- InChI
- InChI=1S/C9H18O/c1-7(2)5-9(10)6-8(3)4/h7-8H,5-6H2,1-4H3
- InChI Key
- PTTPXKJBFFKCEK-UHFFFAOYSA-N
- Formula
- C9H18O
- SMILES
- CC(C)CC(=O)CC(C)C
- Molecular Weight1
- 142.24
- CAS
- 108-83-8
- Other Names
-
- (iso-C4H9)2CO
- 2,6-Dimethyl-heptan-4-on
- 2,6-Dimethylheptan-4-one
- 2,6-Dimetil-eptan-4-one
- 2,6-dimethyl-4-heptanone
- 2,6-dimethyl-4-heptanone (diisobutyl ketone)
- DIBK
- Di-isobutylcetone
- Diisobutilchetone
- Diisobutylketon
- Isovalerone
- NSC 15136
- UN 1157
- Valerone
- diisobutyl ketone
- isobutyl ketone
- s-diisopropylacetone
- sym-Diisopropylacetone
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- 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).
- 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).
- ΔfH°liquid : Liquid 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.
- 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.
- 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 | 0.5116 | ChemSep v8.3 pure component data Compiled value | |
| Tig | 669.15 | K | NCMS SOLV-DB |
| ΔcH°liquid | -5705.50 ± 1.10 | kJ/mol | NIST |
| μ | 2.66 | debye | ChemSep v8.3 pure component data Compiled value |
| Tflash,cc | 322.15 | K | NCMS SOLV-DB |
| ΔfG° | -113.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-357.70; -357.60] | kJ/mol |
|
| ΔfH°gas | -357.60 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -357.70 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -408.60 ± 1.20 | kJ/mol | NIST |
| ΔfusH° | 13.62 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [50.90; 51.00] | kJ/mol |
|
| ΔvapH° | 50.92 | kJ/mol | NCMS SOLV-DB |
| ΔvapH° | 51.00 | kJ/mol | NIST |
| ΔvapH° | 50.92 ± 0.04 | kJ/mol | NIST |
| ΔvapH° | 50.90 ± 0.10 | kJ/mol | NIST |
| IE | [8.98; 9.04] | eV |
|
| IE | 9.01 ± 0.03 | eV | NIST |
| IE | 8.98 ± 0.01 | eV | NIST |
| IE | 9.04 ± 0.03 | eV | NIST |
| log10WS | -2.99 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.646 | NCMS SOLV-DB | |
| McVol | 139.240 | 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 | 2530.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| pKa | 21.00 | NCMS SOLV-DB | |
| Ptriple | 2.50e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [935.00; 999.00] |
|
|
| Inp | 961.00 | NIST | |
| Inp | 954.70 | NIST | |
| Inp | 935.00 | NIST | |
| Inp | 943.00 | NIST | |
| Inp | 962.10 | NIST | |
| Inp | 951.20 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 945.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 955.00 | NIST | |
| Inp | Outlier 999.00 | NIST | |
| Inp | 953.00 | NIST | |
| Inp | 954.70 | NIST | |
| Inp | 962.10 | NIST | |
| Ip | [1162.00; 1207.00] |
|
|
| Ip | 1189.50 | NIST | |
| Ip | 1178.00 | NIST | |
| Ip | 1207.00 | NIST | |
| Ip | 1162.00 | NIST | |
| Ip | 1207.00 | NIST | |
| Ip | 1207.00 | NIST | |
| Tboil | [397.15; 442.60] | K |
|
| Tboil | 441.40 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 441.39 | K | NCMS SOLV-DB |
| Tboil | 442.60 | K | NIST |
| Tboil | 442.55 | K | NIST |
| Tboil | Outlier 397.15 ± 1.00 | K | NIST |
| Tboil | 442.50 ± 0.60 | K | NIST |
| Tboil | 442.50 ± 0.80 | K | NIST |
| Tboil | 442.50 ± 1.00 | K | NIST |
| Tboil | 441.30 ± 1.50 | K | NIST |
| Tboil | 441.20 ± 2.00 | K | NIST |
| Tboil | 441.20 ± 0.60 | K | NIST |
| Tboil | 441.39 ± 0.10 | K | NIST |
| Tboil | 442.00 ± 8.00 | K | NIST |
| Tboil | 438.15 ± 1.50 | K | NIST |
| Tboil | 441.00 ± 3.00 | K | NIST |
| Tboil | 438.90 ± 5.00 | K | NIST |
| Tboil | 439.00 ± 6.00 | K | NIST |
| Tboil | 438.00 ± 5.00 | K | NIST |
| Tboil | 438.15 ± 2.00 | K | NIST |
| Tc | 620.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [227.00; 231.70] | K |
|
| Tfus | 231.40 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 227.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 227.11 | K | NCMS SOLV-DB |
| Tfus | 231.65 | K | NIST |
| Tfus | 231.60 ± 3.00 | K | NIST |
| Tfus | 227.00 ± 0.60 | K | NIST |
| Tfus | 227.00 ± 0.60 | K | NIST |
| Tfus | 231.70 ± 2.00 | K | NIST |
| Tfus | 227.11 ± 0.07 | K | NIST |
| Ttriple | 227.17 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 5.57 | ChemSep v8.3 pure component data Compiled value | |
| URi | 6.62 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.522 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2530000 | 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 |
|---|---|---|---|---|
| Cp,liquid | 297.30 | J/mol×K | 298.15 | NIST |
| η | 0.0009030 | Pa×s | 298.15 | NCMS SOLV-DB |
| ΔvapH | [38.60; 49.80] | kJ/mol | [308.00; 393.50] |
|
| ΔvapH | 49.80 ± 0.10 | kJ/mol | 308.00 | NIST |
| ΔvapH | 49.30 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 48.40 ± 0.10 | kJ/mol | 323.00 | NIST |
| ΔvapH | 47.90 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 47.10 ± 0.10 | kJ/mol | 338.00 | NIST |
| ΔvapH | 46.60 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 46.10 ± 0.10 | kJ/mol | 348.00 | NIST |
| ΔvapH | 45.20 ± 0.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 38.60 | kJ/mol | 379.30 | NIST |
| ΔvapH | 46.80 | kJ/mol | 393.50 | NIST |
| Pvap | 0.22 | kPa | 298.15 | NCMS SOLV-DB |
| n0 | [1.41100; 1.41550] | [293.15; 298.15] |
|
|
| n0 | 1.41550 | 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 | 1.41100 | 298.15 | NCMS SOLV-DB | |
| ρl | [792.50; 809.04] | kg/m3 | [293.20; 313.20] |
|
| ρl | 809.04 | kg/m3 | 293.20 | Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents |
| ρl | 792.50 | kg/m3 | 313.20 | Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and different solvents |
| γ | 0.02 | N/m | 298.15 | NCMS SOLV-DB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [174.92; 543.34] | J/mol×K | [227.17; 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 | 1.18320e+02 | |||
| Coefficient B | -5.05350e+02 | |||
| Coefficient C | 6.20224e+00 | |||
| Coefficient D | 2.80360e-04 | |||
| Coefficient E | -1.03890e-07 | |||
| Temperature range, min. | 227.17 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 174.92 | J/mol×K | 227.17 | Calculated Property |
| Cp,gas | 255.38 | J/mol×K | 368.60 | Calculated Property |
| Cp,gas | 324.22 | J/mol×K | 510.02 | Calculated Property |
| Cp,gas | 379.46 | J/mol×K | 651.45 | Calculated Property |
| Cp,gas | 423.79 | J/mol×K | 792.87 | Calculated Property |
| Cp,gas | 459.57 | J/mol×K | 934.30 | Calculated Property |
| Cp,gas | 488.44 | J/mol×K | 1075.72 | Calculated Property |
| Cp,gas | 511.55 | J/mol×K | 1217.15 | Calculated Property |
| Cp,gas | 529.66 | J/mol×K | 1358.57 | Calculated Property |
| Cp,gas | 543.34 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [286.93; 378.26] | J/mol×K | [307.50; 457.50] |
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 | 8.58340e+01 | |||
| Coefficient B | -1.02600e+02 | |||
| Coefficient C | 4.79424e+00 | |||
| Coefficient D | 3.39780e-03 | |||
| Coefficient E | -2.13210e-06 | |||
| Temperature range, min. | 307.50 | |||
| Temperature range, max. | 457.50 | |||
| Cp,liquid | 286.93 | J/mol×K | 307.50 | Calculated Property |
| Cp,liquid | 297.53 | J/mol×K | 324.17 | Calculated Property |
| Cp,liquid | 308.04 | J/mol×K | 340.83 | Calculated Property |
| Cp,liquid | 318.47 | J/mol×K | 357.50 | Calculated Property |
| Cp,liquid | 328.79 | J/mol×K | 374.17 | Calculated Property |
| Cp,liquid | 338.99 | J/mol×K | 390.83 | Calculated Property |
| Cp,liquid | 349.06 | J/mol×K | 407.50 | Calculated Property |
| Cp,liquid | 358.98 | J/mol×K | 424.17 | Calculated Property |
| Cp,liquid | 368.72 | J/mol×K | 440.83 | Calculated Property |
| Cp,liquid | 378.26 | J/mol×K | 457.50 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0053987; 0.0002056] | Pa×s | [227.17; 492.00] |
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 | -7.46920e+01 | |||
| Coefficient B | 4.01860e+03 | |||
| Coefficient C | 9.60180e+00 | |||
| Coefficient D | -6.12160e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 227.17 | |||
| Temperature range, max. | 492.00 | |||
| η | 0.0053987 | Pa×s | 227.17 | Calculated Property |
| η | 0.0020958 | Pa×s | 256.60 | Calculated Property |
| η | 0.0010761 | Pa×s | 286.02 | Calculated Property |
| η | 0.0006668 | Pa×s | 315.45 | Calculated Property |
| η | 0.0004701 | Pa×s | 344.87 | Calculated Property |
| η | 0.0003626 | Pa×s | 374.30 | Calculated Property |
| η | 0.0002981 | Pa×s | 403.72 | Calculated Property |
| η | 0.0002562 | Pa×s | 433.15 | Calculated Property |
| η | 0.0002271 | Pa×s | 462.57 | Calculated Property |
| η | 0.0002056 | Pa×s | 492.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [55.03; 9.51] | kJ/mol | [227.17; 615.00] |
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 | 4.91610e+01 | |||
| Coefficient B | -1.65090e+00 | |||
| Coefficient C | 5.89370e+00 | |||
| Coefficient D | -6.63070e+00 | |||
| Coefficient E | 2.73540e+00 | |||
| Critical temperature, Tc (K) | 6.20000e+02 | |||
| Temperature range, min. | 227.17 | |||
| Temperature range, max. | 615.00 | |||
| ΔvapH | 55.03 | kJ/mol | 227.17 | Calculated Property |
| ΔvapH | 52.51 | kJ/mol | 270.26 | Calculated Property |
| ΔvapH | 49.60 | kJ/mol | 313.35 | Calculated Property |
| ΔvapH | 46.48 | kJ/mol | 356.45 | Calculated Property |
| ΔvapH | 43.18 | kJ/mol | 399.54 | Calculated Property |
| ΔvapH | 39.61 | kJ/mol | 442.63 | Calculated Property |
| ΔvapH | 35.54 | kJ/mol | 485.72 | Calculated Property |
| ΔvapH | 30.47 | kJ/mol | 528.82 | Calculated Property |
| ΔvapH | 23.38 | kJ/mol | 571.91 | Calculated Property |
| ΔvapH | 9.51 | kJ/mol | 615.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [330.63; 467.75] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.50856e+01 | |||
| Coefficient B | -3.94760e+03 | |||
| Coefficient C | -6.38620e+01 | |||
| Temperature range, min. | 330.63 | |||
| Temperature range, max. | 467.75 | |||
| Pvap | 1.33 | kPa | 330.63 | Calculated Property |
| Pvap | 2.97 | kPa | 345.87 | Calculated Property |
| Pvap | 6.08 | kPa | 361.10 | Calculated Property |
| Pvap | 11.61 | kPa | 376.34 | Calculated Property |
| Pvap | 20.90 | kPa | 391.57 | Calculated Property |
| Pvap | 35.69 | kPa | 406.81 | Calculated Property |
| Pvap | 58.23 | kPa | 422.04 | Calculated Property |
| Pvap | 91.29 | kPa | 437.28 | Calculated Property |
| Pvap | 138.16 | kPa | 452.51 | Calculated Property |
| Pvap | 202.67 | kPa | 467.75 | Calculated Property |
| Pvap | [2.36e-04; 2365.22] | kPa | [227.17; 615.00] |
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 | 1.15271e+02 | |||
| Coefficient B | -1.00643e+04 | |||
| Coefficient C | -1.47018e+01 | |||
| Coefficient D | 8.65215e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 227.17 | |||
| Temperature range, max. | 615.00 | |||
| Pvap | 2.36e-04 | kPa | 227.17 | Calculated Property |
| Pvap | 0.03 | kPa | 270.26 | Calculated Property |
| Pvap | 0.61 | kPa | 313.35 | Calculated Property |
| Pvap | 5.72 | kPa | 356.45 | Calculated Property |
| Pvap | 29.76 | kPa | 399.54 | Calculated Property |
| Pvap | 104.98 | kPa | 442.63 | Calculated Property |
| Pvap | 284.66 | kPa | 485.72 | Calculated Property |
| Pvap | 644.43 | kPa | 528.82 | Calculated Property |
| Pvap | 1288.27 | kPa | 571.91 | Calculated Property |
| Pvap | 2365.22 | kPa | 615.00 | Calculated Property |
| Pvap | [2.43e-04; 2359.43] | kPa | [227.17; 615.00] |
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 | 1.12806e+02 | |||
| Coefficient B | -9.95574e+03 | |||
| Coefficient C | -1.43270e+01 | |||
| Coefficient D | 8.33011e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 227.17 | |||
| Temperature range, max. | 615.00 | |||
| Pvap | 2.43e-04 | kPa | 227.17 | Calculated Property |
| Pvap | 0.03 | kPa | 270.26 | Calculated Property |
| Pvap | 0.61 | kPa | 313.35 | Calculated Property |
| Pvap | 5.73 | kPa | 356.45 | Calculated Property |
| Pvap | 29.81 | kPa | 399.54 | Calculated Property |
| Pvap | 105.16 | kPa | 442.63 | Calculated Property |
| Pvap | 285.20 | kPa | 485.72 | Calculated Property |
| Pvap | 645.37 | kPa | 528.82 | Calculated Property |
| Pvap | 1288.38 | kPa | 571.91 | Calculated Property |
| Pvap | 2359.43 | kPa | 615.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [853.56; 449.88] | kg/m3 | [227.17; 594.59] |
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 | 5.38089e+01 | |||
| Coefficient B | 2.32310e-01 | |||
| Coefficient C | 6.20000e+02 | |||
| Coefficient D | 2.46640e-01 | |||
| Temperature range, min. | 227.17 | |||
| Temperature range, max. | 594.59 | |||
| ρl | 853.56 | kg/m3 | 227.17 | Calculated Property |
| ρl | 824.35 | kg/m3 | 267.99 | Calculated Property |
| ρl | 793.60 | kg/m3 | 308.82 | Calculated Property |
| ρl | 760.97 | kg/m3 | 349.64 | Calculated Property |
| ρl | 725.98 | kg/m3 | 390.47 | Calculated Property |
| ρl | 687.91 | kg/m3 | 431.29 | Calculated Property |
| ρl | 645.57 | kg/m3 | 472.12 | Calculated Property |
| ρl | 596.83 | kg/m3 | 512.94 | Calculated Property |
| ρl | 536.96 | kg/m3 | 553.77 | Calculated Property |
| ρl | 449.88 | kg/m3 | 594.59 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 1.21e-04] | N/m | [227.17; 615.00] |
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 | -9.44570e-03 | |||
| Coefficient B | 5.80920e+01 | |||
| Coefficient C | -3.51490e+00 | |||
| Coefficient D | 1.16420e-03 | |||
| Coefficient E | -5.14250e-06 | |||
| Temperature range, min. | 227.17 | |||
| Temperature range, max. | 615.00 | |||
| γ | 0.03 | N/m | 227.17 | Calculated Property |
| γ | 0.03 | N/m | 270.26 | Calculated Property |
| γ | 0.02 | N/m | 313.35 | Calculated Property |
| γ | 0.02 | N/m | 356.45 | Calculated Property |
| γ | 0.01 | N/m | 399.54 | Calculated Property |
| γ | 0.01 | N/m | 442.63 | Calculated Property |
| γ | 0.01 | N/m | 485.72 | Calculated Property |
| γ | 0.01 | N/m | 528.82 | Calculated Property |
| γ | 0.00 | N/m | 571.91 | Calculated Property |
| γ | 1.21e-04 | N/m | 615.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.12] | W/m×K | [227.17; 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 | -3.80230e+05 | |||
| Coefficient B | 2.48400e-02 | |||
| Coefficient C | 1.33630e+08 | |||
| Coefficient D | -3.95230e+12 | |||
| Temperature range, min. | 227.17 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 227.17 | Calculated Property |
| λgas | 0.01 | W/m×K | 313.04 | Calculated Property |
| λgas | 0.02 | W/m×K | 398.91 | Calculated Property |
| λgas | 0.03 | W/m×K | 484.78 | Calculated Property |
| λgas | 0.04 | W/m×K | 570.65 | Calculated Property |
| λgas | 0.05 | W/m×K | 656.52 | Calculated Property |
| λgas | 0.06 | W/m×K | 742.39 | Calculated Property |
| λgas | 0.08 | W/m×K | 828.26 | Calculated Property |
| λgas | 0.10 | W/m×K | 914.13 | Calculated Property |
| λgas | 0.12 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.18; 0.09] | W/m×K | [184.50; 492.00] |
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 | -1.20880e-01 | |||
| Coefficient B | 2.22500e+01 | |||
| Coefficient C | -1.29740e+00 | |||
| Coefficient D | 8.89030e-06 | |||
| Coefficient E | -1.20790e-06 | |||
| Temperature range, min. | 184.50 | |||
| Temperature range, max. | 492.00 | |||
| λliquid | 0.18 | W/m×K | 184.50 | Calculated Property |
| λliquid | 0.17 | W/m×K | 218.67 | Calculated Property |
| λliquid | 0.16 | W/m×K | 252.83 | Calculated Property |
| λliquid | 0.15 | W/m×K | 287.00 | Calculated Property |
| λliquid | 0.14 | W/m×K | 321.17 | Calculated Property |
| λliquid | 0.13 | W/m×K | 355.33 | Calculated Property |
| λliquid | 0.12 | W/m×K | 389.50 | Calculated Property |
| λliquid | 0.11 | W/m×K | 423.67 | Calculated Property |
| λliquid | 0.10 | W/m×K | 457.83 | Calculated Property |
| λliquid | 0.09 | W/m×K | 492.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 4-Heptanone, 2,6-dimethyl-.
Mixtures
- 4-Heptanone, 2,6-dimethyl- + Propanoic acid + Water
- 4-Heptanone, 2,6-dimethyl- + Water
- 4-Heptanone, 2,6-dimethyl- + 2-Heptanone, 4,6-dimethyl-
- 4-Heptanone, 2,6-dimethyl- + Acetic acid + Water
- 4-Heptanone, 2,6-dimethyl- + Ethanedioic acid + Water
- 4-Heptanone, 2,6-dimethyl- + Maleic 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).
- Cheméo Relay (1.0)
- 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.
- Crippen Method
- (Liquid + liquid) equilibria of (water + propionic acid + methyl isoamyl ketone or diisobutyl ketone or ethyl isoamyl keton) at T = 298.2 K
- Quaternary phase equilibrium of water-carboxylic acid mixture (formic-propionic acid or acetic-propionic acid)-solvent liquid systems at 298.15 K
- Liquid-liquid equilibrium data and thermophysical properties for ternary systems composed of water, acetic acid and 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
- Comparison of Extractability of Oxalic Acid from Dilute Aqueous Solutions Using Dioctylamine and Trioctylphosphine Oxide
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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