- InChI
- InChI=1S/C7H14O/c1-6(2)4-5-7(3)8/h6H,4-5H2,1-3H3
- InChI Key
- FFWSICBKRCICMR-UHFFFAOYSA-N
- Formula
- C7H14O
- SMILES
- CC(=O)CCC(C)C
- Molecular Weight1
- 114.19
- CAS
- 110-12-3
- Other Names
-
- (CH3)2CHCH2CH2COCH3
- 2-Methyl-5-Hexanone
- 3-Methylbutyl methyl ketone
- 5-Methylhexan-2-one
- 5-methyl-2-hexanone
- Ketone, methyl isoamyl
- MIAK
- Methyl isoamyl ketone
- Methyl isopentyl ketone
- UN 2302
- isoamyl methyl ketone
- isopentyl methyl ketone
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : 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.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- 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.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4344 | ChemSep v8.3 pure component data Compiled value | |
| Tig | 698.15 | K | NCMS SOLV-DB |
| Tflash,cc | 309.15 | K | NCMS SOLV-DB |
| ΔfG° | -122.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -304.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 11.96 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 37.69 | kJ/mol | NCMS SOLV-DB |
| IE | 9.28 ± 0.01 | eV | NIST |
| log10WS | -1.33 | Aq. Solubility Prediction | |
| logPoct/wat | 1.718 | NCMS SOLV-DB | |
| McVol | 111.060 | ml/mol | McGowan Calculated Property |
| NFPA Fire | [%!d(float64=2); %!d(float64=2)] |
|
|
| NFPA Fire | 2 | KDB | |
| NFPA Fire | 2 | 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 | 2970.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 2.42e-05 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [819.00; 865.00] |
|
|
| Inp | 836.50 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 830.90 | NIST | |
| Inp | Outlier 862.00 | NIST | |
| Inp | Outlier 862.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | Outlier 865.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 825.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | Outlier 862.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 831.00 | NIST | |
| Ip | [1140.00; 1190.00] |
|
|
| Ip | 1172.10 | NIST | |
| Ip | 1156.10 | NIST | |
| Ip | 1160.90 | NIST | |
| Ip | 1166.30 | NIST | |
| Ip | 1150.00 | NIST | |
| Ip | 1142.00 | NIST | |
| Ip | 1168.00 | NIST | |
| Ip | Outlier 1190.00 | NIST | |
| Ip | 1155.00 | NIST | |
| Ip | 1154.00 | NIST | |
| Ip | 1186.00 | NIST | |
| Ip | 1141.00 | NIST | |
| Ip | 1146.00 | NIST | |
| Ip | 1154.00 | NIST | |
| Ip | 1140.00 | NIST | |
| Ip | 1188.00 | NIST | |
| Ip | 1156.00 | NIST | |
| Ip | 1154.00 | NIST | |
| Ip | 1140.00 | NIST | |
| Tboil | [407.65; 418.15] | K |
|
| Tboil | 417.95 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 418.15 | K | NCMS SOLV-DB |
| Tboil | 417.20 | K | NIST |
| Tboil | 418.05 | K | NIST |
| Tboil | 417.35 ± 1.00 | K | NIST |
| Tboil | 409.05 ± 1.00 | K | NIST |
| Tboil | 417.40 ± 0.50 | K | NIST |
| Tboil | 408.15 ± 2.00 | K | NIST |
| Tboil | 417.00 ± 3.00 | K | NIST |
| Tboil | 416.45 ± 1.00 | K | NIST |
| Tboil | 417.15 ± 2.00 | K | NIST |
| Tboil | 417.15 ± 2.00 | K | NIST |
| Tboil | 410.15 ± 2.00 | K | NIST |
| Tboil | 407.65 ± 2.00 | K | NIST |
| Tboil | 416.15 ± 2.00 | K | NIST |
| Tboil | 416.00 ± 5.00 | K | NIST |
| Tc | [601.00; 604.10] | K |
|
| Tc | 604.10 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 601.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [199.15; 199.30] | K |
|
| Tfus | 199.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 199.25 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 199.15 | K | NCMS SOLV-DB |
| Tfus | 199.25 | K | NIST |
| Tfus | 199.30 ± 0.60 | K | NIST |
| Ttriple | 199.25 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 4.49 | ChemSep v8.3 pure component data Compiled value | |
| URi | 5.27 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.421 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2500000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.25 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | 0.0007000 | Pa×s | 298.15 | NCMS SOLV-DB |
| Pvap | 0.69 | kPa | 298.15 | NCMS SOLV-DB |
| n0 | [1.40510; 1.40740] | [293.15; 298.15] |
|
|
| n0 | 1.40740 | 293.15 | (Liquid + liquid) equilibria of (water + propionic acid + methyl isoamyl ketone or diisobutyl ketone or ethyl isoamyl keton) at T = 298.2 K | |
| n0 | 1.40510 | 293.20 | Experimental and Correlational Study of Phase Equilibria in Aqueous Solutions of Formic and Butyric Acids with Isoamyl Acetate and Methyl Isoamyl Ketone at T = 298.15 K | |
| n0 | 1.40700 | 298.15 | NCMS SOLV-DB | |
| ρl | 887.90 | kg/m3 | 293.20 | Experimental study of phase equilibria in aqueous mixtures of phosphoric acid with isoamyl acetate and methyl isoamyl ketone at T = (298.2, 308.2, and 318.2) K |
| γ | 0.03 | N/m | 298.15 | NCMS SOLV-DB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [156.92; 396.75] | J/mol×K | [273.00; 1200.00] |
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 | 9.68320e+01 | |||
| Coefficient B | -5.30600e+02 | |||
| Coefficient C | 5.97024e+00 | |||
| Coefficient D | 2.84830e-04 | |||
| Coefficient E | -1.15520e-07 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1200.00 | |||
| Cp,gas | 156.92 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 201.40 | J/mol×K | 376.00 | Calculated Property |
| Cp,gas | 241.21 | J/mol×K | 479.00 | Calculated Property |
| Cp,gas | 275.44 | J/mol×K | 582.00 | Calculated Property |
| Cp,gas | 304.63 | J/mol×K | 685.00 | Calculated Property |
| Cp,gas | 329.50 | J/mol×K | 788.00 | Calculated Property |
| Cp,gas | 350.70 | J/mol×K | 891.00 | Calculated Property |
| Cp,gas | 368.73 | J/mol×K | 994.00 | Calculated Property |
| Cp,gas | 383.98 | J/mol×K | 1097.00 | Calculated Property |
| Cp,gas | 396.75 | J/mol×K | 1200.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [204.65; 290.83] | J/mol×K | [199.25; 417.95] |
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 | 1.25240e+02 | |||
| Coefficient B | 1.63140e+02 | |||
| Coefficient C | 2.20334e+00 | |||
| Coefficient D | 7.48830e-03 | |||
| Coefficient E | -3.51440e-06 | |||
| Temperature range, min. | 199.25 | |||
| Temperature range, max. | 417.95 | |||
| Cp,liquid | 204.65 | J/mol×K | 199.25 | Calculated Property |
| Cp,liquid | 209.30 | J/mol×K | 223.55 | Calculated Property |
| Cp,liquid | 215.41 | J/mol×K | 247.85 | Calculated Property |
| Cp,liquid | 222.80 | J/mol×K | 272.15 | Calculated Property |
| Cp,liquid | 231.37 | J/mol×K | 296.45 | Calculated Property |
| Cp,liquid | 241.09 | J/mol×K | 320.75 | Calculated Property |
| Cp,liquid | 251.91 | J/mol×K | 345.05 | Calculated Property |
| Cp,liquid | 263.81 | J/mol×K | 369.35 | Calculated Property |
| Cp,liquid | 276.80 | J/mol×K | 393.65 | Calculated Property |
| Cp,liquid | 290.83 | J/mol×K | 417.95 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0058816; 0.0001125] | Pa×s | [199.25; 501.00] |
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 | -1.52920e+01 | |||
| Coefficient B | 1.38870e+03 | |||
| Coefficient C | 6.13360e-01 | |||
| Coefficient D | -1.53720e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 199.25 | |||
| Temperature range, max. | 501.00 | |||
| η | 0.0058816 | Pa×s | 199.25 | Calculated Property |
| η | 0.0023189 | Pa×s | 232.78 | Calculated Property |
| η | 0.0011581 | Pa×s | 266.31 | Calculated Property |
| η | 0.0006752 | Pa×s | 299.83 | Calculated Property |
| η | 0.0004377 | Pa×s | 333.36 | Calculated Property |
| η | 0.0003060 | Pa×s | 366.89 | Calculated Property |
| η | 0.0002260 | Pa×s | 400.42 | Calculated Property |
| η | 0.0001740 | Pa×s | 433.94 | Calculated Property |
| η | 0.0001382 | Pa×s | 467.47 | Calculated Property |
| η | 0.0001125 | Pa×s | 501.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [55.15; 0.00] | kJ/mol | [199.25; 601.00] |
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 | 8.00537e+01 | |||
| Coefficient B | 1.17745e+00 | |||
| Coefficient C | -7.08374e-01 | |||
| Coefficient D | -2.21424e-01 | |||
| Coefficient E | 1.84955e-01 | |||
| Critical temperature, Tc (K) | 6.01000e+02 | |||
| Temperature range, min. | 199.25 | |||
| Temperature range, max. | 601.00 | |||
| ΔvapH | 55.15 | kJ/mol | 199.25 | Calculated Property |
| ΔvapH | 51.01 | kJ/mol | 243.89 | Calculated Property |
| ΔvapH | 47.23 | kJ/mol | 288.53 | Calculated Property |
| ΔvapH | 43.73 | kJ/mol | 333.17 | Calculated Property |
| ΔvapH | 40.39 | kJ/mol | 377.81 | Calculated Property |
| ΔvapH | 37.07 | kJ/mol | 422.44 | Calculated Property |
| ΔvapH | 33.51 | kJ/mol | 467.08 | Calculated Property |
| ΔvapH | 29.25 | kJ/mol | 511.72 | Calculated Property |
| ΔvapH | 23.06 | kJ/mol | 556.36 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 601.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [311.86; 439.81] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.53053e+01 | |||
| Coefficient B | -3.82231e+03 | |||
| Coefficient C | -5.73400e+01 | |||
| Temperature range, min. | 311.86 | |||
| Temperature range, max. | 439.81 | |||
| Pvap | 1.33 | kPa | 311.86 | Calculated Property |
| Pvap | 2.95 | kPa | 326.08 | Calculated Property |
| Pvap | 6.03 | kPa | 340.29 | Calculated Property |
| Pvap | 11.51 | kPa | 354.51 | Calculated Property |
| Pvap | 20.70 | kPa | 368.73 | Calculated Property |
| Pvap | 35.38 | kPa | 382.94 | Calculated Property |
| Pvap | 57.82 | kPa | 397.16 | Calculated Property |
| Pvap | 90.83 | kPa | 411.38 | Calculated Property |
| Pvap | 137.79 | kPa | 425.59 | Calculated Property |
| Pvap | 202.67 | kPa | 439.81 | Calculated Property |
| Pvap | [2.52e-05; 2980.28] | kPa | [199.25; 601.00] |
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 | 1.07212e+02 | |||
| Coefficient B | -9.18000e+03 | |||
| Coefficient C | -1.36130e+01 | |||
| Coefficient D | 8.76560e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 199.25 | |||
| Temperature range, max. | 601.00 | |||
| Pvap | 2.52e-05 | kPa | 199.25 | Calculated Property |
| Pvap | 8.80e-03 | kPa | 243.89 | Calculated Property |
| Pvap | 0.37 | kPa | 288.53 | Calculated Property |
| Pvap | 4.75 | kPa | 333.17 | Calculated Property |
| Pvap | 29.39 | kPa | 377.81 | Calculated Property |
| Pvap | 114.54 | kPa | 422.44 | Calculated Property |
| Pvap | 329.74 | kPa | 467.08 | Calculated Property |
| Pvap | 775.30 | kPa | 511.72 | Calculated Property |
| Pvap | 1590.81 | kPa | 556.36 | Calculated Property |
| Pvap | 2980.28 | kPa | 601.00 | Calculated Property |
| Pvap | [2.42e-05; 2974.72] | kPa | [199.25; 601.00] |
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 | 1.08727e+02 | |||
| Coefficient B | -9.25172e+03 | |||
| Coefficient C | -1.38402e+01 | |||
| Coefficient D | 8.92111e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 199.25 | |||
| Temperature range, max. | 601.00 | |||
| Pvap | 2.42e-05 | kPa | 199.25 | Calculated Property |
| Pvap | 8.64e-03 | kPa | 243.89 | Calculated Property |
| Pvap | 0.37 | kPa | 288.53 | Calculated Property |
| Pvap | 4.74 | kPa | 333.17 | Calculated Property |
| Pvap | 29.36 | kPa | 377.81 | Calculated Property |
| Pvap | 114.46 | kPa | 422.44 | Calculated Property |
| Pvap | 329.40 | kPa | 467.08 | Calculated Property |
| Pvap | 774.07 | kPa | 511.72 | Calculated Property |
| Pvap | 1587.72 | kPa | 556.36 | Calculated Property |
| Pvap | 2974.72 | kPa | 601.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [887.76; 264.28] | kg/m3 | [199.25; 601.00] |
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 | 6.78673e+01 | |||
| Coefficient B | 2.56800e-01 | |||
| Coefficient C | 6.01000e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Temperature range, min. | 199.25 | |||
| Temperature range, max. | 601.00 | |||
| ρl | 887.76 | kg/m3 | 199.25 | Calculated Property |
| ρl | 852.86 | kg/m3 | 243.89 | Calculated Property |
| ρl | 816.27 | kg/m3 | 288.53 | Calculated Property |
| ρl | 777.55 | kg/m3 | 333.17 | Calculated Property |
| ρl | 736.11 | kg/m3 | 377.81 | Calculated Property |
| ρl | 690.98 | kg/m3 | 422.44 | Calculated Property |
| ρl | 640.52 | kg/m3 | 467.08 | Calculated Property |
| ρl | 581.40 | kg/m3 | 511.72 | Calculated Property |
| ρl | 504.61 | kg/m3 | 556.36 | Calculated Property |
| ρl | 264.28 | kg/m3 | 601.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 7.64e-07] | N/m | [199.25; 596.58] |
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 | -1.03010e-02 | |||
| Coefficient B | 6.76280e+01 | |||
| Coefficient C | -3.39710e+00 | |||
| Coefficient D | 1.09210e-03 | |||
| Coefficient E | -5.45990e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 601 K. | |||
| Temperature range, min. | 199.25 | |||
| Temperature range, max. | 596.58 | |||
| γ | 0.04 | N/m | 199.25 | Calculated Property |
| γ | 0.03 | N/m | 243.40 | Calculated Property |
| γ | 0.03 | N/m | 287.55 | Calculated Property |
| γ | 0.02 | N/m | 331.69 | Calculated Property |
| γ | 0.02 | N/m | 375.84 | Calculated Property |
| γ | 0.01 | N/m | 419.99 | Calculated Property |
| γ | 0.01 | N/m | 464.14 | Calculated Property |
| γ | 0.01 | N/m | 508.29 | Calculated Property |
| γ | 0.00 | N/m | 552.43 | Calculated Property |
| γ | 7.64e-07 | N/m | 596.58 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.12] | W/m×K | [199.25; 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 | 1.46740e+03 | |||
| Coefficient B | 1.04380e+00 | |||
| Coefficient C | 1.71300e+10 | |||
| Coefficient D | -1.53850e+11 | |||
| Temperature range, min. | 199.25 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 199.25 | Calculated Property |
| λgas | 0.01 | W/m×K | 288.22 | Calculated Property |
| λgas | 0.02 | W/m×K | 377.19 | Calculated Property |
| λgas | 0.02 | W/m×K | 466.17 | Calculated Property |
| λgas | 0.04 | W/m×K | 555.14 | Calculated Property |
| λgas | 0.05 | W/m×K | 644.11 | Calculated Property |
| λgas | 0.06 | W/m×K | 733.08 | Calculated Property |
| λgas | 0.08 | W/m×K | 822.06 | Calculated Property |
| λgas | 0.10 | W/m×K | 911.03 | Calculated Property |
| λgas | 0.12 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.18; 0.10] | W/m×K | [180.30; 480.30] |
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 | -1.82330e-01 | |||
| Coefficient B | 1.71240e+01 | |||
| Coefficient C | -1.05950e+00 | |||
| Coefficient D | -4.02980e-05 | |||
| Coefficient E | -9.95470e-07 | |||
| Temperature range, min. | 180.30 | |||
| Temperature range, max. | 480.30 | |||
| λliquid | 0.18 | W/m×K | 180.30 | Calculated Property |
| λliquid | 0.17 | W/m×K | 213.63 | Calculated Property |
| λliquid | 0.16 | W/m×K | 246.97 | Calculated Property |
| λliquid | 0.15 | W/m×K | 280.30 | Calculated Property |
| λliquid | 0.15 | W/m×K | 313.63 | Calculated Property |
| λliquid | 0.14 | W/m×K | 346.97 | Calculated Property |
| λliquid | 0.13 | W/m×K | 380.30 | Calculated Property |
| λliquid | 0.12 | W/m×K | 413.63 | Calculated Property |
| λliquid | 0.11 | W/m×K | 446.97 | Calculated Property |
| λliquid | 0.10 | W/m×K | 480.30 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Hexanone, 5-methyl-.
Mixtures
- 2-Hexanone, 5-methyl- + Propanoic acid + Water
- 2-Hexanone, 5-methyl- + Water
- 2-Hexanone, 5-methyl- + Water + Phosphoric Acid
- 2-Hexanone, 5-methyl- + Formic acid + Water
- 2-Hexanone, 5-methyl- + Butanoic acid + Water
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.
- 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.
- (Liquid + liquid) equilibria of (water + propionic acid + methyl isoamyl ketone or diisobutyl ketone or ethyl isoamyl keton) at T = 298.2 K
- Experimental study of phase equilibria in aqueous mixtures of phosphoric acid with isoamyl acetate and methyl isoamyl ketone at T = (298.2, 308.2, and 318.2) K
- Experimental and Correlational Study of Phase Equilibria in Aqueous Solutions of Formic and Butyric Acids with Isoamyl Acetate and Methyl Isoamyl Ketone at T = 298.15 K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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