Chemical Properties of Phenol, 2-methoxy- (CAS 90-05-1)

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.
• C_p,gas : Ideal gas heat capacity (J/mol×K).
• η : Dynamic viscosity (Pa×s).
• Δ_fG° : Standard Gibbs free energy of formation (kJ/mol).
• Δ_fH°_gas : Enthalpy of formation at standard conditions (kJ/mol).
• Δ_fusH° : Enthalpy of fusion at standard conditions (kJ/mol).
• Δ_vapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
• Δ_vapH : Enthalpy of vaporization at a given temperature (kJ/mol).
• IE : Ionization energy (eV).
• log₁₀WS : Log10 of Water solubility in mol/l.
• logP_oct/wat : Octanol/Water partition coefficient.
• McVol : McGowan's characteristic volume (ml/mol).
• P_c : Critical Pressure (kPa).
• P_vap : Vapor pressure (kPa).
• n₀ : Refractive Index.
• ρ_l : Liquid Density (kg/m³).
• I_np : Non-polar retention indices.
• I_p : Polar retention indices.
• γ : Surface Tension (N/m).
• T_boil : Normal Boiling Point Temperature (K).
• T_c : Critical Temperature (K).
• T_fus : Normal melting (fusion) point (K).
• V_c : Critical Volume (m³/kmol).
• ¹: Molecular weight from the IUPAC atomic weights tables.

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
Ip	[1814.00; 1909.00]
Ip	1880.00		NIST
Ip	1862.00		NIST
Ip	1875.00		NIST
Ip	1867.00		NIST
Ip	1871.00		NIST
Ip	1862.00		NIST
Ip	1841.00		NIST
Ip	1860.00		NIST
Ip	1871.00		NIST
Ip	1846.00		NIST
Ip	1855.00		NIST
Ip	1889.00		NIST
Ip	1865.00		NIST
Ip	1864.00		NIST
Ip	1864.00		NIST
Ip	1861.00		NIST
Ip	1861.00		NIST
Ip	1849.00		NIST
Ip	Outlier 1823.00		NIST
Ip	1875.00		NIST
Ip	Outlier 1815.00		NIST
Ip	Outlier 1823.00		NIST
Ip	1872.00		NIST
Ip	1868.00		NIST
Ip	1868.00		NIST
Ip	1871.00		NIST
Ip	1855.00		NIST
Ip	1872.00		NIST
Ip	1840.00		NIST
Ip	1867.00		NIST
Ip	1849.00		NIST
Ip	1873.00		NIST
Ip	1867.00		NIST
Ip	1859.00		NIST
Ip	1872.00		NIST
Ip	1840.00		NIST
Ip	1850.00		NIST
Ip	1868.00		NIST
Ip	1856.00		NIST
Ip	1849.00		NIST
Ip	1852.00		NIST
Ip	1850.00		NIST
Ip	1851.00		NIST
Ip	1867.00		NIST
Ip	1894.00		NIST
Ip	1896.00		NIST
Ip	1896.00		NIST
Ip	1897.50		NIST
Ip	1846.00		NIST
Ip	1846.00		NIST
Ip	1859.00		NIST
Ip	1836.00		NIST
Ip	1829.00		NIST
Ip	1840.00		NIST
Ip	1882.00		NIST
Ip	1857.00		NIST
Ip	1875.00		NIST
Ip	1859.00		NIST
Ip	1826.00		NIST
Ip	1870.00		NIST
Ip	1858.00		NIST
Ip	1838.00		NIST
Ip	1875.00		NIST
Ip	1833.00		NIST
Ip	1830.00		NIST
Ip	1860.00		NIST
Ip	1878.00		NIST
Ip	1875.00		NIST
Ip	1840.00		NIST
Ip	1873.00		NIST
Ip	1851.00		NIST
Ip	1890.00		NIST
Ip	1893.00		NIST
Ip	1869.00		NIST
Ip	1857.00		NIST
Ip	1862.00		NIST
Ip	1862.00		NIST
Ip	1859.00		NIST
Ip	1880.00		NIST
Ip	1863.00		NIST
Ip	1876.00		NIST
Ip	1886.00		NIST
Ip	1862.00		NIST
Ip	1859.00		NIST
Ip	1885.00		NIST
Ip	1876.00		NIST
Ip	1855.00		NIST
Ip	1892.00		NIST
Ip	1875.00		NIST
Ip	1862.00		NIST
Ip	1876.00		NIST
Ip	1834.00		NIST
Ip	1894.00		NIST
Ip	1825.00		NIST
Ip	1860.00		NIST
Ip	1877.00		NIST
Ip	1883.00		NIST
Ip	1863.00		NIST
Ip	1879.00		NIST
Ip	1831.00		NIST
Ip	1853.00		NIST
Ip	1884.00		NIST
Ip	1869.00		NIST
Ip	1861.00		NIST
Ip	1862.00		NIST
Ip	1893.00		NIST
Ip	1890.00		NIST
Ip	1880.00		NIST
Ip	1872.00		NIST
Ip	1864.00		NIST
Ip	1863.00		NIST
Ip	1846.00		NIST
Ip	1847.00		NIST
Ip	1857.00		NIST
Ip	1875.00		NIST
Ip	1863.00		NIST
Ip	1875.00		NIST
Ip	1854.00		NIST
Ip	1847.00		NIST
Ip	1847.00		NIST
Ip	1840.00		NIST
Ip	1840.00		NIST
Ip	1848.00		NIST
Ip	1857.00		NIST
Ip	1855.00		NIST
Ip	1868.00		NIST
Ip	1869.00		NIST
Ip	1882.00		NIST
Ip	1848.00		NIST
Ip	1851.00		NIST
Ip	1855.00		NIST
Ip	1882.00		NIST
Ip	1882.00		NIST
Ip	1882.00		NIST
Ip	1848.00		NIST
Ip	1848.00		NIST
Ip	1865.00		NIST
Ip	1840.00		NIST
Ip	Outlier 1815.00		NIST
Ip	1859.00		NIST
Ip	Outlier 1816.00		NIST
Ip	Outlier 1815.00		NIST
Ip	1863.00		NIST
Ip	1830.00		NIST
Ip	1840.00		NIST
Ip	1873.00		NIST
Ip	1858.00		NIST
Ip	1877.00		NIST
Ip	1889.00		NIST
Ip	1884.00		NIST
Ip	1873.00		NIST
Ip	1864.00		NIST
Ip	1873.00		NIST
Ip	1875.00		NIST
Ip	1864.00		NIST
Ip	1876.00		NIST
Ip	1875.00		NIST
Ip	1833.00		NIST
Ip	1878.00		NIST
Ip	1855.00		NIST
Ip	1837.00		NIST
Ip	1838.00		NIST
Ip	1843.00		NIST
Ip	1859.00		NIST
Ip	1859.00		NIST
Ip	1843.00		NIST
Ip	1860.00		NIST
Ip	1842.00		NIST
Ip	1876.00		NIST
Ip	1854.00		NIST
Ip	1882.00		NIST
Ip	1859.00		NIST
Ip	Outlier 1909.00		NIST
Ip	1873.00		NIST
Ip	1873.00		NIST
Ip	1850.00		NIST
Ip	1855.00		NIST
Ip	1852.00		NIST
Ip	1859.00		NIST
Ip	1870.00		NIST
Ip	1880.00		NIST
Ip	1840.00		NIST
Ip	1890.00		NIST
Ip	Outlier 1899.00		NIST
Ip	1850.00		NIST
Ip	1840.00		NIST
Ip	1853.00		NIST
Ip	1878.00		NIST
Ip	1831.00		NIST
Ip	1867.00		NIST
Ip	1846.00		NIST
Ip	1859.00		NIST
Ip	1850.00		NIST
Ip	1850.00		NIST
Ip	Outlier 1814.00		NIST
Ip	1860.00		NIST
Ip	1840.00		NIST
Ip	1840.00		NIST
Ip	1882.00		NIST
Ip	1870.00		NIST
Ip	1830.00		NIST
Ip	1873.00		NIST
Ip	1890.00		NIST
Ip	1862.00		NIST
Ip	1886.00		NIST
Ip	1855.00		NIST
Ip	1834.00		NIST
Ip	1883.00		NIST
Ip	1884.00		NIST
Ip	1846.00		NIST
Ip	1875.00		NIST
Ip	1840.00		NIST
Ip	1869.00		NIST
Ip	1865.00		NIST
Ip	Outlier 1815.00		NIST
Ip	1876.00		NIST
Ip	1837.00		NIST
Ip	1843.00		NIST
Ip	1850.00		NIST
Ip	1880.00		NIST
Ip	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	708.38	K	Relay (1.0) Calculated Property
Tfus	[301.15; 302.65]	K
Tfus	302.15	K	Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
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	0.334	m3/kmol	Relay (1.0) Calculated Property

Temperature Dependent Properties

Property	Value	Unit	Temperature (K)	Source
ΔvapH	[52.70; 62.60]	kJ/mol	[298.15; 428.50]
ΔvapH	62.60	kJ/mol	298.15	Thermochemical Study of the Methoxy- and Dimethoxyphenol Isomers
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]
Pvap	2.98	kPa	373.15	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
Pvap	4.69	kPa	383.15	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
Pvap	7.08	kPa	393.15	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
Pvap	15.20	kPa	413.15	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
Pvap	25.30	kPa	428.15	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
Pvap	40.30	kPa	443.15	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
n0	1.54410		293.15	Liquid-liquid equilibria of water + solutes (acetic acid/ acetol/furfural/guaiacol/methanol/phenol/propanal) + solvents (isopropyl acetate/toluene) ternary systems for pyrolysis oil fractionation
ρl	[1085.02; 1138.64]	kg/m3	[288.15; 343.15]
ρl	1138.64	kg/m3	288.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1133.81	kg/m3	293.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1128.96	kg/m3	298.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1124.11	kg/m3	303.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1119.25	kg/m3	308.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1114.38	kg/m3	313.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1109.51	kg/m3	318.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1104.63	kg/m3	323.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1099.74	kg/m3	328.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1094.84	kg/m3	333.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1089.94	kg/m3	338.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl	1085.02	kg/m3	343.15	Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model

Correlations

Property	Value	Unit	Temperature (K)	Source
Cp,gas	[129.01; 302.86]	J/mol×K	[273.00; 1000.00]	Joback Predicted correlation
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K
Coefficient A			-2.08000e+01
Coefficient B			6.81320e-01
Coefficient C			-5.33560e-04
Coefficient D			1.75900e-07
Coefficient E			0.00000e+00
Temperature range, min.			273.00
Temperature range, max.			1000.00
Cp,gas	129.01	J/mol×K	273.00	Calculated Property
Cp,gas	161.24	J/mol×K	353.78	Calculated Property
Cp,gas	188.95	J/mol×K	434.56	Calculated Property
Cp,gas	212.68	J/mol×K	515.33	Calculated Property
Cp,gas	233.00	J/mol×K	596.11	Calculated Property
Cp,gas	250.47	J/mol×K	676.89	Calculated Property
Cp,gas	265.63	J/mol×K	757.67	Calculated Property
Cp,gas	279.04	J/mol×K	838.44	Calculated Property
Cp,gas	291.27	J/mol×K	919.22	Calculated Property
Cp,gas	302.86	J/mol×K	1000.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
η	[0.0088534; 0.0000723]	Pa×s	[301.73; 501.88]	Joback Predicted correlation
Equation			Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K
Coefficient A			-1.67836e+01
Coefficient B			3.63785e+03
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Comment			Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc.
Temperature range, min.			301.73
Temperature range, max.			501.88
η	0.0088534	Pa×s	301.73	Calculated Property
η	0.0038697	Pa×s	323.97	Calculated Property
η	0.0018811	Pa×s	346.21	Calculated Property
η	0.0009976	Pa×s	368.45	Calculated Property
η	0.0005687	Pa×s	390.69	Calculated Property
η	0.0003444	Pa×s	412.92	Calculated Property
η	0.0002196	Pa×s	435.16	Calculated Property
η	0.0001462	Pa×s	457.40	Calculated Property
η	0.0001011	Pa×s	479.64	Calculated Property
η	0.0000723	Pa×s	501.88	Calculated Property

Property	Value	Unit	Temperature (K)	Source
Pvap	[1.33; 202.65]	kPa	[358.42; 506.24]	The Yaws Handbook of Vapor Pressure
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
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
Pvap	[1.27; 103.31]	kPa	[355.00; 478.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46516e+01
Coefficient B			-4.03746e+03
Coefficient C			-7.48100e+01
Reference			von Terres, Gebert, et al., 1955, 2
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			355.00
Temperature range, max.			478.00
Pvap	1.27	kPa	355.00	Calculated Property
Pvap	2.49	kPa	368.67	Calculated Property
Pvap	4.58	kPa	382.33	Calculated Property
Pvap	8.01	kPa	396.00	Calculated Property
Pvap	13.39	kPa	409.67	Calculated Property
Pvap	21.48	kPa	423.33	Calculated Property
Pvap	33.25	kPa	437.00	Calculated Property
Pvap	49.88	kPa	450.67	Calculated Property
Pvap	72.71	kPa	464.33	Calculated Property
Pvap	103.31	kPa	478.00	Calculated Property
Pvap	[0.13; 100.43]	kPa	[325.60; 478.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.74092e+01
Coefficient B			-5.72099e+03
Coefficient C			-3.10350e+01
Reference			Stull, 1947
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			325.60
Temperature range, max.			478.00
Pvap	0.13	kPa	325.60	Calculated Property
Pvap	0.38	kPa	342.53	Calculated Property
Pvap	0.99	kPa	359.47	Calculated Property
Pvap	2.33	kPa	376.40	Calculated Property
Pvap	5.04	kPa	393.33	Calculated Property
Pvap	10.21	kPa	410.27	Calculated Property
Pvap	19.46	kPa	427.20	Calculated Property
Pvap	35.17	kPa	444.13	Calculated Property
Pvap	60.67	kPa	461.07	Calculated Property
Pvap	100.43	kPa	478.00	Calculated Property
Pvap	[1.27; 103.31]	kPa	[355.00; 478.00]	NIST
Equation			ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K
Coefficient A			1.46516e+01
Coefficient B			-4.03746e+03
Coefficient C			-7.48100e+01
Reference			von Terres, Gebert, et al., 1955
Comment			Coefficents calculated by NIST from author's data.
Temperature range, min.			355.00
Temperature range, max.			478.00
Pvap	1.27	kPa	355.00	Calculated Property
Pvap	2.49	kPa	368.67	Calculated Property
Pvap	4.58	kPa	382.33	Calculated Property
Pvap	8.01	kPa	396.00	Calculated Property
Pvap	13.39	kPa	409.67	Calculated Property
Pvap	21.48	kPa	423.33	Calculated Property
Pvap	33.25	kPa	437.00	Calculated Property
Pvap	49.88	kPa	450.67	Calculated Property
Pvap	72.71	kPa	464.33	Calculated Property
Pvap	103.31	kPa	478.00	Calculated Property

Property	Value	Unit	Temperature (K)	Source
γ	[0.04; 0.02]	N/m	[301.15; 478.15]	Jasper (1972), surface tension of pure liquid compounds Compiled value
Equation			Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K
Coefficient A			6.69580e-02
Coefficient B			-9.43000e-05
Coefficient C			0.00000e+00
Coefficient D			0.00000e+00
Coefficient E			0.00000e+00
Temperature range, min.			301.15
Temperature range, max.			478.15
γ	0.04	N/m	301.15	Calculated Property
γ	0.04	N/m	320.82	Calculated Property
γ	0.03	N/m	340.48	Calculated Property
γ	0.03	N/m	360.15	Calculated Property
γ	0.03	N/m	379.82	Calculated Property
γ	0.03	N/m	399.48	Calculated Property
γ	0.03	N/m	419.15	Calculated Property
γ	0.03	N/m	438.82	Calculated Property
γ	0.02	N/m	458.48	Calculated Property
γ	0.02	N/m	478.15	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

• 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).
• Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
• 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

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