- 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
- Butanone 2
- C2H5COCH3
- Ethyl methyl cetone
- Ethylmethylketon
- Ketone, ethyl methyl
- Ketone, methyl ethyl
- MEK
- Meetco
- Methyl acetone
- Metiletilchetone
- Metyloetyloketon
- Rcra waste number U159
- UN 1193
- butan-2-one
- butanone
- ethyl methyl ketone
- methyl ethyl ketone
- 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).
- εr : Dielectric Constant (Relative permittivity).
- 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.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- pKa : Log10 of Acid Dissociation Constant.
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : 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).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- 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; 0.3290] |
|
|
| ω | 0.3290 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.3220 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.3200 | KDB | |
| PAff | 827.30 | kJ/mol | NIST |
| Tig | [677.15; 789.26] | K |
|
| Tig | 789.26 | K | KDB |
| Tig | 677.15 | K | NCMS SOLV-DB |
| 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 | [2.76; 3.30] | debye |
|
| μ | 2.76 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 3.30 | debye | KDB |
| η | [0.0003730; 0.0004011] | Pa×s |
|
| η | 0.0003880 | Pa×s | A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents |
| η | 0.0004011 | Pa×s | Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents |
| η | 0.0003760 | Pa×s | 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 |
| η | 0.0003730 | Pa×s | 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 |
| EA | 9.99e-04 | eV | NIST |
| εr | 18.51 | NCMS SOLV-DB | |
| LFL | 1.80 | % in Air | KDB |
| UFL | 11.50 | % in Air | KDB |
| Tflash,cc | [264.15; 267.59] | K |
|
| Tflash,cc | 267.59 | K | KDB |
| Tflash,cc | 264.15 | K | NCMS SOLV-DB |
| Tflash,oc | 266.48 | K | KDB |
| ΔfG° | [-147.00; -146.20] | kJ/mol |
|
| ΔfG° | -147.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -146.20 | kJ/mol | KDB |
| ΔfH°gas | [-239.00; -238.10] | kJ/mol |
|
| ΔfH°gas | -239.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| 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° | 7.72 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [32.00; 35.51] | kJ/mol |
|
| ΔvapH° | 34.52 | kJ/mol | NCMS SOLV-DB |
| 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. Solubility Prediction | |
| log10WS | 0.52 | Estimated Solubility | |
| logPoct/wat | 0.290 | NCMS SOLV-DB | |
| McVol | 68.790 | ml/mol | McGowan Calculated Property |
| NFPA Fire | [%!d(float64=3); %!d(float64=3)] |
|
|
| NFPA Fire | 3 | KDB | |
| NFPA Fire | 3 | NCMS SOLV-DB | |
| NFPA Health | [%!d(float64=1); %!d(float64=1)] |
|
|
| NFPA Health | 1 | KDB | |
| NFPA Health | 1 | NCMS SOLV-DB | |
| NFPA Safety | 0 | NCMS SOLV-DB | |
| Pc | [3998.00; 4390.00] | kPa |
|
| Pc | 4207.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 4154.32 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4210.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| 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 | Outlier 3998.00 ± 202.65 | kPa | NIST |
| Pc | Outlier 4390.00 ± 202.65 | kPa | NIST |
| pKa | 14.70 | NCMS SOLV-DB | |
| Ptriple | 1.39e-03 | kPa | ChemSep v8.3 pure component data Compiled value |
| 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 | Outlier 622.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 572.00 | NIST | |
| Inp | 575.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 573.00 | 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 | |
| Ip | [866.00; 953.00] |
|
|
| Ip | 917.39 | NIST | |
| Ip | 922.33 | NIST | |
| Ip | 925.59 | NIST | |
| Ip | 928.27 | NIST | |
| Ip | 931.34 | NIST | |
| Ip | 935.77 | NIST | |
| Ip | 940.31 | NIST | |
| Ip | 943.44 | NIST | |
| Ip | Outlier 946.71 | NIST | |
| Ip | Outlier 949.95 | NIST | |
| Ip | 937.60 | NIST | |
| Ip | 938.60 | NIST | |
| Ip | Outlier 947.76 | NIST | |
| Ip | 932.30 | NIST | |
| Ip | 919.80 | NIST | |
| Ip | 923.70 | NIST | |
| Ip | 927.80 | NIST | |
| Ip | 919.00 | NIST | |
| Ip | 930.00 | NIST | |
| Ip | 905.00 | NIST | |
| Ip | 881.00 | NIST | |
| Ip | 900.00 | NIST | |
| Ip | 900.00 | NIST | |
| Ip | 893.00 | NIST | |
| Ip | 908.00 | NIST | |
| Ip | 891.00 | NIST | |
| Ip | 923.30 | NIST | |
| Ip | 897.00 | NIST | |
| Ip | 903.00 | NIST | |
| Ip | 905.00 | NIST | |
| Ip | 926.00 | NIST | |
| Ip | 912.70 | NIST | |
| Ip | 885.00 | NIST | |
| Ip | 915.00 | NIST | |
| Ip | 894.00 | NIST | |
| Ip | 908.00 | NIST | |
| Ip | 888.00 | NIST | |
| Ip | 875.00 | NIST | |
| Ip | 905.00 | NIST | |
| Ip | 900.00 | NIST | |
| Ip | 893.00 | NIST | |
| Ip | 882.00 | NIST | |
| Ip | 905.00 | NIST | |
| Ip | 901.00 | NIST | |
| Ip | 907.00 | NIST | |
| Ip | 905.00 | NIST | |
| Ip | 908.00 | NIST | |
| Ip | 903.00 | NIST | |
| Ip | 904.00 | NIST | |
| Ip | 882.00 | NIST | |
| Ip | 924.00 | NIST | |
| Ip | 914.00 | NIST | |
| Ip | 908.00 | NIST | |
| Ip | 918.00 | NIST | |
| Ip | 893.00 | NIST | |
| Ip | 906.00 | NIST | |
| Ip | 906.00 | NIST | |
| Ip | 906.00 | NIST | |
| Ip | 918.00 | NIST | |
| Ip | 945.00 | NIST | |
| Ip | 920.00 | NIST | |
| Ip | 907.00 | NIST | |
| Ip | 899.00 | NIST | |
| Ip | 901.00 | NIST | |
| Ip | 914.00 | NIST | |
| Ip | 888.00 | NIST | |
| Ip | Outlier 866.00 | NIST | |
| Ip | 901.00 | NIST | |
| Ip | Outlier 866.00 | NIST | |
| Ip | Outlier 866.00 | NIST | |
| Ip | 906.00 | NIST | |
| Ip | 912.00 | NIST | |
| Ip | 890.00 | NIST | |
| Ip | 923.00 | NIST | |
| Ip | 911.00 | NIST | |
| Ip | Outlier 953.00 | NIST | |
| Ip | 912.00 | NIST | |
| Ip | 888.00 | NIST | |
| Ip | 888.00 | NIST | |
| Ip | 889.00 | NIST | |
| Ip | 903.00 | NIST | |
| Ip | 910.00 | NIST | |
| Ip | 894.00 | NIST | |
| Ip | 906.00 | NIST | |
| Ip | 909.00 | NIST | |
| Ip | 882.00 | NIST | |
| Ip | 901.00 | NIST | |
| Ip | 907.00 | NIST | |
| Ip | 909.00 | NIST | |
| Ip | 908.00 | NIST | |
| Ip | 894.00 | NIST | |
| Ip | 875.00 | NIST | |
| Ip | 881.00 | NIST | |
| Ip | 920.00 | NIST | |
| Ip | 904.00 | NIST | |
| Ip | 908.00 | NIST | |
| Ip | 908.00 | NIST | |
| Ip | 908.00 | NIST | |
| Ip | 930.00 | NIST | |
| Ip | 908.00 | NIST | |
| Ip | 917.39 | NIST | |
| Ip | 935.77 | NIST | |
| Ip | 937.60 | NIST | |
| Ip | 923.70 | NIST | |
| Ip | 891.00 | NIST | |
| Ip | 924.00 | NIST | |
| Ip | 914.00 | NIST | |
| Ip | 906.00 | NIST | |
| Ip | 907.00 | NIST | |
| Ip | Outlier 866.00 | NIST | |
| Ip | 912.00 | NIST | |
| Ip | 905.00 | NIST | |
| Ip | 903.00 | NIST | |
| Ip | 897.00 | NIST | |
| Ip | 885.00 | NIST | |
| Ip | 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 | 352.85 | K | Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K |
| Tboil | 352.68 | K | Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures |
| Tboil | 352.72 | K | Isobaric vapor-liquid equilibrium for 2-butanone + ethanol + phosphate-based ionic liquids at 101.3 kPa |
| Tboil | 352.69 | K | Excess enthalpies and (vapour + liquid) equilibrium data for the binary mixtures of dimethylsulphoxide with ketones |
| Tboil | 352.72 | K | Isobaric Vapor-Liquid Equilibrium for 2-Butanone + Ethanol System Containing Different Ionic Liquids at 101.3 kPa |
| Tboil | 352.78 | 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 |
| Tboil | 352.68 | K | Liquid-Liquid and Vapor-Liquid-Liquid Equilibrium of the 2-Butanone + 2-Butanol + Water System |
| Tboil | 352.71 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 352.74 | K | KDB |
| Tboil | 352.75 | K | NCMS SOLV-DB |
| 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 | Outlier 351.15 ± 2.00 | K | NIST |
| Tboil | 352.70 ± 0.30 | K | NIST |
| Tboil | 352.95 ± 1.00 | K | NIST |
| Tboil | Outlier 354.00 ± 2.00 | K | NIST |
| Tboil | Outlier 354.00 ± 2.00 | K | NIST |
| Tboil | 352.65 ± 2.00 | K | NIST |
| Tboil | 352.75 ± 0.25 | K | NIST |
| Tboil | Outlier 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 | Outlier 351.15 ± 4.00 | K | NIST |
| Tboil | Outlier 354.15 ± 2.00 | K | NIST |
| Tc | [533.00; 536.80] | K |
|
| Tc | 536.70 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 535.60 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 536.80 | K | ChemSep v8.3 pure component data Compiled value |
| 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; 187.15] | K |
|
| Tfus | 186.35 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 186.48 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 186.48 | K | KDB |
| Tfus | 186.50 | K | Aq. Solubility Prediction |
| Tfus | Outlier 187.15 | K | NCMS SOLV-DB |
| 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 | 186.48 | K | ChemSep v8.3 pure component data Compiled value |
| 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 |
| 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 |
| UQi | 2.88 | ChemSep v8.3 pure component data Compiled value | |
| URi | 3.25 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.267; 0.267] | m3/kmol |
|
| Vc | 0.267 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Vc | 0.267 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.267 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.267 | m3/kmol | KDB |
| Zc | [0.2516810; 0.2520000] |
|
|
| Zc | 0.2520000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value | |
| Zc | 0.2520000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2516810 | KDB |
Temperature Dependent Properties
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 |
|---|---|---|---|---|
| Cp,gas | [74.68; 247.74] | J/mol×K | [150.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 6.94040e+01 | |||
| Coefficient B | -5.45040e+02 | |||
| Coefficient C | 5.23124e+00 | |||
| Coefficient D | 4.55780e-04 | |||
| Coefficient E | -1.63510e-07 | |||
| Temperature range, min. | 150.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 74.68 | J/mol×K | 150.00 | Calculated Property |
| Cp,gas | 103.75 | J/mol×K | 300.00 | Calculated Property |
| Cp,gas | 135.56 | J/mol×K | 450.00 | Calculated Property |
| Cp,gas | 162.86 | J/mol×K | 600.00 | Calculated Property |
| Cp,gas | 185.50 | J/mol×K | 750.00 | Calculated Property |
| Cp,gas | 204.15 | J/mol×K | 900.00 | Calculated Property |
| Cp,gas | 219.38 | J/mol×K | 1050.00 | Calculated Property |
| Cp,gas | 231.55 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | 240.94 | J/mol×K | 1350.00 | Calculated Property |
| Cp,gas | 247.74 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [149.24; 174.98] | J/mol×K | [180.00; 373.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.37210e+02 | |||
| Coefficient B | 2.45980e+02 | |||
| Coefficient C | -5.82855e-01 | |||
| Coefficient D | 9.40400e-03 | |||
| Coefficient E | 3.31430e-07 | |||
| Temperature range, min. | 180.00 | |||
| Temperature range, max. | 373.15 | |||
| Cp,liquid | 149.24 | J/mol×K | 180.00 | Calculated Property |
| Cp,liquid | 149.97 | J/mol×K | 201.46 | Calculated Property |
| Cp,liquid | 151.13 | J/mol×K | 222.92 | Calculated Property |
| Cp,liquid | 152.72 | J/mol×K | 244.38 | Calculated Property |
| Cp,liquid | 154.77 | J/mol×K | 265.84 | Calculated Property |
| Cp,liquid | 157.35 | J/mol×K | 287.31 | Calculated Property |
| Cp,liquid | 160.52 | J/mol×K | 308.77 | Calculated Property |
| Cp,liquid | 164.42 | J/mol×K | 330.23 | Calculated Property |
| Cp,liquid | 169.18 | J/mol×K | 351.69 | Calculated Property |
| Cp,liquid | 174.98 | J/mol×K | 373.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0022590; 0.0000757] | Pa×s | [186.48; 535.50] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -6.05190e-01 | |||
| Coefficient B | 5.03020e+02 | |||
| Coefficient C | -1.56590e+00 | |||
| Coefficient D | 5.57820e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 186.48 | |||
| Temperature range, max. | 535.50 | |||
| η | 0.0022590 | Pa×s | 186.48 | Calculated Property |
| η | 0.0010572 | Pa×s | 225.26 | Calculated Property |
| η | 0.0005945 | Pa×s | 264.04 | Calculated Property |
| η | 0.0003763 | Pa×s | 302.82 | Calculated Property |
| η | 0.0002584 | Pa×s | 341.60 | Calculated Property |
| η | 0.0001882 | Pa×s | 380.38 | Calculated Property |
| η | 0.0001433 | Pa×s | 419.16 | Calculated Property |
| η | 0.0001129 | Pa×s | 457.94 | Calculated Property |
| η | 0.0000914 | Pa×s | 496.72 | Calculated Property |
| η | 0.0000757 | Pa×s | 535.50 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [39.96; 4.82] | kJ/mol | [186.48; 535.50] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 4.72210e+01 | |||
| Coefficient B | 3.07590e-01 | |||
| Coefficient C | 4.85910e-01 | |||
| Coefficient D | -8.64500e-01 | |||
| Coefficient E | 4.50180e-01 | |||
| Critical temperature, Tc (K) | 5.36800e+02 | |||
| Temperature range, min. | 186.48 | |||
| Temperature range, max. | 535.50 | |||
| ΔvapH | 39.96 | kJ/mol | 186.48 | Calculated Property |
| ΔvapH | 38.14 | kJ/mol | 225.26 | Calculated Property |
| ΔvapH | 36.24 | kJ/mol | 264.04 | Calculated Property |
| ΔvapH | 34.23 | kJ/mol | 302.82 | Calculated Property |
| ΔvapH | 32.06 | kJ/mol | 341.60 | Calculated Property |
| ΔvapH | 29.63 | kJ/mol | 380.38 | Calculated Property |
| ΔvapH | 26.76 | kJ/mol | 419.16 | Calculated Property |
| ΔvapH | 23.12 | kJ/mol | 457.94 | Calculated Property |
| ΔvapH | 17.91 | kJ/mol | 496.72 | Calculated Property |
| ΔvapH | 4.82 | kJ/mol | 535.50 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.68] | kPa | [259.76; 376.05] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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 | [1.41e-03; 4210.92] | kPa | [186.48; 535.50] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.70924e+01 | |||
| Coefficient B | -6.49896e+03 | |||
| Coefficient C | -9.38958e+00 | |||
| Coefficient D | 8.32043e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 186.48 | |||
| Temperature range, max. | 535.50 | |||
| Pvap | 1.41e-03 | kPa | 186.48 | Calculated Property |
| Pvap | 0.11 | kPa | 225.26 | Calculated Property |
| Pvap | 2.02 | kPa | 264.04 | Calculated Property |
| Pvap | 15.64 | kPa | 302.82 | Calculated Property |
| Pvap | 71.01 | kPa | 341.60 | Calculated Property |
| Pvap | 227.16 | kPa | 380.38 | Calculated Property |
| Pvap | 574.10 | kPa | 419.16 | Calculated Property |
| Pvap | 1233.95 | kPa | 457.94 | Calculated Property |
| Pvap | 2370.19 | kPa | 496.72 | Calculated Property |
| Pvap | 4210.92 | kPa | 535.50 | Calculated Property |
| Pvap | [1.45e-03; 4143.73] | kPa | [186.48; 535.50] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 6.69787e+01 | |||
| Coefficient B | -6.16017e+03 | |||
| Coefficient C | -7.78365e+00 | |||
| Coefficient D | 6.13927e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| 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 |
| Pvap | [25.20; 173.41] | kPa | [314.60; 370.60] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37911e+01 | |||
| Coefficient B | -2.64845e+03 | |||
| Coefficient C | -6.39040e+01 | |||
| Reference | Nickerson, Kobe, et al., 1961 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 314.60 | |||
| Temperature range, max. | 370.60 | |||
| Pvap | 25.20 | kPa | 314.60 | Calculated Property |
| Pvap | 32.54 | kPa | 320.82 | Calculated Property |
| Pvap | 41.53 | kPa | 327.04 | Calculated Property |
| Pvap | 52.40 | kPa | 333.27 | Calculated Property |
| Pvap | 65.42 | kPa | 339.49 | Calculated Property |
| Pvap | 80.88 | kPa | 345.71 | Calculated Property |
| Pvap | 99.09 | kPa | 351.93 | Calculated Property |
| Pvap | 120.36 | kPa | 358.16 | Calculated Property |
| Pvap | 145.02 | kPa | 364.38 | Calculated Property |
| Pvap | 173.41 | kPa | 370.60 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [902.52; 273.73] | kg/m3 | [186.48; 535.50] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 1.19104e+01 | |||
| Coefficient B | 1.07160e-01 | |||
| Coefficient C | 5.36800e+02 | |||
| Coefficient D | 1.50660e-01 | |||
| Temperature range, min. | 186.48 | |||
| Temperature range, max. | 535.50 | |||
| ρl | 902.52 | kg/m3 | 186.48 | Calculated Property |
| ρl | 870.00 | kg/m3 | 225.26 | Calculated Property |
| ρl | 835.22 | kg/m3 | 264.04 | Calculated Property |
| ρl | 797.62 | kg/m3 | 302.82 | Calculated Property |
| ρl | 756.39 | kg/m3 | 341.60 | Calculated Property |
| ρl | 710.25 | kg/m3 | 380.38 | Calculated Property |
| ρl | 657.00 | kg/m3 | 419.16 | Calculated Property |
| ρl | 592.16 | kg/m3 | 457.94 | Calculated Property |
| ρl | 503.51 | kg/m3 | 496.72 | Calculated Property |
| ρl | 273.73 | kg/m3 | 535.50 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.02] | N/m | [186.45; 352.75] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 5.74174e-02 | |||
| Coefficient B | -1.12200e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 186.45 | |||
| Temperature range, max. | 352.75 | |||
| γ | 0.04 | N/m | 186.45 | Calculated Property |
| γ | 0.03 | N/m | 204.93 | Calculated Property |
| γ | 0.03 | N/m | 223.41 | Calculated Property |
| γ | 0.03 | N/m | 241.88 | Calculated Property |
| γ | 0.03 | N/m | 260.36 | Calculated Property |
| γ | 0.03 | N/m | 278.84 | Calculated Property |
| γ | 0.02 | N/m | 297.32 | Calculated Property |
| γ | 0.02 | N/m | 315.79 | Calculated Property |
| γ | 0.02 | N/m | 334.27 | Calculated Property |
| γ | 0.02 | N/m | 352.75 | Calculated Property |
| γ | [0.04; 2.10e-05] | N/m | [186.48; 534.80] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -2.20050e-02 | |||
| Coefficient B | 1.77770e+01 | |||
| Coefficient C | -2.74970e+00 | |||
| Coefficient D | -3.55820e-04 | |||
| Coefficient E | -3.17740e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 535.5 K. | |||
| Temperature range, min. | 186.48 | |||
| Temperature range, max. | 534.80 | |||
| γ | 0.04 | N/m | 186.48 | Calculated Property |
| γ | 0.03 | N/m | 225.18 | Calculated Property |
| γ | 0.03 | N/m | 263.88 | Calculated Property |
| γ | 0.02 | N/m | 302.59 | Calculated Property |
| γ | 0.02 | N/m | 341.29 | Calculated Property |
| γ | 0.01 | N/m | 379.99 | Calculated Property |
| γ | 0.01 | N/m | 418.69 | Calculated Property |
| γ | 0.01 | N/m | 457.40 | Calculated Property |
| γ | 0.00 | N/m | 496.10 | Calculated Property |
| γ | 2.10e-05 | N/m | 534.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.12] | W/m×K | [186.48; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | -4.97070e+06 | |||
| Coefficient B | -2.31060e-01 | |||
| Coefficient C | 2.25770e+09 | |||
| Coefficient D | -1.08340e+13 | |||
| Temperature range, min. | 186.48 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 186.48 | Calculated Property |
| λgas | 0.01 | W/m×K | 276.87 | Calculated Property |
| λgas | 0.02 | W/m×K | 367.26 | Calculated Property |
| λgas | 0.03 | W/m×K | 457.65 | Calculated Property |
| λgas | 0.04 | W/m×K | 548.04 | Calculated Property |
| λgas | 0.05 | W/m×K | 638.44 | Calculated Property |
| λgas | 0.06 | W/m×K | 728.83 | Calculated Property |
| λgas | 0.08 | W/m×K | 819.22 | Calculated Property |
| λgas | 0.10 | W/m×K | 909.61 | Calculated Property |
| λgas | 0.12 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.17; 0.11] | W/m×K | [184.45; 422.04] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -1.78710e-01 | |||
| Coefficient B | 4.30860e+00 | |||
| Coefficient C | -1.03430e+00 | |||
| Coefficient D | 1.08010e-04 | |||
| Coefficient E | -1.54110e-06 | |||
| Temperature range, min. | 184.45 | |||
| Temperature range, max. | 422.04 | |||
| λliquid | 0.17 | W/m×K | 184.45 | Calculated Property |
| λliquid | 0.17 | W/m×K | 210.85 | Calculated Property |
| λliquid | 0.16 | W/m×K | 237.25 | Calculated Property |
| λliquid | 0.16 | W/m×K | 263.65 | Calculated Property |
| λliquid | 0.15 | W/m×K | 290.05 | Calculated Property |
| λliquid | 0.14 | W/m×K | 316.44 | Calculated Property |
| λliquid | 0.13 | W/m×K | 342.84 | Calculated Property |
| λliquid | 0.12 | W/m×K | 369.24 | Calculated Property |
| λliquid | 0.12 | W/m×K | 395.64 | Calculated Property |
| λliquid | 0.11 | W/m×K | 422.04 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Butanone.
Mixtures
- 2-Butanone + Ethanol
- 2-Butanone + Pentane, 2,2,4-trimethyl-
- 2-Butanone + Ethanol + Pentane, 2,2,4-trimethyl-
- Dimethyl phthalate + 2-Butanone
- 2-Butanone + Hexanedioic acid, dimethyl ester
- 2-Butanone + Dodecanedioic acid
- 2-Butanone + 1,2-Ethanediol + TETRAMETHYLAMMONIUM CHLORIDE
- 2-Butanone + Methylphosphonic acid
- 2-Butanone + Acetic acid
- 2-Butanone + Isopropyl acetate
- 2-Butanone + Acetic acid + Water
- 2-Butanone + Benzoic acid, 2-methyl-3-nitro-
- 2-Butanone + Ethyl Acetate
- 2-Butanone + sodium chloride + Water
- 2-Butanone + Water
- 2-Butanone + Benzenamine, 4-methyl-2-nitro-
- 2-Butanone + Triethylamine
- Diethyl carbonate + 2-Butanone + Water
- 2-Butanone + 2-ISOPROPYLIMIDAZOLE
- 2-Butanone + Methyl Alcohol
Find more mixtures with 2-Butanone.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- 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
- Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
- 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
- Dielectric study of H-bonded interactions in amyl alcohols with ketones and DMSO at T = 298.15 K
- Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
- 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
- Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
- Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
- Enthalpies of solution and enthalpies of solvation of organic solutes in ethylene glycol at 298.15 K: Prediction and analysis of intermolecular interaction contributions
- 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
- Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
- 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
- Distribution of Butyric Acid between Water and Several Solvents
- 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
- Henry s Law Constants for Fragrance and Organic Solvent Compounds in Aqueous Industrial Surfactants
- 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
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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