- InChI
- InChI=1S/C6H12O2/c1-2-3-4-5-6(7)8/h2-5H2,1H3,(H,7,8)
- InChI Key
- FUZZWVXGSFPDMH-UHFFFAOYSA-N
- Formula
- C6H12O2
- SMILES
- CCCCCC(=O)O
- Molecular Weight1
- 116.16
- CAS
- 142-62-1
- Other Names
-
- 1-Hexanoic acid
- 1-pentanecarboxylic acid
- Butylacetic acid
- CH3(CH2)4COOH
- Capronic acid
- Hexacid 698
- Hexoic acid
- Kyselina kapronova
- NSC 8266
- Pentane-1-carboxylic acid
- Pentanecarboxylic acid
- Pentiformic acid
- Pentylformic acid
- caproic acid
- n-Caproic acid
- n-Hexoic acid
- n-Hexylic acid
- n-hexanoic acid
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- 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.
- 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.
- I : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : 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 | 0.7330 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°liquid | [-3518.00; -3490.40] | kJ/mol |
|
| ΔcH°liquid | -3494.29 ± 0.66 | kJ/mol | NIST |
| ΔcH°liquid | -3492.40 ± 0.60 | kJ/mol | NIST |
| ΔcH°liquid | -3490.40 ± 0.54 | kJ/mol | NIST |
| ΔcH°liquid | -3518.00 | kJ/mol | NIST |
| ΔcH°solid | -3522.80 | kJ/mol | NIST |
| μ | 1.57 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -338.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-515.10; -508.60] | kJ/mol |
|
| ΔfH°gas | -511.90 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -511.20 ± 1.50 | kJ/mol | NIST |
| ΔfH°gas | -508.60 ± 2.30 | kJ/mol | NIST |
| ΔfH°gas | -511.20 ± 1.50 | kJ/mol | NIST |
| ΔfH°gas | -513.00 ± 2.00 | kJ/mol | NIST |
| ΔfH°gas | -515.10 ± 1.10 | kJ/mol | NIST |
| ΔfH°gas | -512.50 ± 2.10 | kJ/mol | NIST |
| ΔfH°gas | -515.10 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | [-585.68; -581.80] | kJ/mol |
|
| ΔfH°liquid | -581.80 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -583.58 ± 0.75 | kJ/mol | NIST |
| ΔfH°liquid | -585.68 ± 0.54 | kJ/mol | NIST |
| ΔfusH° | 21.44 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [69.20; 73.20] | kJ/mol |
|
| ΔvapH° | 69.20 ± 0.90 | kJ/mol | NIST |
| ΔvapH° | 71.30 | kJ/mol | NIST |
| ΔvapH° | 73.20 ± 2.00 | kJ/mol | NIST |
| ΔvapH° | 73.20 ± 2.00 | kJ/mol | NIST |
| ΔvapH° | 71.00 ± 1.00 | kJ/mol | NIST |
| IE | 10.12 | eV | NIST |
| log10WS | -1.06 | Aq. Solubility Prediction | |
| logPoct/wat | 1.651 | Crippen Calculated Property | |
| McVol | 102.840 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [3154.44; 3377.00] | kPa |
|
| Pc | 3308.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 3200.00 | kPa | KDB |
| Pc | 3377.00 ± 40.00 | kPa | NIST |
| Pc | 3200.00 ± 100.00 | kPa | NIST |
| Pc | 3154.44 ± 90.00 | kPa | NIST |
| Ptriple | 3.17e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [158.10; 1038.00] |
|
|
| Inp | 1010.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 993.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 951.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 956.00 | NIST | |
| Inp | 988.00 | NIST | |
| Inp | 1005.51 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 959.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 948.00 | NIST | |
| Inp | 967.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 962.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 952.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 996.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 987.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1001.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 998.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 989.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 987.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 992.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 971.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 969.00 | NIST | |
| Inp | 995.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 975.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 957.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 958.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 997.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1001.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 965.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | Outlier 158.10 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 977.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 950.00 | NIST | |
| Inp | 968.00 | NIST | |
| Inp | 972.00 | NIST | |
| Inp | 981.00 | NIST | |
| Inp | 999.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 991.00 | NIST | |
| Inp | 976.00 | NIST | |
| Inp | 984.00 | NIST | |
| Inp | 970.00 | NIST | |
| Inp | 983.00 | NIST | |
| Inp | 986.00 | NIST | |
| Inp | 974.00 | NIST | |
| Inp | 961.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Inp | 990.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 964.00 | NIST | |
| Inp | Outlier 158.10 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 969.00 | NIST | |
| I | [1797.00; 1889.00] |
|
|
| I | 1841.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1858.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1815.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1836.00 | NIST | |
| I | Outlier 1807.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1839.00 | NIST | |
| I | 1824.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1831.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1838.00 | NIST | |
| I | 1838.00 | NIST | |
| I | 1810.00 | NIST | |
| I | 1838.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1823.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1843.00 | NIST | |
| I | 1813.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1858.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1816.00 | NIST | |
| I | 1827.00 | NIST | |
| I | 1823.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1873.00 | NIST | |
| I | Outlier 1803.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1829.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1816.00 | NIST | |
| I | 1849.30 | NIST | |
| I | 1825.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1813.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1853.00 | NIST | |
| I | Outlier 1889.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1845.00 | NIST | |
| I | Outlier 1884.50 | NIST | |
| I | 1834.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1856.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1819.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1822.00 | NIST | |
| I | 1823.00 | NIST | |
| I | 1831.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1838.00 | NIST | |
| I | 1858.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1866.00 | NIST | |
| I | Outlier 1884.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1838.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1845.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1838.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1832.00 | NIST | |
| I | 1828.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1832.00 | NIST | |
| I | 1817.00 | NIST | |
| I | 1814.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1824.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1842.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1848.00 | NIST | |
| I | Outlier 1800.00 | NIST | |
| I | 1820.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1843.00 | NIST | |
| I | 1842.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1845.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1828.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1838.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1858.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1858.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1842.00 | NIST | |
| I | 1860.00 | NIST | |
| I | Outlier 1804.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1832.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1814.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1849.00 | NIST | |
| I | Outlier 1797.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1832.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1861.00 | NIST | |
| I | Outlier 1802.00 | NIST | |
| I | 1832.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1826.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1812.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1838.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1815.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1845.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1852.00 | NIST | |
| I | Outlier 1808.00 | NIST | |
| I | 1829.00 | NIST | |
| I | 1812.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1856.00 | NIST | |
| I | 1845.00 | NIST | |
| I | 1871.00 | NIST | |
| I | Outlier 1807.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1844.00 | NIST | |
| I | Outlier 1807.00 | NIST | |
| I | 1866.00 | NIST | |
| I | Outlier 1807.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1871.60 | NIST | |
| I | 1820.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1853.00 | NIST | |
| I | Outlier 1807.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1845.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1845.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1850.00 | NIST | |
| I | Outlier 1885.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1816.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1826.00 | NIST | |
| I | 1813.00 | NIST | |
| I | 1821.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1845.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1832.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1832.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1839.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1839.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1821.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1828.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1829.00 | NIST | |
| I | 1857.00 | NIST | |
| I | Outlier 1809.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1822.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1817.00 | NIST | |
| I | 1845.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1813.00 | NIST | |
| I | 1832.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1839.00 | NIST | |
| I | 1817.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1810.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1816.00 | NIST | |
| I | 1849.30 | NIST | |
| I | 1874.00 | NIST | |
| I | 1856.00 | NIST | |
| I | 1822.00 | NIST | |
| Tboil | [468.15; 481.65] | K |
|
| Tboil | 478.85 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 478.40 | K | KDB |
| Tboil | 475.70 | K | NIST |
| Tboil | 478.20 | K | NIST |
| Tboil | 477.15 ± 3.00 | K | NIST |
| Tboil | 478.05 ± 0.50 | K | NIST |
| Tboil | 478.15 ± 2.00 | K | NIST |
| Tboil | 476.15 ± 2.00 | K | NIST |
| Tboil | 476.15 ± 2.00 | K | NIST |
| Tboil | 478.45 ± 0.50 | K | NIST |
| Tboil | 478.30 ± 0.50 | K | NIST |
| Tboil | 478.15 ± 2.00 | K | NIST |
| Tboil | 477.65 ± 2.00 | K | NIST |
| Tboil | 478.30 ± 0.70 | K | NIST |
| Tboil | 476.15 ± 2.00 | K | NIST |
| Tboil | 474.65 ± 3.00 | K | NIST |
| Tboil | 476.15 ± 3.00 | K | NIST |
| Tboil | 478.15 ± 2.00 | K | NIST |
| Tboil | 481.65 ± 3.00 | K | NIST |
| Tboil | 478.05 ± 1.00 | K | NIST |
| Tboil | 479.15 ± 2.00 | K | NIST |
| Tboil | 478.50 ± 0.20 | K | NIST |
| Tboil | 477.15 ± 2.00 | K | NIST |
| Tboil | 478.15 ± 2.00 | K | NIST |
| Tboil | 477.90 ± 1.50 | K | NIST |
| Tboil | 475.65 ± 3.00 | K | NIST |
| Tboil | 473.15 ± 3.00 | K | NIST |
| Tboil | 472.65 ± 3.00 | K | NIST |
| Tboil | 476.00 ± 6.00 | K | NIST |
| Tboil | 478.15 ± 2.00 | K | NIST |
| Tboil | 478.15 ± 2.00 | K | NIST |
| Tboil | 478.65 ± 3.00 | K | NIST |
| Tboil | 478.85 ± 1.50 | K | NIST |
| Tboil | 475.65 ± 3.00 | K | NIST |
| Tboil | 477.40 ± 1.50 | K | NIST |
| Tboil | 477.00 ± 3.00 | K | NIST |
| Tboil | 477.90 ± 1.50 | K | NIST |
| Tboil | 472.20 ± 1.50 | K | NIST |
| Tboil | 477.15 ± 3.00 | K | NIST |
| Tboil | 481.15 ± 4.00 | K | NIST |
| Tboil | 477.65 ± 4.00 | K | NIST |
| Tboil | 476.15 ± 5.00 | K | NIST |
| Tboil | Outlier 471.15 ± 5.00 | K | NIST |
| Tboil | Outlier 468.15 ± 5.00 | K | NIST |
| Tc | [655.10; 669.63] | K |
|
| Tc | 660.20 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 662.00 | K | KDB |
| Tc | 655.10 ± 1.00 | K | NIST |
| Tc | 663.00 ± 1.00 | K | NIST |
| Tc | 669.63 ± 3.00 | K | NIST |
| Tfus | [269.00; 271.40] | K |
|
| Tfus | 269.25 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 270.00 | K | KDB |
| Tfus | 269.90 | K | Aq. Solubility Prediction |
| Tfus | 269.70 ± 0.05 | K | NIST |
| Tfus | 269.20 ± 0.50 | K | NIST |
| Tfus | 269.00 ± 1.50 | K | NIST |
| Tfus | 269.00 ± 4.00 | K | NIST |
| Tfus | Outlier 271.40 ± 1.50 | K | NIST |
| Ttriple | [269.25; 269.71] | K |
|
| Ttriple | 269.25 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 269.71 | K | KDB |
| UQi | 4.23 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.90 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.408 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2460000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [161.07; 376.36] | J/mol×K | [298.15; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))² Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.16220e+02 | |||
| Coefficient B | 2.07080e+02 | |||
| Coefficient C | 6.86610e+02 | |||
| Coefficient D | 1.53550e+02 | |||
| Coefficient E | 1.93250e+03 | |||
| Comment | ChemSep eq 107, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 161.07 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 212.57 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 253.36 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 286.25 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 313.34 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 335.04 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 351.56 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 363.45 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 371.45 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 376.36 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [225.26; 345.68] | J/mol×K | [269.25; 478.85] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.61980e+02 | |||
| Coefficient B | 4.41160e-02 | |||
| Coefficient C | 7.09000e-04 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidHeatCapacityCp | |||
| Temperature range, min. | 269.25 | |||
| Temperature range, max. | 478.85 | |||
| Cp,liquid | 225.26 | J/mol×K | 269.25 | Calculated Property |
| Cp,liquid | 235.56 | J/mol×K | 292.54 | Calculated Property |
| Cp,liquid | 246.63 | J/mol×K | 315.83 | Calculated Property |
| Cp,liquid | 258.48 | J/mol×K | 339.12 | Calculated Property |
| Cp,liquid | 271.09 | J/mol×K | 362.41 | Calculated Property |
| Cp,liquid | 284.47 | J/mol×K | 385.69 | Calculated Property |
| Cp,liquid | 298.62 | J/mol×K | 408.98 | Calculated Property |
| Cp,liquid | 313.53 | J/mol×K | 432.27 | Calculated Property |
| Cp,liquid | 329.22 | J/mol×K | 455.56 | Calculated Property |
| Cp,liquid | 345.68 | J/mol×K | 478.85 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0058544; 0.0004019] | Pa×s | [269.25; 478.85] |
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 | -4.64020e+01 | |||
| Coefficient B | 3.44860e+03 | |||
| Coefficient C | 5.08490e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 269.25 | |||
| Temperature range, max. | 478.85 | |||
| η | 0.0058544 | Pa×s | 269.25 | Calculated Property |
| η | 0.0032200 | Pa×s | 292.54 | Calculated Property |
| η | 0.0019929 | Pa×s | 315.83 | Calculated Property |
| η | 0.0013519 | Pa×s | 339.12 | Calculated Property |
| η | 0.0009858 | Pa×s | 362.41 | Calculated Property |
| η | 0.0007617 | Pa×s | 385.69 | Calculated Property |
| η | 0.0006168 | Pa×s | 408.98 | Calculated Property |
| η | 0.0005190 | Pa×s | 432.27 | Calculated Property |
| η | 0.0004507 | Pa×s | 455.56 | Calculated Property |
| η | 0.0004019 | Pa×s | 478.85 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [64.78; 0.00] | kJ/mol | [269.25; 660.20] |
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 | 9.07460e+01 | |||
| Coefficient B | 8.92600e-01 | |||
| Coefficient C | -7.51720e-01 | |||
| Coefficient D | 3.43780e-01 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.60200e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 269.25 | |||
| Temperature range, max. | 660.20 | |||
| ΔvapH | 64.78 | kJ/mol | 269.25 | Calculated Property |
| ΔvapH | 61.21 | kJ/mol | 312.69 | Calculated Property |
| ΔvapH | 57.56 | kJ/mol | 356.13 | Calculated Property |
| ΔvapH | 53.75 | kJ/mol | 399.57 | Calculated Property |
| ΔvapH | 49.62 | kJ/mol | 443.01 | Calculated Property |
| ΔvapH | 45.00 | kJ/mol | 486.44 | Calculated Property |
| ΔvapH | 39.62 | kJ/mol | 529.88 | Calculated Property |
| ΔvapH | 32.98 | kJ/mol | 573.32 | Calculated Property |
| ΔvapH | 23.90 | kJ/mol | 616.76 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 660.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [368.34; 503.07] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.53785e+01 | |||
| Coefficient B | -4.07436e+03 | |||
| Coefficient C | -9.83480e+01 | |||
| Temperature range, min. | 368.34 | |||
| Temperature range, max. | 503.07 | |||
| Pvap | 1.33 | kPa | 368.34 | Calculated Property |
| Pvap | 2.95 | kPa | 383.31 | Calculated Property |
| Pvap | 6.01 | kPa | 398.28 | Calculated Property |
| Pvap | 11.47 | kPa | 413.25 | Calculated Property |
| Pvap | 20.64 | kPa | 428.22 | Calculated Property |
| Pvap | 35.28 | kPa | 443.19 | Calculated Property |
| Pvap | 57.68 | kPa | 458.16 | Calculated Property |
| Pvap | 90.67 | kPa | 473.13 | Calculated Property |
| Pvap | 137.66 | kPa | 488.10 | Calculated Property |
| Pvap | 202.64 | kPa | 503.07 | Calculated Property |
| Pvap | [3.17e-04; 3307.36] | kPa | [269.25; 660.20] |
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 | 9.14692e+01 | |||
| Coefficient B | -1.13940e+04 | |||
| Coefficient C | -1.02240e+01 | |||
| Coefficient D | 3.29480e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 269.25 | |||
| Temperature range, max. | 660.20 | |||
| Pvap | 3.17e-04 | kPa | 269.25 | Calculated Property |
| Pvap | 0.02 | kPa | 312.69 | Calculated Property |
| Pvap | 0.56 | kPa | 356.13 | Calculated Property |
| Pvap | 5.59 | kPa | 399.57 | Calculated Property |
| Pvap | 32.25 | kPa | 443.01 | Calculated Property |
| Pvap | 125.55 | kPa | 486.44 | Calculated Property |
| Pvap | 367.85 | kPa | 529.88 | Calculated Property |
| Pvap | 876.04 | kPa | 573.32 | Calculated Property |
| Pvap | 1795.02 | kPa | 616.76 | Calculated Property |
| Pvap | 3307.36 | kPa | 660.20 | Calculated Property |
| Pvap | [2.67e-04; 3332.50] | kPa | [270.15; 667.00] |
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 | 1.28361e+02 | |||
| Coefficient B | -1.31241e+04 | |||
| Coefficient C | -1.57781e+01 | |||
| Coefficient D | 4.55839e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 270.15 | |||
| Temperature range, max. | 667.00 | |||
| Pvap | 2.67e-04 | kPa | 270.15 | Calculated Property |
| Pvap | 0.03 | kPa | 314.24 | Calculated Property |
| Pvap | 0.62 | kPa | 358.34 | Calculated Property |
| Pvap | 6.41 | kPa | 402.43 | Calculated Property |
| Pvap | 36.92 | kPa | 446.53 | Calculated Property |
| Pvap | 141.57 | kPa | 490.62 | Calculated Property |
| Pvap | 406.22 | kPa | 534.72 | Calculated Property |
| Pvap | 944.14 | kPa | 578.81 | Calculated Property |
| Pvap | 1879.00 | kPa | 622.91 | Calculated Property |
| Pvap | 3332.50 | kPa | 667.00 | Calculated Property |
| Pvap | [1.26; 46.33] | kPa | [371.30; 452.30] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46180e+01 | |||
| Coefficient B | -3.48316e+03 | |||
| Coefficient C | -1.29255e+02 | |||
| Reference | Rose, Acciarri, et al., 1957 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 371.30 | |||
| Temperature range, max. | 452.30 | |||
| Pvap | 1.26 | kPa | 371.30 | Calculated Property |
| Pvap | 2.10 | kPa | 380.30 | Calculated Property |
| Pvap | 3.40 | kPa | 389.30 | Calculated Property |
| Pvap | 5.32 | kPa | 398.30 | Calculated Property |
| Pvap | 8.09 | kPa | 407.30 | Calculated Property |
| Pvap | 11.98 | kPa | 416.30 | Calculated Property |
| Pvap | 17.33 | kPa | 425.30 | Calculated Property |
| Pvap | 24.52 | kPa | 434.30 | Calculated Property |
| Pvap | 34.01 | kPa | 443.30 | Calculated Property |
| Pvap | 46.33 | kPa | 452.30 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [940.46; 285.12] | kg/m3 | [269.25; 660.20] |
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 | 7.29856e+01 | |||
| Coefficient B | 2.55980e-01 | |||
| Coefficient C | 6.60200e+02 | |||
| Coefficient D | 2.53040e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 269.25 | |||
| Temperature range, max. | 660.20 | |||
| ρl | 940.46 | kg/m3 | 269.25 | Calculated Property |
| ρl | 908.08 | kg/m3 | 312.69 | Calculated Property |
| ρl | 873.79 | kg/m3 | 356.13 | Calculated Property |
| ρl | 837.14 | kg/m3 | 399.57 | Calculated Property |
| ρl | 797.46 | kg/m3 | 443.01 | Calculated Property |
| ρl | 753.68 | kg/m3 | 486.44 | Calculated Property |
| ρl | 703.96 | kg/m3 | 529.88 | Calculated Property |
| ρl | 644.58 | kg/m3 | 573.32 | Calculated Property |
| ρl | 565.31 | kg/m3 | 616.76 | Calculated Property |
| ρl | 285.12 | kg/m3 | 660.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.00] | N/m | [269.25; 660.20] |
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 γ in N/m, T in K | |||
| Coefficient A | 5.40100e-02 | |||
| Coefficient B | 1.12330e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.60200e+02 | |||
| Comment | ChemSep eq 106, SurfaceTension | |||
| Temperature range, min. | 269.25 | |||
| Temperature range, max. | 660.20 | |||
| γ | 0.03 | N/m | 269.25 | Calculated Property |
| γ | 0.03 | N/m | 312.69 | Calculated Property |
| γ | 0.02 | N/m | 356.13 | Calculated Property |
| γ | 0.02 | N/m | 399.57 | Calculated Property |
| γ | 0.02 | N/m | 443.01 | Calculated Property |
| γ | 0.01 | N/m | 486.44 | Calculated Property |
| γ | 0.01 | N/m | 529.88 | Calculated Property |
| γ | 0.01 | N/m | 573.32 | Calculated Property |
| γ | 0.00 | N/m | 616.76 | Calculated Property |
| γ | 0.00 | N/m | 660.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.03; 0.04] | W/m×K | [478.85; 641.42] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 1.20490e+09 | |||
| Coefficient B | -4.00590e+00 | |||
| Coefficient C | -1.66880e+03 | |||
| Coefficient D | 7.22550e+05 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 478.85 | |||
| Temperature range, max. | 641.42 | |||
| λ | 0.03 | W/m×K | 478.85 | Calculated Property |
| λ | 0.03 | W/m×K | 496.91 | Calculated Property |
| λ | 0.03 | W/m×K | 514.98 | Calculated Property |
| λ | 0.03 | W/m×K | 533.04 | Calculated Property |
| λ | 0.04 | W/m×K | 551.10 | Calculated Property |
| λ | 0.04 | W/m×K | 569.17 | Calculated Property |
| λ | 0.04 | W/m×K | 587.23 | Calculated Property |
| λ | 0.04 | W/m×K | 605.29 | Calculated Property |
| λ | 0.04 | W/m×K | 623.36 | Calculated Property |
| λ | 0.04 | W/m×K | 641.42 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.15; 0.10] | W/m×K | [269.25; 603.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ in W/m×K, T in K | |||
| Coefficient A | 1.85500e-01 | |||
| Coefficient B | -1.46000e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidThermalConductivity | |||
| Temperature range, min. | 269.25 | |||
| Temperature range, max. | 603.15 | |||
| λ | 0.15 | W/m×K | 269.25 | Calculated Property |
| λ | 0.14 | W/m×K | 306.35 | Calculated Property |
| λ | 0.14 | W/m×K | 343.45 | Calculated Property |
| λ | 0.13 | W/m×K | 380.55 | Calculated Property |
| λ | 0.12 | W/m×K | 417.65 | Calculated Property |
| λ | 0.12 | W/m×K | 454.75 | Calculated Property |
| λ | 0.11 | W/m×K | 491.85 | Calculated Property |
| λ | 0.11 | W/m×K | 528.95 | Calculated Property |
| λ | 0.10 | W/m×K | 566.05 | Calculated Property |
| λ | 0.10 | W/m×K | 603.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Hexanoic acid.
Mixtures
- Hexanoic acid + Cyclohexane
- 1-Octanol + Hexanoic acid + Water
- Hexanoic acid + 1-Hexanol
- Formamide, N,N-dimethyl- + Hexanoic acid
- Hexanoic acid + Dimethyl Sulfoxide
- Hexanoic acid + Propanoic acid
- Hexanoic acid + Propanoic acid, 2-methyl-
- Hexanoic acid + Pentanoic acid
- Heptanoic acid + Hexanoic acid
- Hexanoic acid + 2-Propenoic acid + Water
- Hexanoic acid + Water
Sources
- KDB Vapor Pressure Data
- 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 for ternary systems of (water + carboxylic acid + 1-octanol) at 293.15 K: modeling phase equilibria using a solvatochromic approach
- Vapor-liquid equilibrium measurements and modeling for the cyclohexane + n-hexanoic acid binary system
- Vapour-liquid equilibrium of propionic acid + caproic acid, isobutyric acid + caproic acid, valeric acid + caproic acid and caproic acid + enanthoic acid binary mixtures
- (Liquid + liquid) equilibria in {water + acrylic acid + (1-butanol, or 2-butanol, or 1-pentanol)} systems at T = 293.2 K, T = 303.2 K, and T = 313.2 K and atmospheric pressure
- Excess molar enthalpies of binary systems containing 2-octanone, hexanoic acid, or octanoic acid at T = 298.15 K
- Liquid-liquid equilibria and density data for pseudoternary systems of refined soybean oil + (hexanal, or heptanal, or butyric acid, or valeric acid, or caproic acid, or caprylic acid) + dimethyl sulfoxide at 298.15 K
- Effect of temperature on the dilution enthalpies of carboxylic acids in aqueous solutions
- Density, Viscosity, and Thermal Conductivity of Eight Carboxylic Acids from (290.3 to 473.4) K
- Liquid-Liquid Equilibria for Ternary Mixtures of gamma-Valerolactone + n-Tetradecane + (Butanoic Acid or Hexanoic Acid or Methyl Myristate) at 298.15 K
- Subatmospheric Vapor Pressure Curves for Propionic Acid, Butyric Acid, Isobutyric Acid, Valeric Acid, Isovaleric Acid, Hexanoic Acid, and Heptanoic Acid
- Apparent Molar Volume and Surface Tension of Dilute Aqueous Solutions of Carboxylic Acids
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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