- InChI
- InChI=1S/C6H12O/c1-5(2)4-6(3)7/h5H,4H2,1-3H3
- InChI Key
- NTIZESTWPVYFNL-UHFFFAOYSA-N
- Formula
- C6H12O
- SMILES
- CC(=O)CC(C)C
- Molecular Weight1
- 100.16
- CAS
- 108-10-1
- Other Names
-
- 2-Methyl-4-pentanal
- 2-Methyl-4-pentanone
- 2-Methylpropyl methyl ketone
- 2-Pentanone, 4-methyl-
- 4-METHYL-2-PENTANONE
- 4-Methyl-2-oxopentane
- 4-Methyl-2-pentanon
- 4-Methyl-pentan-2-on
- 4-Methylpentan-2-one
- 4-Metilpentan-2-one
- 4-methyl-2-pentanone (MIBK; methyl isobutyl ketone)
- HEXONE
- Hexon
- Isobutyl methyl ketone
- Isobutyl-methylketon
- Isopropylacetone
- Ketone, isobutyl methyl
- METHYL-ISO-BUTYL KETONE
- MIBK
- MIK
- Methyl i-butyl ketone
- Methyl-2-pentanon,4-
- Methyl-isobutyl-cetone
- Methylisobutylketon
- Metilisobutilchetone
- Metyloizobutyloketon
- NSC 5712
- Rcra waste number U161
- Shell MIBK
- UN 1245
- ethyl iso-butyl ketone
- iso-C4H9COCH3
- isopropyl acetone
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- ΔcH°solid : Standard solid 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).
- 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).
- Rg : Radius of Gyration.
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (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.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3850 | KDB | |
| Tig | 729.82 | K | KDB |
| ΔcH°solid | -3694.60 | kJ/mol | NIST |
| μ | 2.80 | debye | KDB |
| η | [0.0005500; 0.0005600] | Pa×s |
|
| η | 0.0005500 | Pa×s | Viscosi... |
| η | 0.0005600 | Pa×s | Viscosi... |
| LFL | 1.40 | % in Air | KDB |
| UFL | 7.50 | % in Air | KDB |
| Tflash,cc | 297.04 | K | KDB |
| Tflash,oc | 295.93 | K | KDB |
| ΔfG° | -131.72 | kJ/mol | Joback Calculated Property |
| Rg | 3.7400 | KDB | |
| ΔfH°gas | [-291.20; -284.00] | kJ/mol |
|
| ΔfH°gas | -284.00 | kJ/mol | KDB |
| ΔfH°gas | -291.20 ± 1.40 | kJ/mol | NIST |
| ΔfH°solid | -381.50 | kJ/mol | NIST |
| ΔfusH° | 9.37 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [40.56; 42.50] | kJ/mol |
|
| ΔvapH° | 40.65 | kJ/mol | NIST |
| ΔvapH° | 40.56 | kJ/mol | NIST |
| ΔvapH° | 42.50 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 41.00 | kJ/mol | NIST |
| IE | [9.30; 9.42] | eV |
|
| IE | 9.30 ± 0.01 | eV | NIST |
| IE | 9.30 ± 0.01 | eV | NIST |
| IE | Outlier 9.42 | eV | NIST |
| IE | 9.34 ± 0.01 | eV | NIST |
| IE | 9.30 ± 0.02 | eV | NIST |
| IE | 9.30 ± 0.03 | eV | NIST |
| log10WS | [-0.96; -0.74] |
|
|
| log10WS | -0.96 | Aq. Sol... | |
| log10WS | -0.74 | Estimat... | |
| logPoct/wat | 1.621 | Crippen Calculated Property | |
| McVol | 96.970 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [3270.00; 3390.00] | kPa |
|
| Pc | 3270.00 | kPa | KDB |
| Pc | 3390.00 ± 20.00 | kPa | NIST |
| Pc | 3270.00 ± 5.00 | kPa | NIST |
| Pc | 3280.00 ± 96.50 | kPa | NIST |
| Inp | [698.00; 759.00] |
|
|
| Inp | 721.20 | NIST | |
| Inp | 722.94 | NIST | |
| Inp | 719.78 | NIST | |
| Inp | 720.12 | NIST | |
| Inp | 720.65 | NIST | |
| Inp | 721.70 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | Outlier 703.00 | NIST | |
| Inp | 705.00 | NIST | |
| Inp | 706.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 734.70 | NIST | |
| Inp | 729.60 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 729.50 | NIST | |
| Inp | 716.00 | NIST | |
| Inp | 733.30 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 742.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | Outlier 753.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | Outlier 749.00 | NIST | |
| Inp | Outlier 759.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | Outlier 698.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 713.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 715.83 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 720.00 | NIST | |
| I | [994.00; 1059.00] |
|
|
| I | 1039.50 | NIST | |
| I | 1025.20 | NIST | |
| I | 1029.00 | NIST | |
| I | 1033.90 | NIST | |
| I | 1034.00 | NIST | |
| I | 1007.00 | NIST | |
| I | 1015.00 | NIST | |
| I | 994.00 | NIST | |
| I | Outlier 1059.00 | NIST | |
| I | 1010.00 | NIST | |
| I | Outlier 1059.00 | NIST | |
| I | 1021.20 | NIST | |
| I | 1012.00 | NIST | |
| I | 1009.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1008.00 | NIST | |
| I | 999.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1028.00 | NIST | |
| I | 1013.00 | NIST | |
| I | 1006.00 | NIST | |
| I | 1008.00 | NIST | |
| I | 1013.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1020.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1007.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1007.00 | NIST | |
| I | 1008.00 | NIST | |
| I | 1008.00 | NIST | |
| I | 1017.00 | NIST | |
| I | 1008.00 | NIST | |
| I | 999.00 | NIST | |
| I | 1017.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1002.00 | NIST | |
| I | 1000.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1019.00 | NIST | |
| Tboil | [387.35; 392.30] | K |
|
| Tboil | 389.60 | K | KDB |
| Tboil | 392.30 | K | Liquid-... |
| Tboil | 390.50 | K | Solubil... |
| Tboil | 390.54 | K | Excess ... |
| Tboil | 389.15 | K | Vapor-L... |
| Tboil | 389.45 | K | Measure... |
| Tboil | 387.35 | K | Conduct... |
| Tc | [571.00; 575.50] | K |
|
| Tc | 571.00 | K | KDB |
| Tc | 575.50 ± 0.50 | K | NIST |
| Tc | 574.60 ± 0.50 | K | NIST |
| Tc | 571.00 | K | NIST |
| Tc | 571.00 ± 1.11 | K | NIST |
| Tfus | [189.00; 189.15] | K |
|
| Tfus | 189.00 | K | KDB |
| Tfus | 189.15 | K | NIST |
| Vc | 0.371 | m3/kmol | Joback Calculated Property |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [180.50; 187.90] | J/mol×K | [394.30; 415.75] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 182 184 186 188 400 410 | ||||
| Cp,gas | 180.50 ± 0.27 | J/mol×K | 394.30 | NIST |
| Cp,gas | 182.26 ± 0.27 | J/mol×K | 399.44 | NIST |
| Cp,gas | 184.31 ± 0.28 | J/mol×K | 405.15 | NIST |
| Cp,gas | 186.06 ± 0.28 | J/mol×K | 410.70 | NIST |
| Cp,gas | 187.90 ± 0.28 | J/mol×K | 415.75 | NIST |
| Cp,liquid | 211.90 | J/mol×K | 298.15 | NIST |
| η | [0.0002910; 0.0061867] | Pa×s | [192.31; 390.11] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 200 250 300 350 | ||||
| η | 0.0061867 | Pa×s | 192.31 | Joback Calculated Property |
| η | 0.0025603 | Pa×s | 225.28 | Joback Calculated Property |
| η | 0.0013273 | Pa×s | 258.24 | Joback Calculated Property |
| η | 0.0007984 | Pa×s | 291.21 | Joback Calculated Property |
| η | 0.0005326 | Pa×s | 324.18 | Joback Calculated Property |
| η | 0.0003828 | Pa×s | 357.14 | Joback Calculated Property |
| η | 0.0002910 | Pa×s | 390.11 | Joback Calculated Property |
| ΔvapH | [34.49; 42.50] | kJ/mol | [308.00; 389.40] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 34 36 38 40 42 320 340 360 380 | ||||
| ΔvapH | 40.10 ± 0.10 | kJ/mol | 308.00 | NIST |
| ΔvapH | 39.00 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 38.00 ± 0.10 | kJ/mol | 338.00 | NIST |
| ΔvapH | 42.50 | kJ/mol | 340.50 | NIST |
| ΔvapH | 41.20 | kJ/mol | 342.00 | NIST |
| ΔvapH | 37.60 | kJ/mol | 347.00 | NIST |
| ΔvapH | 37.40 ± 0.10 | kJ/mol | 348.00 | NIST |
| ΔvapH | 38.70 | kJ/mol | 359.00 | NIST |
| ΔvapH | 39.20 | kJ/mol | 362.50 | NIST |
| ΔvapH | 37.00 | kJ/mol | 369.00 | NIST |
| ΔvapH | 40.61 | kJ/mol | 388.90 | NIST |
| ΔvapH | 34.49 | kJ/mol | 389.40 | NIST |
| Pvap | [3.89; 114.12] | kPa | [303.15; 393.15] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 120 320 340 360 380 | ||||
| Pvap | 3.89 | kPa | 303.15 | Density... |
| Pvap | 5.88 | kPa | 313.15 | Phase e... |
| Pvap | 9.42 | kPa | 323.15 | Phase e... |
| Pvap | 13.85 | kPa | 331.98 | Phase e... |
| Pvap | 14.56 | kPa | 333.15 | Phase e... |
| Pvap | 19.35 | kPa | 340.18 | Vapor L... |
| Pvap | 19.78 | kPa | 340.66 | Vapor L... |
| Pvap | 20.72 | kPa | 341.81 | Phase e... |
| Pvap | 21.82 | kPa | 343.15 | Phase e... |
| Pvap | 21.92 | kPa | 343.42 | Vapor L... |
| Pvap | 30.01 | kPa | 351.55 | Vapor L... |
| Pvap | 30.29 | kPa | 351.81 | Phase e... |
| Pvap | 31.12 | kPa | 352.71 | Vapor L... |
| Pvap | 31.71 | kPa | 353.11 | Vapor L... |
| Pvap | 31.80 | kPa | 353.15 | Phase e... |
| Pvap | 39.35 | kPa | 359.22 | Vapor L... |
| Pvap | 39.63 | kPa | 359.39 | Vapor L... |
| Pvap | 40.05 | kPa | 359.58 | Vapor L... |
| Pvap | 43.51 | kPa | 362.04 | Phase e... |
| Pvap | 44.70 | kPa | 362.88 | Vapor L... |
| Pvap | 45.19 | kPa | 363.15 | Phase e... |
| Pvap | 49.68 | kPa | 365.90 | Vapor L... |
| Pvap | 50.66 | kPa | 366.61 | Vapor L... |
| Pvap | 53.01 | kPa | 368.06 | Vapor L... |
| Pvap | 53.42 | kPa | 368.07 | Vapor L... |
| Pvap | 53.26 | kPa | 368.14 | Vapor L... |
| Pvap | 53.24 | kPa | 368.15 | Vapor L... |
| Pvap | 54.29 | kPa | 368.70 | Vapor L... |
| Pvap | 59.43 | kPa | 371.34 | Vapor L... |
| Pvap | 59.75 | kPa | 371.64 | Vapor L... |
| Pvap | 60.19 | kPa | 371.91 | Vapor L... |
| Pvap | 60.56 | kPa | 372.03 | Phase e... |
| Pvap | 62.78 | kPa | 373.15 | Phase e... |
| Pvap | 65.18 | kPa | 374.37 | Vapor L... |
| Pvap | 69.16 | kPa | 376.26 | Vapor L... |
| Pvap | 69.98 | kPa | 376.49 | Vapor L... |
| Pvap | 74.83 | kPa | 378.80 | Vapor L... |
| Pvap | 79.56 | kPa | 380.65 | Vapor L... |
| Pvap | 80.16 | kPa | 381.06 | Vapor L... |
| Pvap | 82.62 | kPa | 382.04 | Phase e... |
| Pvap | 84.16 | kPa | 382.66 | Vapor L... |
| Pvap | 85.44 | kPa | 383.15 | Phase e... |
| Pvap | 90.58 | kPa | 384.99 | Vapor L... |
| Pvap | 98.70 | kPa | 388.07 | Vapor L... |
| Pvap | 99.40 | kPa | 388.31 | Vapor L... |
| Pvap | 100.35 | kPa | 388.63 | Vapor L... |
| Pvap | 100.41 | kPa | 388.65 | Vapor L... |
| Pvap | 101.85 | kPa | 389.06 | Vapor L... |
| Pvap | 101.30 | kPa | 389.15 | Vapor-L... |
| Pvap | 102.78 | kPa | 389.49 | Vapor L... |
| Pvap | 110.74 | kPa | 392.07 | Phase e... |
| Pvap | 114.12 | kPa | 393.15 | Phase e... |
| n0 | [1.39327; 1.39586] | [293.15; 298.15] |
|
|
|
T(K) Refractive Index 1.39 1.39 1.39 1.4 1.4 1.4 294 296 298 | ||||
| n0 | 1.39586 | 293.15 | Vapor L... | |
| n0 | 1.39355 | 298.15 | Isobari... | |
| n0 | 1.39360 | 298.15 | Bubble ... | |
| n0 | 1.39350 | 298.15 | Excess ... | |
| n0 | 1.39327 | 298.15 | Ternary... | |
| n0 | 1.39420 | 298.15 | Isobari... | |
| n0 | 1.39360 | 298.15 | Liquid-... | |
| ρl | [773.00; 805.12] | kg/m3 | [288.15; 323.15] |
|
|
T(K) Liquid Density (kg/m3) 770 775 780 785 790 795 800 805 290 300 310 320 | ||||
| ρl | 805.12 | kg/m3 | 288.15 | Thermal... |
| ρl | 801.00 | kg/m3 | 293.00 | KDB |
| ρl | 800.80 | kg/m3 | 293.15 | Evaluat... |
| ρl | 800.90 | kg/m3 | 293.15 | Effect ... |
| ρl | 800.00 | kg/m3 | 293.15 | Thermop... |
| ρl | 801.00 | kg/m3 | 293.15 | Thermop... |
| ρl | 799.61 | kg/m3 | 293.20 | Liquid-... |
| ρl | 799.00 | kg/m3 | 298.15 | Liquid ... |
| ρl | 798.09 | kg/m3 | 298.15 | Evaluat... |
| ρl | 800.59 | kg/m3 | 298.15 | Liquid-... |
| ρl | 795.98 | kg/m3 | 298.15 | Thermal... |
| ρl | 795.94 | kg/m3 | 298.15 | Liquid ... |
| ρl | 796.23 | kg/m3 | 298.15 | Liquid-... |
| ρl | 796.19 | kg/m3 | 298.15 | Excess ... |
| ρl | 799.80 | kg/m3 | 298.15 | Liquid ... |
| ρl | 796.50 | kg/m3 | 298.15 | Isother... |
| ρl | 796.03 | kg/m3 | 298.15 | Evaluat... |
| ρl | 796.10 | kg/m3 | 298.15 | Evaluat... |
| ρl | 792.00 | kg/m3 | 303.15 | Thermop... |
| ρl | 791.25 | kg/m3 | 303.15 | Excess ... |
| ρl | 791.60 | kg/m3 | 303.15 | Evaluat... |
| ρl | 796.33 | kg/m3 | 303.15 | Excess ... |
| ρl | 786.75 | kg/m3 | 308.15 | Thermal... |
| ρl | 786.90 | kg/m3 | 308.15 | Evaluat... |
| ρl | 782.30 | kg/m3 | 313.15 | Evaluat... |
| ρl | 782.00 | kg/m3 | 313.15 | Thermop... |
| ρl | 781.11 | kg/m3 | 313.20 | Liquid-... |
| ρl | 777.60 | kg/m3 | 318.15 | Evaluat... |
| ρl | 777.46 | kg/m3 | 318.15 | Thermal... |
| ρl | 773.00 | kg/m3 | 323.15 | Evaluat... |
| csound,fluid | [1138.00; 1175.00] | m/s | [303.15; 313.15] |
|
| csound,fluid | 1175.00 | m/s | 303.15 | Densiti... |
| csound,fluid | 1156.00 | m/s | 308.15 | Densiti... |
| csound,fluid | 1138.00 | m/s | 313.15 | Densiti... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 308.15 | 101.30 | 0.0005 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [288.82; 413.37] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.49712e+01 | |||
| Coefficient B | -3.51652e+03 | |||
| Coefficient C | -4.93340e+01 | |||
| Temperature range, min. | 288.82 | |||
| Temperature range, max. | 413.37 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 288.82 | Calculated Property |
| Pvap | 2.97 | kPa | 302.66 | Calculated Property |
| Pvap | 6.10 | kPa | 316.50 | Calculated Property |
| Pvap | 11.67 | kPa | 330.34 | Calculated Property |
| Pvap | 21.00 | kPa | 344.18 | Calculated Property |
| Pvap | 35.84 | kPa | 358.01 | Calculated Property |
| Pvap | 58.43 | kPa | 371.85 | Calculated Property |
| Pvap | 91.52 | kPa | 385.69 | Calculated Property |
| Pvap | 138.33 | kPa | 399.53 | Calculated Property |
| Pvap | 202.63 | kPa | 413.37 | Calculated Property |
| Pvap | [2.17; 100.82] | kPa | [295.15; 389.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.58031e+02 | |||
| Coefficient B | -1.05457e+04 | |||
| Coefficient C | -2.16516e+01 | |||
| Coefficient D | 1.85635e-05 | |||
| Temperature range, min. | 295.15 | |||
| Temperature range, max. | 389.15 | |||
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 300 350 | ||||
| Pvap | 2.17 | kPa | 295.15 | Calculated Property |
| Pvap | 3.89 | kPa | 305.59 | Calculated Property |
| Pvap | 6.64 | kPa | 316.04 | Calculated Property |
| Pvap | 10.82 | kPa | 326.48 | Calculated Property |
| Pvap | 16.93 | kPa | 336.93 | Calculated Property |
| Pvap | 25.58 | kPa | 347.37 | Calculated Property |
| Pvap | 37.46 | kPa | 357.82 | Calculated Property |
| Pvap | 53.36 | kPa | 368.26 | Calculated Property |
| Pvap | 74.15 | kPa | 378.71 | Calculated Property |
| Pvap | 100.82 | kPa | 389.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Methyl Isobutyl Ketone.
Mixtures
- Methyl Isobutyl Ketone + Isopropyl Alcohol
- Methyl Isobutyl Ketone + Diisopropyl ether
- Methyl Isobutyl Ketone + Diisopropyl ether + Isopropyl Alcohol
- Methyl Isobutyl Ketone + 1-Butanol
- Methyl Isobutyl Ketone + 1-Propanol + Water
- Methyl Isobutyl Ketone + Isopropyl Alcohol + Water
- Methyl Isobutyl Ketone + Lactic acid + Water
- Methyl Isobutyl Ketone + Cyclopentanol + Water
- Methyl Isobutyl Ketone + Water
- Methyl Isobutyl Ketone + Acetic acid + Water
- Methyl Isobutyl Ketone + 2-Pyrrolidinone, 1-methyl-
- Methyl Isobutyl Ketone + Ethylbenzene
- Methyl Isobutyl Ketone + Trichloromethane
- Methyl Isobutyl Ketone + Dimethyl Sulfoxide
- Methyl Isobutyl Ketone + Furan, 2,5-dimethyl-
- Methyl Isobutyl Ketone + Acetone
- Methyl Isobutyl Ketone + Acetonitrile
- Methyl Isobutyl Ketone + Cyclohexane
- Methyl Isobutyl Ketone + Methyl Alcohol
- Methyl Isobutyl Ketone + Ethanol
Find more mixtures with Methyl Isobutyl Ketone.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, diisopropyl ether and 4-methyl-2-pentanone
- Liquid liquid equilibria for the quaternary system methyl isobutyl ketone water phenol hydroquinone
- Isobaric vapour liquid equilibria for the binary systems 4-methyl-2-pentanone + 1-butanol and + 2-butanol at 20 and 101.3 kPa
- Compact apparatus for rapid measurement of high-pressure phase equilibria of carbon dioxide expanded liquids
- Isothermal vapour-liquid equilibria in the binary and ternary systems composed of 2,2,4-trimethylpentane, 2-methyl-1-propanol, and 4-methyl-2-pentanone
- Selection of entrainers for the separation of the binary azeotropic system methanol + dimethyl carbonate by extractive distillation
- Measurements and correlation of liquid-liquid equilibria of 4-methyl-2-pentanone + ethanol + water and 4-methyl-2-pentanone + n-butanol + water ternary systems between 283.2 and 323.2 K
- Solubility of lansoprazole in different solvents
- 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
- Liquid liquid equilibria of 4-methyl-2-pentanone + 1-propanol or 2-propanol + water ternary systems: Measurements and correlation at different temperatures
- Isothermal vapor-liquid equilibrium and excess molar enthalpies of the binary mixtures furfural + methyl isobutyl ketone, + 2-butanol and + 2-methyl-2-butanol
- Liquid-liquid equilibria of water + lactic acid + methyl isobutyl ketone
- Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
- Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
- Salt influence on MIBK/water liquid-liquid equilibrium: Measuring and modeling with ePC-SAFT and COSMO-RS
- Liquid-liquid equilibria for methyl isobutyl ketone + cresols + water at 333.15K, 343.15K and 353.15K: Experimental results and data correlation
- Liquid-liquid equilibrium for ternary systems, methyl isobutyl ketone +(catechol, resorcinol and hydroquinone) + water at 333.15 K, 343.15 K and 353.15 K
- Measurement of the solubility of the salt of 2- mercaptobenzothiazole with cyclohexylamine and tert-butylamine in various solvents at low temperatures: Models and thermodynamic parameters
- The solubility of maleic acid in various inorganic salts and organic solvents: Thermodynamics model and parameters
- Liquid-liquid equilibria of ternary and quaternary systems involving 5-hydroxymethylfurfural, water, organic solvents, and salts at 313.15 K and atmospheric pressure
- Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents
- Salt effect on liquid-liquid equilibria of tetrahydrofuran/water/5-hydroxymethylfurfural systems
- Salting-out effect of NaCl and KCl on the ternary LLE data for the systems of (water + propionic acid + isopropyl methyl ketone) and of (water + propionic acid + isobutyl methyl ketone)
- 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
- Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
- Density, viscosity, isothermal (vapour + liquid) equilibrium, excess molar volume, viscosity deviation, and their correlations for chloroform + methyl isobutyl ketone binary system
- Excess enthalpies and (vapour + liquid) equilibrium data for the binary mixtures of dimethylsulphoxide with ketones
- Excess molar volumes and ultrasonic studies of dimethylsulphoxide with ketones at T = 303.15 K
- Excess molar volumes and ultrasonic studies of N-methyl-2-pyrrolidone with ketones at T = 303.15 K
- Phase equilibrium properties of binary mixtures containing 2,5-dimethylfuran and furfuryl alcohol or methyl isobutyl ketone at several temperatures
- Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
- Effect of 1-ethyl-3-methylimidazolium tetrafluoroborate on the phase equilibria for systems containing 5-hydroxymethylfurfural, water, organic solvent in the absence and presence of sodium chloride
- Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
- Evaluation of thermodynamic properties of fluid mixtures by PC-SAFT model
- Ternary and Binary LLE Measurements for Solvent (4- Methyl-2-pentanone and 2-Methyl-2-butanol) + Furfural + Water between 298 and 401 K
- Solubility of Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
- Influence of Salt on the Solubility and Tie-Line Data for Water + Formic Acid + Methyl Isobutyl Ketone at T = 298.15 K
- Equilibrium Study on the Extraction of Levulinic Acid from Aqueous Solution with Aliquat 336 Dissolved in Different Diluents: Solvent s Polarity Effect and Column Design
- Liquid-Liquid Equilibria of Ionic Liquids-Water-Acetic Acid Mixtures
- Solubility Measurement and Correlation of Two Erlotinib Hydrochloride Polymorphs in Alcohols and Ketones from 273.15 to 323.15 K
- Evaluation of Diethyl Carbonate and Methyl Isobutyl Ketone as Entrainers for the Separation of 1-Hexene and n-Hexane
- Determination and Thermodynamic Modeling of Solid Liquid Phase Equilibrium for Esomeprazole Sodium in Monosolvents and in the (Ethanol + Ethyl Acetate) Binary Solvent Mixtures
- Vapor Liquid Equilibrium for Methyl Isobutyl Ketone (MIBK) + (1-Propanol or 2-Propanol) Binary Mixtures
- Thermal and Volumetric Properties of Some C5 and C6 Alkanones at Infinite Dilution in Water
- Measurement and Thermodynamic Modeling of Ternary (Liquid + Liquid) Equilibrium for Extraction of N,N-Dimethylacetamide from Aqueous Solution with Different Solvents
- Extraction of Citric Acid and Maleic Acid from Their Aqueous Solutions Using a Phosphorus-Bonded Extractant, Tri-n-octylphosphineoxide, and a Secondary Amine, Dioctylamine
- Liquid-Liquid Equilibrium Data and Correlation for the Quaternary Systems Water + Polyphenol (Hydroquinone, Catechol, and Resorcinol) + Methyl Isobutyl Ketone + Methylbenzene
- Liquid-Liquid Equilibria for the Ternary Systems Water + Cyclohexanol + Methyl Isobutyl Carbinol and Water + Cyclohexanol + Methyl Isobutyl Ketone at Different Temperatures
- Liquid-Liquid Equilibrium of Water + 2-Methoxyphenol + Methyl Isobutyl Ketone and Water + 1,2-Benzenediol + Methyl Isobutyl Ketone at 303.15 K and 328.15 K
- Solubility of 2,5-Furandicarboxylic Acid in Eight Pure Solvents and Two Binary Solvent Systems at 313.15-363.15 K
- Liquid-Liquid Equilibrium for the Ternary Systems (Methyl Isobutyl Ketone + Quinoline or Isoquinoline + Water) at 298.15, 318.15, and 338.15 K
- Liquid-Liquid Equilibrium for Ternary Systems, Water + 5-Hydroxymethylfurfural + (1-Butanol, Isobutanol, Methyl Isobutyl Ketone), at 313.15, 323.15, and 333.15 K
- Solubility Determination and Correlation of Glibenclamide in 11 Monosolvents and (Acetone + Acetonitrile) Binary Solvents from 283.15 K to 323.15 K
- Experimental Study on Reactive Extraction of Malonic Acid with Validation by Fourier Transform Infrared Spectroscopy
- Comparison of Extractability of Oxalic Acid from Dilute Aqueous Solutions Using Dioctylamine and Trioctylphosphine Oxide
- Effect of Diluents on Extraction Equilibrium of trans-Aconitic Acid
- Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
- Parametric Analysis of Mandelic Acid Separation from Aqueous Solutions by Using Secondary Amine Mixture (Amberlite LA-2) in Various Diluents
- Experiments and COSMO-SAC Modeling of Methyl Isobutyl Ketone + Dimethylphenols + Water Mixtures
- Vapor-Liquid Equilibrium for Binary of 1-Butanol + N,N-Dimethylacetamide and Methyl Isobutyl Ketone + N,N-Dimethylacetamide at 101.3 kPa
- Air-Water Partitioning of C5 and C6 Alkanones: Measurement, Critical Compilation, Correlation, and Recommended Data
- Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 4-Methylpentan-2-one at 298.15 K
- Measurements of Quaternary Liquid-Liquid Equilibrium for Water + Acetic Acid + Propionic Acid + Solvent (Butyronitrile, Benzyl Acetate, or Methyl Isobutyl Ketone) at 298.15 K
- Liquid-Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + Water + Hydroquinone
- Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and Methyl Isobutyl Ketone at 100 kPa
- Liquid-Liquid and Vapor-Liquid-Liquid Equilibrium of the 4-Methyl-2-pentanone + 2-Butanol + Water System
- Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
- Biomass-Derived Platform Chemicals: Thermodynamic Studies on the Extraction of 5-Hydroxymethylfurfural from Ionic Liquids
- Liquid Liquid Equilibria for the System Water + 4-Methylpentan-2-one + Acetic Acid at Several Temperatures
- Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing Methyl Isobutyl Ketone (MIBK) and 2-Butanol, tert-Pentanol, or 2-Ethyl-1-hexanol
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Liquid Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + m-Benzenediol + Water
- Liquid Liquid Equilibria for the Ternary System Methyl Isobutyl Ketone + 1,2-Benzenediol + Water
- Liquid Liquid Equilibria of the Ternary System Water + Acrylic Acid + 4-Methyl-2-pentanone at 298.15 K
- Liquid Liquid Equilibria for the Ternary System Water + Methyl Isobutyl Ketone + tert-Butyl Alcohol at Several Temperatures
- Viscosity of the Tributyl Phosphate + Methyl Isobutyl Ketone + Phosphoric Acid System
- Volumetric and Transport Properties of Binary Liquid Mixtures of Aliphatic Ketones with Phenylacetonitrile at T = 308.15 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
- Solubility of Penicillin Sulfoxide in Different Solvents
- Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
- Conductivity and Dissociation Constants of Quaternary Ammonium Perchlorates and Picrates in 4-Methyl-pentan-2-one
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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