- InChI
- InChI=1S/C7H8O2/c1-9-7-5-3-2-4-6(7)8/h2-5,8H,1H3
- InChI Key
- LHGVFZTZFXWLCP-UHFFFAOYSA-N
- Formula
- C7H8O2
- SMILES
- COc1ccccc1O
- Molecular Weight1
- 124.14
- CAS
- 90-05-1
- Other Names
-
- 1-Hydroxy-2-methoxybenzene
- 2-Hydroxyanisole
- 2-Methoxy phenol (guiacol)
- 2-methoxyphenol
- 2-methoxyphenol (guaiacol)
- Anastil
- Catechol monomethyl ether
- Guaiastil
- Guaicol
- Guaicolina
- Guajakol
- Guajol
- Guasol
- Methylcatachol
- Methylcatechol
- NSC 3815
- O-Methyl catechol
- Phenol, o-methoxy-
- Pyrocatechol monomethyl ether
- Pyroguaiac acid
- guaiacol
- guaiacol (2-methoxyphenol)
- guiacol
- o-Guaiacol
- o-Guiacol
- o-hydroxyanisole
- o-methoxyphenol
- ortho-Guaiacol
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- 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.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5367 | Relay (1.0) Calculated Property | |
| ΔfG° | -139.15 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -243.38 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 14.90 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 62.60 ± 0.50 | kJ/mol | NIST |
| IE | 8.12 | eV | Relay (1.0) Calculated Property |
| log10WS | [-1.96; -1.96] |
|
|
| log10WS | -1.96 | Aq. Solubility Prediction | |
| log10WS | -1.96 | Estimated Solubility | |
| logPoct/wat | 1.401 | Crippen Calculated Property | |
| McVol | 97.470 | ml/mol | McGowan Calculated Property |
| Pc | 4910.80 | kPa | Joback Calculated Property |
| Inp | [180.07; 1114.00] |
|
|
| Inp | 1066.80 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1101.00 | NIST | |
| Inp | 1089.05 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1060.10 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1102.40 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1092.40 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1088.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | Outlier 180.07 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | Outlier 180.07 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1066.80 | NIST | |
| I | [1814.00; 1909.00] |
|
|
| I | 1880.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1889.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1849.00 | NIST | |
| I | Outlier 1823.00 | NIST | |
| I | 1875.00 | NIST | |
| I | Outlier 1815.00 | NIST | |
| I | Outlier 1823.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1859.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1856.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1897.50 | NIST | |
| I | 1846.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1859.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1829.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1859.00 | NIST | |
| I | 1826.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1858.00 | NIST | |
| I | 1838.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1859.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1859.00 | NIST | |
| I | 1885.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1892.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1883.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1879.00 | NIST | |
| I | 1831.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1884.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1847.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1840.00 | NIST | |
| I | Outlier 1815.00 | NIST | |
| I | 1859.00 | NIST | |
| I | Outlier 1816.00 | NIST | |
| I | Outlier 1815.00 | NIST | |
| I | 1863.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1858.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1889.00 | NIST | |
| I | 1884.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1838.00 | NIST | |
| I | 1843.00 | NIST | |
| I | 1859.00 | NIST | |
| I | 1859.00 | NIST | |
| I | 1843.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1842.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1859.00 | NIST | |
| I | Outlier 1909.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1859.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1890.00 | NIST | |
| I | Outlier 1899.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1831.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1859.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1850.00 | NIST | |
| I | Outlier 1814.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1883.00 | NIST | |
| I | 1884.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1865.00 | NIST | |
| I | Outlier 1815.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1843.00 | NIST | |
| I | 1850.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1860.00 | NIST | |
| Tboil | [478.10; 478.30] | K |
|
| Tboil | 478.10 | K | Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa |
| Tboil | 478.25 | K | Isobaric (vapour + liquid) equilibria of binary systems containing butyl acetate for the separation of methoxy aromatic compounds (anisole and guaiacol) from biomass fast pyrolysis oil |
| Tboil | 478.20 | K | NIST |
| Tboil | 478.20 ± 0.60 | K | NIST |
| Tboil | 478.20 ± 0.50 | K | NIST |
| Tboil | 478.30 ± 0.50 | K | NIST |
| Tboil | 478.15 ± 1.00 | K | NIST |
| Tc | 708.90 | K | Relay (1.0) Calculated Property |
| Tfus | [301.15; 302.65] | K |
|
| Tfus | 302.65 | K | Aq. Solubility Prediction |
| Tfus | 301.15 ± 0.40 | K | NIST |
| Tfus | 301.25 ± 0.40 | K | NIST |
| Tfus | 301.45 ± 0.60 | K | NIST |
| Vc | 0.339 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [358.42; 506.24] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.61703e+01 | |||
| Coefficient B | -5.07444e+03 | |||
| Coefficient C | -3.89280e+01 | |||
| Temperature range, min. | 358.42 | |||
| Temperature range, max. | 506.24 | |||
| Pvap | 1.33 | kPa | 358.42 | Calculated Property |
| Pvap | 2.90 | kPa | 374.84 | Calculated Property |
| Pvap | 5.86 | kPa | 391.27 | Calculated Property |
| Pvap | 11.13 | kPa | 407.69 | Calculated Property |
| Pvap | 20.01 | kPa | 424.12 | Calculated Property |
| Pvap | 34.30 | kPa | 440.54 | Calculated Property |
| Pvap | 56.35 | kPa | 456.97 | Calculated Property |
| Pvap | 89.17 | kPa | 473.39 | Calculated Property |
| Pvap | 136.45 | kPa | 489.82 | Calculated Property |
| Pvap | 202.65 | kPa | 506.24 | Calculated Property |
Similar Compounds
Find more compounds similar to Phenol, 2-methoxy-.
Mixtures
- Phenol, 2-methoxy- + Methane
- Phenol, 2-methoxy- + Acetic acid, butyl ester
- Phenol, 2-methoxy- + Acetonitrile
- Phenol, 2-methoxy- + Tetrahydrofuran
- Phenol, 2-methoxy- + Ethanol
- Phenol, 2-methoxy- + Water
- Phenol, 2-methoxy- + Anisole
- Phenol, 2-methoxy- + Isopropyl acetate + Water
- Phenol, 2-methoxy- + Benzene, 1,2-dimethoxy-
- 2-Propanol, 2-methyl- + Phenol, 2-methoxy-
- Phenol, 2-methoxy- + Morpholine
- Phenol, 2-methoxy- + Methyl Isobutyl Ketone + Water
- Phenol, 2-methoxy- + Choline chloride
- Phenol, 2-methoxy- + Diethylamine, hydrochloride
- Phenol, 2-methoxy- + Choline chloride + Carbon dioxide
- Phenol, 2-methoxy- + Carbon dioxide + Diethylamine, hydrochloride
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Isobaric vapour + liquid equilibria for three binary systems (toluene + anisole, nbutylbenzene + anisole, and guaiacol + anisole) at 101.33 kPa
- Extraction of phenolic compounds from aqueous solution using choline bis(trifluoromethylsulfonyl)imide
- Phase equilibria of phenolic compounds in water or ethanol
- Guaiacol and its mixtures: new data and predictive models Part 1: Phase equilibrium
- Guaiacol and its mixtures: new data and predictive models Part 2: Gibbs energy of solvation
- Liquid-liquid equilibria of water + solutes (acetic acid/ acetol/furfural/guaiacol/methanol/phenol/propanal) + solvents (isopropyl acetate/toluene) ternary systems for pyrolysis oil fractionation
- Isobaric (vapour + liquid) equilibria of binary systems containing butyl acetate for the separation of methoxy aromatic compounds (anisole and guaiacol) from biomass fast pyrolysis oil
- Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
- Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
- Analysis of solute-pyridine intermolecular interactions based on experimental enthalpies of solution and enthalpies of solvation of solutes dissolved in pyridine
- Liquid-Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass
- Solubilities and Thermodynamic Properties of Carbon Dioxide in Guaiacol-Based Deep Eutectic Solvents
- 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
- Thermochemical Study of the Methoxy- and Dimethoxyphenol Isomers
- Isothermal Vapor-Liquid Equilibria for Binary Mixtures Composed of the Closely Boiling Compounds 1,2-Dimethoxybenzene and 2-Methoxyphenol with an Adducted Agent: tert-Butanol or Morpholine
- Infinite Dilution Binary Diffusion Coefficients for Compounds Derived from Biomass in Water at 0.1 MPa and Temperatures from (298.2 to 353.2) K
- Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
- Joback Method
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.
These property values are available through the Cheméo API. A free account gives you an access key.