- 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
- Guaiacol
- Guaiastil
- Guaicol
- Guaicolina
- Guajakol
- Guajol
- Guasol
- Methylcatachol
- Methylcatechol
- NSC 3815
- O-Methyl catechol
- Phenol, o-methoxy-
- Pyrocatechol monomethyl ether
- Pyroguaiac acid
- guaiacol (2-methoxyphenol)
- guiacol
- o-Guaiacol
- o-Guiacol
- o-Hydroxyanisole
- o-Methoxyphenol
- ortho-Guaiacol
- 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).
- 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.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -139.15 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -260.81 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 14.90 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 62.60 ± 0.50 | kJ/mol | NIST |
| log10WS | [-1.96; -1.96] |
|
|
| log10WS | -1.96 | Aq. Sol... | |
| log10WS | -1.96 | Estimat... | |
| 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 | 1090.00 | NIST | |
| Inp | 1070.00 | 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 | |
| Tboil | [478.10; 478.30] | K |
|
| Tboil | 478.10 | K | Isobari... |
| Tboil | 478.25 | K | Isobari... |
| 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 | 716.68 | K | Joback Calculated Property |
| Tfus | [301.15; 302.65] | K |
|
| Tfus | 302.65 | K | Aq. Sol... |
| Tfus | 301.15 ± 0.40 | K | NIST |
| Tfus | 301.25 ± 0.40 | K | NIST |
| Tfus | 301.45 ± 0.60 | K | NIST |
| Vc | 0.303 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [205.43; 258.19] | J/mol×K | [489.28; 716.68] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 210 220 230 240 250 260 500 600 700 | ||||
| Cp,gas | 205.43 | J/mol×K | 489.28 | Joback Calculated Property |
| Cp,gas | 215.86 | J/mol×K | 527.18 | Joback Calculated Property |
| Cp,gas | 225.57 | J/mol×K | 565.08 | Joback Calculated Property |
| Cp,gas | 234.59 | J/mol×K | 602.98 | Joback Calculated Property |
| Cp,gas | 243.00 | J/mol×K | 640.88 | Joback Calculated Property |
| Cp,gas | 250.84 | J/mol×K | 678.78 | Joback Calculated Property |
| Cp,gas | 258.19 | J/mol×K | 716.68 | Joback Calculated Property |
| η | [0.0000871; 0.0032569] | Pa×s | [329.02; 489.28] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 350 400 450 | ||||
| η | 0.0032569 | Pa×s | 329.02 | Joback Calculated Property |
| η | 0.0014199 | Pa×s | 355.73 | Joback Calculated Property |
| η | 0.0006951 | Pa×s | 382.44 | Joback Calculated Property |
| η | 0.0003736 | Pa×s | 409.15 | Joback Calculated Property |
| η | 0.0002167 | Pa×s | 435.86 | Joback Calculated Property |
| η | 0.0001338 | Pa×s | 462.57 | Joback Calculated Property |
| η | 0.0000871 | Pa×s | 489.28 | Joback Calculated Property |
| ΔvapH | [52.70; 52.70] | kJ/mol | [416.50; 428.50] |
|
| ΔvapH | 52.70 | kJ/mol | 416.50 | NIST |
| ΔvapH | 52.70 | kJ/mol | 428.50 | NIST |
| Pvap | [2.98; 40.30] | kPa | [373.15; 443.15] |
|
|
T(K) Vapor pressure (kPa) 0 5 10 15 20 25 30 35 40 380 400 420 440 | ||||
| Pvap | 2.98 | kPa | 373.15 | Isother... |
| Pvap | 4.69 | kPa | 383.15 | Isother... |
| Pvap | 7.08 | kPa | 393.15 | Isother... |
| Pvap | 15.20 | kPa | 413.15 | Isother... |
| Pvap | 25.30 | kPa | 428.15 | Isother... |
| Pvap | 40.30 | kPa | 443.15 | Isother... |
| n0 | 1.54410 | 293.15 | Liquid-... | |
| ρl | [1085.02; 1138.64] | kg/m3 | [288.15; 343.15] |
|
|
T(K) Liquid Density (kg/m3) 1080 1090 1100 1110 1120 1130 1140 300 320 340 | ||||
| ρl | 1138.64 | kg/m3 | 288.15 | Experim... |
| ρl | 1133.81 | kg/m3 | 293.15 | Experim... |
| ρl | 1128.96 | kg/m3 | 298.15 | Experim... |
| ρl | 1124.11 | kg/m3 | 303.15 | Experim... |
| ρl | 1119.25 | kg/m3 | 308.15 | Experim... |
| ρl | 1114.38 | kg/m3 | 313.15 | Experim... |
| ρl | 1109.51 | kg/m3 | 318.15 | Experim... |
| ρl | 1104.63 | kg/m3 | 323.15 | Experim... |
| ρl | 1099.74 | kg/m3 | 328.15 | Experim... |
| ρl | 1094.84 | kg/m3 | 333.15 | Experim... |
| ρl | 1089.94 | kg/m3 | 338.15 | Experim... |
| ρl | 1085.02 | kg/m3 | 343.15 | Experim... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [358.42; 506.24] |
The Yaw...
|
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
| 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- + Anisole
- Phenol, 2-methoxy- + Isopropyl acetate + Water
- Phenol, 2-methoxy- + Acetic acid, butyl ester
- Phenol, 2-methoxy- + Benzene, 1,2-dimethoxy-
- 2-Propanol, 2-methyl- + Phenol, 2-methoxy-
- Phenol, 2-methoxy- + Morpholine
- Phenol, 2-methoxy- + Water
- Phenol, 2-methoxy- + Ethanol
- Phenol, 2-methoxy- + Methane
- Phenol, 2-methoxy- + Acetonitrile
- Phenol, 2-methoxy- + Tetrahydrofuran
- Phenol, 2-methoxy- + Choline chloride
- Phenol, 2-methoxy- + Diethylamine, hydrochloride
- Phenol, 2-methoxy- + Choline chloride + Carbon dioxide
- Phenol, 2-methoxy- + Carbon dioxide + Diethylamine, hydrochloride
- Phenol, 2-methoxy- + Methyl Isobutyl Ketone + Water
Sources
- 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
- 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
- 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
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