | NIST |
| Tboil | 352.80 ± 0.40 | K | NIST |
| Tboil | 351.40 ± 1.00 | K | NIST |
| Tboil | Outlier 350.65 ± 2.00 | K | NIST |
| Tboil | 352.65 ± 1.00 | K | NIST |
| Tboil | 351.55 ± 1.00 | K | NIST |
| Tboil | 353.15 ± 1.00 | K | NIST |
| Tboil | Outlier 354.15 ± 2.00 | K | NIST |
| Tboil | 353.90 ± 1.00 | K | NIST |
| Tboil | Outlier 350.15 ± 5.00 | K | NIST |
| Tboil | 351.85 ± 1.00 | K | NIST |
| Tboil | 352.68 ± 0.20 | K | NIST |
| Tboil | 351.15 ± 2.00 | K | NIST |
| Tboil | 352.70 ± 0.30 | K | NIST |
| Tboil | 352.95 ± 1.00 | K | NIST |
| Tboil | 354.00 ± 2.00 | K | NIST |
| Tboil | 354.00 ± 2.00 | K | NIST |
| Tboil | 352.65 ± 2.00 | K | NIST |
| Tboil | 352.75 ± 0.25 | K | NIST |
| Tboil | 351.15 ± 1.00 | K | NIST |
| Tboil | 352.15 ± 0.50 | K | NIST |
| Tboil | 352.85 ± 0.50 | K | NIST |
| Tboil | 352.30 ± 1.00 | K | NIST |
| Tboil | Outlier 350.90 ± 1.00 | K | NIST |
| Tboil | 352.75 ± 0.30 | K | NIST |
| Tboil | 353.65 ± 2.00 | K | NIST |
| Tboil | 352.40 ± 1.00 | K | NIST |
| Tboil | 351.40 ± 1.00 | K | NIST |
| Tboil | 351.75 ± 1.00 | K | NIST |
| Tboil | 352.80 ± 0.30 | K | NIST |
| Tboil | 352.75 ± 0.50 | K | NIST |
| Tboil | Outlier 354.15 ± 1.00 | K | NIST |
| Tboil | 352.00 ± 2.00 | K | NIST |
| Tboil | 353.75 ± 1.00 | K | NIST |
| Tboil | 351.75 ± 1.00 | K | NIST |
| Tboil | 351.15 ± 4.00 | K | NIST |
| Tboil | Outlier 354.15 ± 2.00 | K | NIST |
| Tc | [533.00; 536.80] | K |
|
| Tc | 536.78 | K | KDB |
| Tc | 536.80 | K | NIST |
| Tc | 535.77 ± 0.20 | K | NIST |
| Tc | 535.77 ± 0.20 | K | NIST |
| Tc | 535.77 ± 0.20 | K | NIST |
| Tc | 536.78 ± 0.20 | K | NIST |
| Tc | 535.77 ± 0.30 | K | NIST |
| Tc | 535.70 ± 0.39 | K | NIST |
| Tc | 533.70 ± 3.00 | K | NIST |
| Tc | Outlier 533.00 ± 3.00 | K | NIST |
| Tfus | [186.00; 186.85] | K |
|
| Tfus | 186.48 | K | KDB |
| Tfus | 186.50 | K | Aq. Sol... |
| Tfus | 186.85 | K | NIST |
| Tfus | 186.42 ± 0.02 | K | NIST |
| Tfus | 186.46 ± 0.01 | K | NIST |
| Tfus | 186.25 ± 0.30 | K | NIST |
| Tfus | 186.00 ± 2.00 | K | NIST |
| Tfus | 186.55 ± 0.30 | K | NIST |
| Tfus | 186.80 ± 0.20 | K | NIST |
| Ttriple | [186.10; 186.50] | K |
|
| Ttriple | 186.50 ± 0.01 | K | NIST |
| Ttriple | 186.47 ± 0.04 | K | NIST |
| Ttriple | 186.40 ± 0.06 | K | NIST |
| Ttriple | 186.48 ± 0.03 | K | NIST |
| Ttriple | 186.10 ± 0.10 | K | NIST |
| Vc | 0.267 | m3/kmol | KDB |
| Zc | 0.2516810 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [113.43; 138.62] | J/mol×K | [347.15; 467.15] |
|
| Cp,gas | 113.43 ± 0.23 | J/mol×K | 347.15 | NIST |
| Cp,gas | 115.65 ± 0.17 | J/mol×K | 358.79 | NIST |
| Cp,gas | 118.70 ± 0.18 | J/mol×K | 371.90 | NIST |
| Cp,gas | 119.03 ± 0.24 | J/mol×K | 372.15 | NIST |
| Cp,gas | 121.75 ± 0.18 | J/mol×K | 385.60 | NIST |
| Cp,gas | 124.39 ± 0.25 | J/mol×K | 397.15 | NIST |
| Cp,gas | 124.60 ± 0.19 | J/mol×K | 399.55 | NIST |
| Cp,gas | 126.98 ± 0.19 | J/mol×K | 410.70 | NIST |
| Cp,gas | 131.71 ± 0.26 | J/mol×K | 432.15 | NIST |
| Cp,gas | 138.62 ± 0.28 | J/mol×K | 467.15 | NIST |
| Cp,liquid | [157.91; 162.20] | J/mol×K | [293.00; 303.15] |
|
| Cp,liquid | 158.00 | J/mol×K | 293.00 | NIST |
| Cp,liquid | 160.70 | J/mol×K | 297.00 | NIST |
| Cp,liquid | 160.70 | J/mol×K | 297.00 | NIST |
| Cp,liquid | 158.40 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 159.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 157.91 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 158.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 158.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 158.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 158.91 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 158.41 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 159.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 162.20 | J/mol×K | 303.15 | NIST |
| η | [0.0002545; 0.0004306] | Pa×s | [288.15; 323.15] |
|
| η | 0.0004306 | Pa×s | 288.15 | Densiti... |
| η | 0.0004306 | Pa×s | 288.15 | Densiti... |
| η | 0.0004136 | Pa×s | 293.15 | Densiti... |
| η | 0.0004136 | Pa×s | 293.15 | Densiti... |
| η | 0.0003980 | Pa×s | 293.15 | Dynamic... |
| η | 0.0003980 | Pa×s | 293.15 | Physica... |
| η | 0.0003956 | Pa×s | 293.15 | Densiti... |
| η | 0.0003810 | Pa×s | 298.15 | Densiti... |
| η | 0.0003962 | Pa×s | 298.15 | Densiti... |
| η | 0.0003856 | Pa×s | 298.15 | Density... |
| η | 0.0003856 | Pa×s | 298.15 | Excess ... |
| η | 0.0003780 | Pa×s | 298.15 | Physica... |
| η | 0.0002828 | Pa×s | 298.15 | Densiti... |
| η | 0.0003780 | Pa×s | 298.15 | Dynamic... |
| η | 0.0003962 | Pa×s | 298.15 | Densiti... |
| η | 0.0003620 | Pa×s | 303.15 | Densiti... |
| η | 0.0003600 | Pa×s | 303.15 | Dynamic... |
| η | 0.0003793 | Pa×s | 303.15 | Densiti... |
| η | 0.0003653 | Pa×s | 303.15 | Density... |
| η | 0.0003680 | Pa×s | 303.15 | Densiti... |
| η | 0.0003653 | Pa×s | 303.15 | Excess ... |
| η | 0.0003600 | Pa×s | 303.15 | Physica... |
| η | 0.0002666 | Pa×s | 303.15 | Densiti... |
| η | 0.0003793 | Pa×s | 303.15 | Densiti... |
| η | 0.0003440 | Pa×s | 308.15 | Excess ... |
| η | 0.0003520 | Pa×s | 308.15 | Densiti... |
| η | 0.0002601 | Pa×s | 308.15 | Densiti... |
| η | 0.0003440 | Pa×s | 308.15 | Density... |
| η | 0.0003626 | Pa×s | 308.15 | Densiti... |
| η | 0.0003450 | Pa×s | 308.15 | Densiti... |
| η | 0.0003626 | Pa×s | 308.15 | Densiti... |
| η | 0.0003461 | Pa×s | 313.15 | Densiti... |
| η | 0.0002545 | Pa×s | 313.15 | Densiti... |
| η | 0.0003461 | Pa×s | 313.15 | Densiti... |
| η | 0.0003300 | Pa×s | 313.15 | Densiti... |
| η | 0.0003390 | Pa×s | 313.15 | Densiti... |
| η | 0.0003303 | Pa×s | 318.15 | Densiti... |
| η | 0.0003303 | Pa×s | 318.15 | Densiti... |
| η | 0.0003160 | Pa×s | 318.15 | Densiti... |
| η | 0.0003030 | Pa×s | 323.15 | Densiti... |
| η | 0.0003167 | Pa×s | 323.15 | Densiti... |
| η | 0.0003168 | Pa×s | 323.15 | Densiti... |
| ΔfusH | [8.38; 8.48] | kJ/mol | [186.10; 186.50] |
|
| ΔfusH | 8.48 | kJ/mol | 186.10 | NIST |
| ΔfusH | 8.38 | kJ/mol | 186.47 | NIST |
| ΔfusH | 8.44 | kJ/mol | 186.48 | NIST |
| ΔfusH | 8.44 | kJ/mol | 186.50 | NIST |
| ΔfusH | 8.44 | kJ/mol | 186.50 | NIST |
| ΔvapH | [30.00; 35.60] | kJ/mol | [310.00; 505.00] |
|
| ΔvapH | 35.60 | kJ/mol | 310.00 | NIST |
| ΔvapH | 33.80 ± 0.10 | kJ/mol | 314.00 | NIST |
| ΔvapH | 33.80 | kJ/mol | 315.00 | NIST |
| ΔvapH | 34.60 | kJ/mol | 318.00 | NIST |
| ΔvapH | 32.30 ± 0.10 | kJ/mol | 338.00 | NIST |
| ΔvapH | 33.90 | kJ/mol | 339.00 | NIST |
| ΔvapH | 33.90 | kJ/mol | 342.00 | NIST |
| ΔvapH | 31.30 ± 0.10 | kJ/mol | 352.00 | NIST |
| ΔvapH | 31.21 | kJ/mol | 352.60 | KDB |
| ΔvapH | 31.30 | kJ/mol | 352.80 | NIST |
| ΔvapH | 30.50 ± 0.10 | kJ/mol | 363.00 | NIST |
| ΔvapH | 30.00 ± 0.10 | kJ/mol | 370.00 | NIST |
| ΔvapH | 32.50 | kJ/mol | 378.00 | NIST |
| ΔvapH | 31.60 | kJ/mol | 438.00 | NIST |
| ΔvapH | 31.10 | kJ/mol | 505.00 | NIST |
| Pvap | [15.74; 101.30] | kPa | [303.15; 352.72] |
|
| Pvap | 15.74 | kPa | 303.15 | Density... |
| Pvap | 20.00 | kPa | 309.65 | Measure... |
| Pvap | 30.00 | kPa | 319.95 | Measure... |
| Pvap | 94.00 | kPa | 350.25 | Vapor L... |
| Pvap | 101.30 | kPa | 352.68 | Measure... |
| Pvap | 101.30 | kPa | 352.72 | Isobari... |
| Pvap | 101.30 | kPa | 352.72 | Isobari... |
| n0 | [1.36294; 1.38153] | [288.15; 323.15] |
|
|
| n0 | 1.38153 | 288.15 | Experim... | |
| n0 | 1.37870 | 293.15 | Solubil... | |
| n0 | 1.37900 | 293.15 | Solid-L... | |
| n0 | 1.37910 | 293.15 | Isother... | |
| n0 | 1.37879 | 293.15 | Mixing ... | |
| n0 | 1.37880 | 293.15 | Solubil... | |
| n0 | 1.37880 | 293.15 | Isother... | |
| n0 | 1.37879 | 293.15 | Thermod... | |
| n0 | 1.37892 | 293.15 | Experim... | |
| n0 | 1.37631 | 298.15 | Experim... | |
| n0 | 1.37700 | 298.15 | Excess ... | |
| n0 | 1.37618 | 298.15 | Ternary... | |
| n0 | 1.37930 | 298.15 | Isobari... | |
| n0 | 1.37618 | 298.15 | Mixing ... | |
| n0 | 1.37618 | 298.15 | Thermod... | |
| n0 | 1.37500 | 298.15 | Densiti... | |
| n0 | 1.37690 | 298.15 | (Vapor ... | |
| n0 | 1.37604 | 298.15 | Propert... | |
| n0 | 1.37614 | 298.15 | Isobari... | |
| n0 | 1.37623 | 298.15 | Vapor l... | |
| n0 | 1.37690 | 298.15 | Bubble-... | |
| n0 | 1.37623 | 298.15 | Densiti... | |
| n0 | 1.37610 | 298.15 | Isobari... | |
| n0 | 1.37355 | 303.15 | Thermod... | |
| n0 | 1.37366 | 303.15 | Experim... | |
| n0 | 1.37383 | 303.15 | Density... | |
| n0 | 1.37355 | 303.15 | Mixing ... | |
| n0 | 1.37000 | 308.15 | Densiti... | |
| n0 | 1.37102 | 308.15 | Experim... | |
| n0 | 1.36834 | 313.15 | Experim... | |
| n0 | 1.36570 | 318.15 | Densiti... | |
| n0 | 1.36565 | 318.15 | Experim... | |
| n0 | 1.36294 | 323.15 | Experim... | |
| ρl | [772.97; 810.33] | kg/m3 | [288.15; 323.15] |
|
| ρl | 810.33 | kg/m3 | 288.15 | Excess ... |
| ρl | 810.26 | kg/m3 | 288.15 | Volumet... |
| ρl | 805.00 | kg/m3 | 293.00 | KDB |
| ρl | 799.80 | kg/m3 | 293.15 | (Vapour... |
| ρl | 805.06 | kg/m3 | 293.15 | Thermod... |
| ρl | 805.06 | kg/m3 | 293.15 | Volumet... |
| ρl | 808.64 | kg/m3 | 293.15 | Volumet... |
| ρl | 804.90 | kg/m3 | 293.15 | Speed o... |
| ρl | 804.97 | kg/m3 | 293.15 | Speed o... |
| ρl | 805.17 | kg/m3 | 293.15 | Speed o... |
| ρl | 804.83 | kg/m3 | 293.15 | Speed o... |
| ρl | 799.94 | kg/m3 | 298.15 | Speed o... |
| ρl | 799.68 | kg/m3 | 298.15 | Speed o... |
| ρl | 799.74 | kg/m3 | 298.15 | Speed o... |
| ρl | 799.75 | kg/m3 | 298.15 | Excess ... |
| ρl | 802.03 | kg/m3 | 298.15 | Quatern... |
| ρl | 799.97 | kg/m3 | 298.15 | Thermod... |
| ρl | 799.97 | kg/m3 | 298.15 | Thermod... |
| ρl | 799.60 | kg/m3 | 298.15 | Volumet... |
| ρl | 800.30 | kg/m3 | 298.15 | Liquid-... |
| ρl | 799.78 | kg/m3 | 298.15 | Thermod... |
| ρl | 799.70 | kg/m3 | 298.15 | Isobari... |
| ρl | 799.97 | kg/m3 | 298.15 | Thermod... |
| ρl | 800.87 | kg/m3 | 298.15 | Experim... |
| ρl | 799.83 | kg/m3 | 298.15 | Volumet... |
| ρl | 799.62 | kg/m3 | 298.15 | Excess ... |
| ρl | 803.24 | kg/m3 | 298.15 | Volumet... |
| ρl | 799.97 | kg/m3 | 298.15 | Thermod... |
| ρl | 799.60 | kg/m3 | 298.15 | Speed o... |
| ρl | 794.67 | kg/m3 | 303.15 | Speed o... |
| ρl | 794.47 | kg/m3 | 303.15 | Speed o... |
| ρl | 794.41 | kg/m3 | 303.15 | Speed o... |
| ρl | 794.55 | kg/m3 | 303.15 | Thermod... |
| ρl | 794.63 | kg/m3 | 303.15 | Excess ... |
| ρl | 794.60 | kg/m3 | 303.15 | Viscome... |
| ρl | 802.50 | kg/m3 | 303.15 | Effect ... |
| ρl | 799.71 | kg/m3 | 303.15 | Excess ... |
| ρl | 797.88 | kg/m3 | 303.15 | Volumet... |
| ρl | 794.50 | kg/m3 | 303.15 | Excess ... |
| ρl | 794.60 | kg/m3 | 303.15 | Volumet... |
| ρl | 799.69 | kg/m3 | 303.15 | Studies... |
| ρl | 794.57 | kg/m3 | 303.15 | Volumet... |
| ρl | 794.33 | kg/m3 | 303.15 | Speed o... |
| ρl | 789.38 | kg/m3 | 308.15 | Speed o... |
| ρl | 789.12 | kg/m3 | 308.15 | Speed o... |
| ρl | 789.18 | kg/m3 | 308.15 | Speed o... |
| ρl | 789.27 | kg/m3 | 308.15 | Volumet... |
| ρl | 792.45 | kg/m3 | 308.15 | Volumet... |
| ρl | 800.10 | kg/m3 | 308.15 | Effect ... |
| ρl | 789.04 | kg/m3 | 308.15 | Speed o... |
| ρl | 783.85 | kg/m3 | 313.15 | Speed o... |
| ρl | 783.80 | kg/m3 | 313.15 | Speed o... |
| ρl | 784.01 | kg/m3 | 313.15 | Excess ... |
| ρl | 784.00 | kg/m3 | 313.15 | Volumet... |
| ρl | 800.30 | kg/m3 | 313.15 | Effect ... |
| ρl | 784.00 | kg/m3 | 313.15 | Viscome... |
| ρl | 783.95 | kg/m3 | 313.15 | Volumet... |
| ρl | 786.94 | kg/m3 | 313.15 | Volumet... |
| ρl | 783.72 | kg/m3 | 313.15 | Speed o... |
| ρl | 778.44 | kg/m3 | 318.15 | Speed o... |
| ρl | 778.48 | kg/m3 | 318.15 | Speed o... |
| ρl | 778.36 | kg/m3 | 318.15 | Speed o... |
| ρl | 773.04 | kg/m3 | 323.15 | Speed o... |
| ρl | 773.09 | kg/m3 | 323.15 | Speed o... |
| ρl | 773.30 | kg/m3 | 323.15 | Viscome... |
| ρl | 773.30 | kg/m3 | 323.15 | Volumet... |
| ρl | 772.97 | kg/m3 | 323.15 | Speed o... |
| ΔfusS | [44.98; 45.59] | J/mol×K | [186.10; 186.48] |
|
| ΔfusS | 45.59 | J/mol×K | 186.10 | NIST |
| ΔfusS | 44.98 | J/mol×K | 186.47 | NIST |
| ΔfusS | 45.25 | J/mol×K | 186.48 | NIST |
| csound,fluid | [1136.00; 1212.30] | m/s | [293.15; 313.15] |
|
| csound,fluid | 1212.30 | m/s | 293.15 | Thermod... |
| csound,fluid | 1212.00 | m/s | 293.15 | Thermod... |
| csound,fluid | 1192.00 | m/s | 298.15 | Vapor l... |
| csound,fluid | 1191.00 | m/s | 298.15 | Thermod... |
| csound,fluid | 1190.80 | m/s | 298.15 | Thermod... |
| csound,fluid | 1170.80 | m/s | 303.15 | Thermod... |
| csound,fluid | 1170.60 | m/s | 303.15 | Thermod... |
| csound,fluid | 1178.00 | m/s | 303.15 | Densiti... |
| csound,fluid | 1158.00 | m/s | 308.15 | Densiti... |
| csound,fluid | 1136.00 | m/s | 313.15 | Densiti... |
| γ | [0.02; 0.02] | N/m | [298.15; 298.20] |
|
| γ | 0.02 | N/m | 298.15 | Concent... |
| γ | 0.02 | N/m | 298.20 | KDB |
| λ | [0.13; 0.15] | W/m×K | [284.48; 374.56] |
|
| λ | 0.15 | W/m×K | 284.48 | Thermal... |
| λ | 0.15 | W/m×K | 294.42 | Thermal... |
| λ | 0.15 | W/m×K | 305.02 | Thermal... |
| λ | 0.14 | W/m×K | 314.26 | Thermal... |
| λ | 0.14 | W/m×K | 323.96 | Thermal... |
| λ | 0.14 | W/m×K | 334.71 | Thermal... |
| λ | 0.14 | W/m×K | 344.54 | Thermal... |
| λ | 0.13 | W/m×K | 354.33 | Thermal... |
| λ | 0.13 | W/m×K | 364.46 | Thermal... |
| λ | 0.13 | W/m×K | 374.56 | Thermal... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 308.15 | 101.30 | 0.0003 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.68] | kPa | [259.76; 376.05] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45436e+01 | |||
| Coefficient B | -3.04648e+03 | |||
| Coefficient C | -4.60570e+01 | |||
| Temperature range, min. | 259.76 | |||
| Temperature range, max. | 376.05 | |||
| Pvap | 1.33 | kPa | 259.76 | Calculated Property |
| Pvap | 3.01 | kPa | 272.68 | Calculated Property |
| Pvap | 6.21 | kPa | 285.60 | Calculated Property |
| Pvap | 11.90 | kPa | 298.52 | Calculated Property |
| Pvap | 21.42 | kPa | 311.44 | Calculated Property |
| Pvap | 36.49 | kPa | 324.37 | Calculated Property |
| Pvap | 59.31 | kPa | 337.29 | Calculated Property |
| Pvap | 92.50 | kPa | 350.21 | Calculated Property |
| Pvap | 139.13 | kPa | 363.13 | Calculated Property |
| Pvap | 202.68 | kPa | 376.05 | Calculated Property |
| Pvap | [1.45e-03; 4143.73] | kPa | [186.48; 535.50] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.69787e+01 | |||
| Coefficient B | -6.16017e+03 | |||
| Coefficient C | -7.78365e+00 | |||
| Coefficient D | 6.13927e-06 | |||
| Temperature range, min. | 186.48 | |||
| Temperature range, max. | 535.50 | |||
| Pvap | 1.45e-03 | kPa | 186.48 | Calculated Property |
| Pvap | 0.11 | kPa | 225.26 | Calculated Property |
| Pvap | 1.96 | kPa | 264.04 | Calculated Property |
| Pvap | 15.33 | kPa | 302.82 | Calculated Property |
| Pvap | 70.44 | kPa | 341.60 | Calculated Property |
| Pvap | 227.74 | kPa | 380.38 | Calculated Property |
| Pvap | 578.94 | kPa | 419.16 | Calculated Property |
| Pvap | 1243.69 | kPa | 457.94 | Calculated Property |
| Pvap | 2369.94 | kPa | 496.72 | Calculated Property |
| Pvap | 4143.73 | kPa | 535.50 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Butanone.
Mixtures
- Diethyl carbonate + 2-Butanone
- 2-Butanone + Benzene, 1,3-dichloro-
- 1-Propanol + 2-Butanone + Benzene, 1,3-dichloro-
- 2-Butanone + 1-Butanol + Benzene, 1,3-dichloro-
- 2-Butanone + Benzene, 1,3-dichloro- + 1-Pentanol
- 2-Butanone + Benzene, 1,3-dichloro- + 1-Hexanol
- 2-Butanone + Formamide, N,N-dimethyl-
- 2-Butanone + Ethanol
- 2-Butanone + Pentane, 2,2,4-trimethyl-
- 2-Butanone + Ethanol + Pentane, 2,2,4-trimethyl-
- 1-Propanol + 2-Butanone
- 2-Butanone + Isopropyl Alcohol
- n-Hexane + 2-Butanone
- 2-Butanone + Heptane
- 2-Butanone + 1-Propanamine, N-propyl-
- 2-Butanone + 1-Butanamine, N-butyl-
- 2-Butanone + Triethylamine
- 2-Butanone + Methylphosphonic acid
- 2-Butanone + Propanoic acid, 2-hydroxy-, ethyl ester
- 2-Butanone + Tetrahydrofuran
Find more mixtures with 2-Butanone.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- A relative headspace method for Henry s constants of volatile organic compounds
- Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
- Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
- Experimental isobaric vapour liquid liquid equilibrium data for the quaternary systems water (1) ethanol (2) acetone (3) n-butyl acetate (4) and water (1) ethanol (2) acetone (3) methyl ethyl ketone (4) and their partially miscible-constituent ternaries
- (Vapor + liquid) equilibrium of binary mixtures formed by N,N-dimethyl formamide with some compounds at 95.1 kPa
- Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
- 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)
- Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
- Effect of temperature on ultrasonic velocity and thermodynamic parameters of bisphenol-C-formaldehyde-acrylate resin solutions
- Isobaric vapour liquid equilibria for binary systems of 2-butanone with ethanol, 1-propanol, and 2-propanol at 20 and 101.3 kPa
- Investigation on isobaric vapor liquid equilibrium for acetic acid +water +methyl ethyl ketone + isopropyl acetate
- Compact apparatus for rapid measurement of high-pressure phase equilibria of carbon dioxide expanded liquids
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
- Solubility of lansoprazole in different solvents
- Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
- Thermodynamics of ketone + amine mixtures. Part X. Excess molarenthalpies at 298.15 K for N,N,N-triethylamine + 2-alkanone systems.Characterization of tertiary amine + 2-alkanone, and ofamino-ketone + n-alkane mixtures in terms of DISQUAC
- Liquid-liquid equilibria for the pseudo-ternary system {aqueous sulfuric acid solution + methyl ethyl ketone or methyl isopropyl ketone + phosphonium-based ionic liquids} at 298.15 K and atmospheric pressure
- Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
- Measurement and correlation of the solubilities of tetra(5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy) neopentane in different pure solvents
- 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
- Solubility of methylphosphonic acid in selected organic solvents
- Experimental measurements and modelling of volumetric properties, refractive index and viscosity of binary systems of ethyl lactate with methyl ethyl ketone, toluene and n-methyl-2-pirrolidone at 288.15 323.15 K and atmospheric pressure. New UNIFAC VISCO and ASOG VISCO interaction parameters
- Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
- Densities, viscosities and refractive indices of binary mixtures containing methyl ethyl ketone. Friction theory. New UNIFAC-VISCO and ASOG-VISCO parameter determination
- Isobaric vapor-liquid equilibrium for methanol + methyl ethyl ketone + bis(trifluoromethylsulfonyl)imide-based ionic liquids at 101.3 kPa
- The solubility of maleic acid in various inorganic salts and organic solvents: Thermodynamics model and parameters
- Isobaric vapor-liquid equilibrium for 2-butanone + ethanol + phosphate-based ionic liquids at 101.3 kPa
- Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
- Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
- Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
- 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
- Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
- Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
- Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
- (Vapour + liquid) equilibria for (2-ethoxypropene + acetone) and (2-ethoxypropene + butanone)
- Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ketones at T = 298.15 K
- Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
- Mixing properties of binary mixtures presenting azeotropes at several temperatures
- Excess enthalpies and (vapour + liquid) equilibrium data for the binary mixtures of dimethylsulphoxide with ketones
- Density, viscosity, refractive index, excess molar enthalpy, viscosity, and refractive index deviations for the (1-butanol + 2-butanone) binary system at T = 303 K. A new adiabatic calorimeter for heat of mixing
- Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
- Measurement and correlation of (liquid + liquid) equilibrium of the azeotrope (cyclohexane + 2-butanone) with different ionic liquids at T = 298.15 K
- Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
- Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
- Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
- A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Combined effects of salinity and temperature on the solubility of organic compounds
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
- Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Measurement and correlation of solubility of dodecanedioic acid in different pure solvents from T = (288.15 to 323.15) K
- Thermodynamics of (ketone + amine) mixtures. Part XI. Excess molar enthalpies at T = 298.15 K for the (1-propanol + N,N,N-triethylamine + 2-butanone) system
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
- Volumetric and optical properties for some (2-butanone + chloroalkane) binary mixtures at T = 298.15 K
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Isobaric (vapor + liquid) equilibria for the binary systems (1-methoxy-2- propanol + 2-methoxyethanol), (2-butanone + 2-methoxyethanol) and (water + 2-methoxyethanol) at pressures of (74.5, 101.3, and 134.0) kPa
- Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
- Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
- Phase equilibria of the ternary systems of (water + diethyl carbonate) with acetone, or 2-butanone at four temperatures
- Thermodynamic study of the solubility of 2,4'-dihydroxydiphenyl sulfone in nine organic solvents from T = (278.15 to 313.15) K and thermodynamic properties of dissolution
- Solubility determination and thermodynamic modelling of terephthaldialdehyde in ten organic solvents from T = (273.15 to 318.15) K and mixing properties of solutions
- Measurement and modelling of econazole nitrate in twelve pure organic solvents at temperatures from 278.15 K to 318.15 K
- Solubility measurement and correlation of the form A of ibrutinib in organic solvents from 278.15 to 323.15 K
- Thermodynamic modelling for solubility of 4-nitrobenzaldehyde in different solvents at temperature range from (273.15 to 313.15) K and mixing properties of solutions
- Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
- Solubility measurement, model evaluation and thermodynamic analysis of rivaroxaban polymorphs in organic solvents
- Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
- Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
- Solubility determination and modelling of 4-nitro-1,2-phenylenediamine in eleven organic solvents from T = (283.15 to 318.15) K and thermodynamic properties of solutions
- Solubility determination and thermodynamic functions of 2-chlorophenothiazine in nine organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
- Solubility and thermodynamic functions of tebuconazole in nine organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Solubility of 2-isopropylimidazole in nine pure organic solvents and liquid mixture of (methanol + ethyl acetate) from T = (278.15 to 313.15) K: Experimental measurement and thermodynamic modelling
- Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Thermodynamic functions for solubility of 3-nitro-o-toluic acid in nine organic solvents from T = (283.15 to 318.15) K and apparent thermodynamic properties of solutions
- Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
- Thermodynamic functions for solubility of 2-mercaptobenzothiazole in eleven pure organic solvents at temperatures from 273.15 K to 318.15 K and mixing properties of solutions
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
- Molar excess enthalpies of ethyl acetate + alkanols at T=298.15K, p=10MPa
- Thermodynamics of ketone + amine mixtures Part IV. Volumetric and speed of sound data at (293.15; 298.15 and 303.15 K) for 2-butanone +dipropylamine, +dibutylamine or +triethylamine systems
- Experimental Determination and Modeling of Densities, Refractive Indices of the Binary Mixtures of Dimethylphthalate (or Dimethyladipate) + 1-Butanol, or + 2-Butanol, or + 2-Butanone at T = (288.15 to 323.15) K
- Excess molar volumes of (1-chlorobutane +heptane + 2-butanone or 2-pentanone) at 288.15 , 303.15 and 313.15 K . Measurements and correlations.
- Densities and viscosities of binary mixtures of ethylmethylketone and 2-alkanols; application of the ERAS model and cubic EOS
- Volumetric properties of binary liquid mixtures of ketones with chloroalkanes at different temperatures and atmospheric pressure
- Isobaric Vapor Liquid Equilibrium for the Binary Systems of sec-Butyl Acetate + Methyl Ethyl Ketone, 2-Methoxyethanol, or 1,2-Dimethoxyethane at 101.3 kPa
- Solubility of Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
- Vapor Liquid Equilibria Measurements for the Five Linear C6 Esters with n-Octane
- Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
- 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
- Solubility Measurement and Correlation of Two Erlotinib Hydrochloride Polymorphs in Alcohols and Ketones from 273.15 to 323.15 K
- Experimental and Modeling Studies on the Solubility of 2-Chloro-N-(4-methylphenyl)propanamide (S1) in Binary Ethyl Acetate + Hexane, Toluene + Hexane, Acetone + Hexane, and Butanone + Hexane Solvent Mixtures Using Polythermal Method
- Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
- Solubility Modeling and Mixing Thermodynamics of Thiamphenicol in Water and Twelve Neat Organic Solvents from T = (278.15 to 318.15) K
- Extraction of Citric Acid and Maleic Acid from Their Aqueous Solutions Using a Phosphorus-Bonded Extractant, Tri-n-octylphosphineoxide, and a Secondary Amine, Dioctylamine
- Isobaric Vapor-Liquid Equilibrium for 2-Butanone + Ethanol System Containing Different Ionic Liquids at 101.3 kPa
- Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
- Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
- Solubility and Molecular Interactions of Trimetazidine Hydrochloride in 12 Monosolvents and Solvent Mixtures of Methanol + (Ethanol, N,N-Dimethylformamide or Ethyl Acetate)
- Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
- Isothermal Vapor-Liquid Equilibrium Measurements of Butan-2-one + 2-Methyl-propan-1-ol/Pentan-1-ol
- Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
- Measurement and Correlation of Solubility and Thermodynamic Properties of Vinpocetine in Nine Pure Solvents and (Ethanol + Water) Binary Solvent
- Measurement and Correlation of Solubility of Gatifloxacin in 12 Pure Solvents from 273.15 K to 318.15 K
- Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
- Solubility Modeling and Solvent Effect of 2-Amino-6-chloropurine in Twelve Neat Solvents
- Solubility in Different Solvents, Correlation, and Solvent Effect in the Solvent Crystallization Process of Iohexol
- Solubility Modeling and Solvent Effect for Flubendazole in 12 Neat Solvents
- Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
- Solid-Liquid Equilibrium Measurements for Posaconazole and Voriconazole in Several Solvents between T = 278.2 and 323.2 K Using Differential Thermal Analysis/Thermal Gravimetric Analysis
- Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
- o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Solubility Determination and Thermodynamic Mixing Properties of 5-Methyl-2-pyrazinecarboxylic Acid in Different Solvents
- Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
- Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
- Solubility Data for Roflumilast and Maraviroc in Various Solvents between T = (278.2-323.2) K
- Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
- Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
- Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
- Measurement of Henry s Law Constants for Acetone, 2-Butanone, 2,3-Butanedione, and Isobutyraldehyde Using a Horizontal Flow Reactor
- Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
- Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
- 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
- Densities and Viscosities for Binary and Ternary Mixtures of Ethanol, 2-Butanone, and 2,2,4-Trimethylpentane at T = (298.15, 308.15, and 318.15) K
- Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
- Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 2-Butanone at 298.15 K
- Thermal Conductivity of Some Oxygenated Fuels and Additives in the Saturated Liquid Phase
- Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
- Solubilities of Proxetine Hydrochloride Hemihydrate between 286 K and 363 K
- Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
- Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
- Excess Molar Volumes and Viscosity Deviations of Binary Liquid Mixtures of 1,3-Dioxolane and 1,4-Dioxane with Butyl Acetate, Butyric Acid, Butylamine, and 2-Butanone at 298.15 K
- Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
- Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
- Density, Viscosity, Vapor-Liquid Equilibrium, Excess Molar Volume, Viscosity Deviation, and Their Correlations for the Chloroform + 2-Butanone Binary System
- Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
- Measurement and Correlation of Griseofulvin Solubility in Different Solvents at Temperatures from (281.95 to 357.60) K
- Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
- Solubilities of Phosphorus-Containing Compounds in Selected Solvents
- Liquid-Liquid and Vapor-Liquid-Liquid Equilibrium of the 2-Butanone + 2-Butanol + Water System
- Thermodynamics of Ketone + Amine Mixtures. Part III. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Butanone + Aniline, + N-Methylaniline, or + Pyridine Systems
- Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
- Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Different Organic Solvents
- Solubility of Candesartan Cilexetil in Different Solvents at Various Temperatures
- Viscometric Behavior of Binary Mixtures of Butan-2-one with Benzene at T = (303.15, 313.15, and 323.15) K
- Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
- Densities and Viscosities of the Binary Mixtures of Phenylmethanol with 2-Butanone
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- 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
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Effect of Ionic Liquids on the Isobaric Vapor-Liquid equilibrium behavior of methanol-methyl ethyl ketone (MEK)
- Solubility of Veratric Acid in Eight Monosolvents and Ethanol + 1-Butanol at Various Temperatures
- Isothermal Vapor Liquid Equilibrium Data for the Butan-2-one + Methanol or Ethanol Systems Using a Static-Analytic Microcell
- 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
- Speed of sound, density and related thermodynamic excess properties of binary mixtures of butan-2-one with C1-C4 nalkanols and chloroform
- Densities, Viscosities and Refractive Indices of the Ternary Mixture Dimethyladipate + 2-Butanone + 1-Butanol at T = (288.15 to 323.15) K
- Ternary Liquid-Liquid Equilibria Ethanol + 2-Butanone + 1-Butyl-3-methylimidazolium Hexafluorophosphate, 2-Propanol + 2-Butanone + 1-Butyl-3-methylimidazolium Hexafluorophosphate, and 2-Butanone + 2-Propanol + 1,3-Dimethylimidazolium Methyl Sulfate at 298.15 K
- Solubility of Imidacloprid in Different Solvents
- Isobaric Vapor Liquid Equilibria for Binary Systems of Acetone + Isopropenyl Acetate, 2-Butanone + Isopropenyl Acetate, and Isopropenyl Acetate + Acetylacetone at 101.3 kPa
- Solubility of Lovastatin in Ethyl Acetate, Propyl Acetate, Isopropyl Acetate, Butyl Acetate, sec-Butyl Acetate, Isobutyl Acetate, tert-Butyl Acetate, and 2-Butanone, between (285 and 313) K
- Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
- Volumetric and Transport Properties of Binary Liquid Mixtures of Aliphatic Ketones with Phenylacetonitrile at T = 308.15 K
- Densities and Viscosities of Binary Liquid Mixtures of 2-Butanone with Branched Alcohols at (293.15 to 313.15) K
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
- 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
- Excess Molar Enthalpies and Vapor-Liquid Equilibrium for N-Methyl-2-pyrrolidone with Ketones
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol and 2-Propanol with 2-Butanone and Butyl Propionate at 101.3 kPa
- Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
- Excess Enthalpies of Dibromomethane with Acetone, 1,4-Dioxane, Pyridine, Diethyl Ether, Ethyl Methyl Ketone, and Tetrahydrofuran at 303.15 K
- Solubility of 1,1'-(Ethane-1,2-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents
- Solubilities of 1,1?-(Propane-1,3-diyl)-bis(3-methyl-1H-imidazolium-1-yl) Dihexafluorophosphate in Different Solvents
- Solubility of 1,1'-(Butane-1,4-diyl)-bis(3-methyl-1H-imidazolium-1-yl) Dihexafluorophosphate in Water, Acetophenone, Cyclohexanone, Acetylacetone, and 2-Butanone
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Methyl Ethyl Ketone + Pentanol Isomers at Different Temperatures
- Solubility of 1,1'-(Butane-1,4-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents from (288.15 to 333.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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