- InChI
- InChI=1S/C8H8O3/c1-11-8(10)6-4-2-3-5-7(6)9/h2-5,9H,1H3
- InChI Key
- OSWPMRLSEDHDFF-UHFFFAOYSA-N
- Formula
- C8H8O3
- SMILES
- COC(=O)c1ccccc1O
- Molecular Weight1
- 152.15
- CAS
- 119-36-8
- Other Names
-
- 2-carbomethoxyphenol
- 2-hydroxybenzoic acid methyl ester
- Benzoic acid, 2-hydroxy-, methyl ester
- methyl 2-hydroxybenzoate
- methyl o-hydroxybenzoate
- methyl ortho-hydroxybenzoate
- salicylic acid methyl ester
- ω : Acentric Factor.
- 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).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- 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 | 0.5813 | ChemSep v8.3 pure component data | |
| μ | 2.47 | debye | ChemSep v8.3 pure component data |
| ΔfG° | -339.00 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | -467.00 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfusH° | 20.67 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 65.04 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 7.65 | eV | NIST |
| log10WS | -2.34 | Aq. Solubility Prediction | |
| logPoct/wat | 1.179 | Crippen Calculated Property | |
| McVol | 113.130 | ml/mol | McGowan Calculated Property |
| Pc | 4090.00 | kPa | ChemSep v8.3 pure component data |
| Ptriple | 5.49e-05 | kPa | ChemSep v8.3 pure component data |
| Inp | [1152.00; 1236.00] |
|
|
| Inp | 1169.35 | NIST | |
| Inp | 1173.30 | NIST | |
| Inp | 1177.24 | NIST | |
| Inp | 1181.56 | NIST | |
| Inp | 1185.90 | NIST | |
| Inp | 1190.36 | NIST | |
| Inp | 1195.52 | NIST | |
| Inp | Outlier 1154.15 | NIST | |
| Inp | 1157.80 | NIST | |
| Inp | 1161.55 | NIST | |
| Inp | 1165.41 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1176.50 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1198.80 | NIST | |
| Inp | 1198.00 | NIST | |
| Inp | Outlier 1234.00 | NIST | |
| Inp | 1187.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | Outlier 1234.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1163.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1201.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1200.70 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1199.50 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1196.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1195.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1198.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1177.40 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1183.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | Outlier 1217.00 | NIST | |
| Inp | Outlier 1236.00 | NIST | |
| Inp | 1176.00 | NIST | |
| Inp | 1188.60 | NIST | |
| Inp | 1188.80 | NIST | |
| Inp | 1203.20 | NIST | |
| Inp | 1167.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1163.10 | NIST | |
| Inp | 1195.50 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1203.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1201.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1195.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1200.00 | NIST | |
| Inp | 1201.00 | NIST | |
| Inp | 1195.00 | NIST | |
| Inp | 1202.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1195.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | Outlier 1222.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Inp | Outlier 1155.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1195.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1203.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1163.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Inp | 1206.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1197.50 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1211.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1201.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Inp | 1163.20 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1167.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1161.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1204.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1164.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1201.00 | NIST | |
| Inp | 1203.00 | NIST | |
| Inp | 1205.00 | NIST | |
| Inp | 1205.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1195.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1206.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1200.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1187.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1207.00 | NIST | |
| Inp | Outlier 1230.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | Outlier 1234.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | Outlier 1152.00 | NIST | |
| Inp | 1187.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1163.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1193.00 | NIST | |
| Inp | 1192.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1177.40 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1188.60 | NIST | |
| Inp | 1163.10 | NIST | |
| Inp | 1169.35 | NIST | |
| Inp | 1190.36 | NIST | |
| Inp | 1165.41 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1203.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1208.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1163.00 | NIST | |
| Inp | 1206.00 | NIST | |
| Inp | 1201.00 | NIST | |
| Inp | 1163.20 | NIST | |
| Inp | 1167.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1176.00 | NIST | |
| I | [1715.00; 1813.00] |
|
|
| I | 1808.00 | NIST | |
| I | 1781.80 | NIST | |
| I | 1766.00 | NIST | |
| I | 1735.00 | NIST | |
| I | 1755.00 | NIST | |
| I | 1804.00 | NIST | |
| I | 1804.00 | NIST | |
| I | 1734.00 | NIST | |
| I | 1784.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1727.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1741.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1803.00 | NIST | |
| I | 1727.00 | NIST | |
| I | 1744.00 | NIST | |
| I | 1743.00 | NIST | |
| I | 1762.00 | NIST | |
| I | 1753.00 | NIST | |
| I | 1739.00 | NIST | |
| I | 1745.00 | NIST | |
| I | 1745.00 | NIST | |
| I | 1755.00 | NIST | |
| I | 1754.00 | NIST | |
| I | 1739.00 | NIST | |
| I | 1744.00 | NIST | |
| I | 1742.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1755.00 | NIST | |
| I | Outlier 1715.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1786.00 | NIST | |
| I | 1778.00 | NIST | |
| I | 1779.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1787.00 | NIST | |
| I | 1787.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1759.00 | NIST | |
| I | 1757.00 | NIST | |
| I | 1771.00 | NIST | |
| I | 1762.20 | NIST | |
| I | 1791.20 | NIST | |
| I | 1753.00 | NIST | |
| I | 1794.00 | NIST | |
| I | 1781.00 | NIST | |
| I | 1780.00 | NIST | |
| I | 1727.00 | NIST | |
| I | 1727.00 | NIST | |
| I | 1758.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1752.00 | NIST | |
| I | 1770.00 | NIST | |
| I | Outlier 1718.00 | NIST | |
| I | 1801.00 | NIST | |
| I | 1770.00 | NIST | |
| I | 1775.00 | NIST | |
| I | 1775.00 | NIST | |
| I | 1775.00 | NIST | |
| I | 1789.00 | NIST | |
| I | 1771.00 | NIST | |
| I | 1740.00 | NIST | |
| I | 1801.00 | NIST | |
| I | 1787.00 | NIST | |
| I | 1775.00 | NIST | |
| I | 1788.00 | NIST | |
| I | 1762.00 | NIST | |
| I | 1809.00 | NIST | |
| I | 1767.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1788.00 | NIST | |
| I | 1760.00 | NIST | |
| I | 1743.00 | NIST | |
| I | 1794.00 | NIST | |
| I | 1768.00 | NIST | |
| I | 1805.00 | NIST | |
| I | 1766.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1763.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1781.00 | NIST | |
| I | 1788.00 | NIST | |
| I | 1800.00 | NIST | |
| I | 1783.00 | NIST | |
| I | 1804.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1745.00 | NIST | |
| I | 1788.00 | NIST | |
| I | 1792.00 | NIST | |
| I | 1804.00 | NIST | |
| I | 1727.00 | NIST | |
| I | 1754.00 | NIST | |
| I | 1727.00 | NIST | |
| I | 1754.00 | NIST | |
| I | 1739.00 | NIST | |
| I | 1772.00 | NIST | |
| I | 1813.00 | NIST | |
| I | 1782.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1730.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1775.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1768.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1738.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1749.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1756.00 | NIST | |
| I | 1757.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1751.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1744.00 | NIST | |
| I | 1748.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1800.00 | NIST | |
| I | 1754.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1754.00 | NIST | |
| I | 1762.00 | NIST | |
| I | 1800.00 | NIST | |
| I | 1798.00 | NIST | |
| I | 1773.00 | NIST | |
| I | 1800.00 | NIST | |
| I | 1800.00 | NIST | |
| I | 1792.00 | NIST | |
| I | 1791.00 | NIST | |
| I | 1804.00 | NIST | |
| I | 1785.00 | NIST | |
| I | 1785.00 | NIST | |
| I | 1801.00 | NIST | |
| I | 1789.00 | NIST | |
| I | 1775.00 | NIST | |
| I | 1747.00 | NIST | |
| I | 1768.00 | NIST | |
| I | 1765.00 | NIST | |
| I | 1783.00 | NIST | |
| I | 1792.00 | NIST | |
| I | 1754.00 | NIST | |
| I | 1730.00 | NIST | |
| Tboil | [495.20; 496.50] | K |
|
| Tboil | 496.35 | K | ChemSep v8.3 pure component data |
| Tboil | 495.20 | K | NIST |
| Tboil | 496.50 | K | NIST |
| Tboil | 496.10 ± 0.50 | K | NIST |
| Tboil | 495.50 ± 0.50 | K | NIST |
| Tboil | 495.35 ± 1.00 | K | NIST |
| Tc | [701.00; 709.00] | K |
|
| Tc | 701.00 | K | ChemSep v8.3 pure component data |
| Tc | 709.00 ± 5.00 | K | NIST |
| Tfus | [264.85; 271.49] | K |
|
| Tfus | 271.49 | K | Experimental and theoretical study of methyl n-hydroxybenzoates |
| Tfus | 264.85 | K | ChemSep v8.3 pure component data |
| Tfus | 264.90 | K | Aq. Solubility Prediction |
| Ttriple | 265.15 | K | ChemSep v8.3 pure component data |
| UQi | 4.45 | ChemSep v8.3 pure component data | |
| URi | 5.67 | ChemSep v8.3 pure component data | |
| Vc | 0.410 | m3/kmol | ChemSep v8.3 pure component data |
| Zc | 0.2840000 | ChemSep v8.3 pure component data |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [122.04; 379.27] | J/mol×K | [255.00; 1500.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 4.60241e+01 | |||
| Coefficient B | -4.54078e+02 | |||
| Coefficient C | 6.11158e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 122.04 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 188.21 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 238.03 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 275.05 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 303.22 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 325.22 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 342.83 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 357.21 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 369.17 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 379.27 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [245.46; 477.88] | J/mol×K | [295.20; 630.90] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 4.10910e+01 | |||
| Coefficient B | 6.92320e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidHeatCapacityCp | |||
| Temperature range, min. | 295.20 | |||
| Temperature range, max. | 630.90 | |||
| Cp,liquid | 245.46 | J/mol×K | 295.20 | Calculated Property |
| Cp,liquid | 271.29 | J/mol×K | 332.50 | Calculated Property |
| Cp,liquid | 297.11 | J/mol×K | 369.80 | Calculated Property |
| Cp,liquid | 322.93 | J/mol×K | 407.10 | Calculated Property |
| Cp,liquid | 348.76 | J/mol×K | 444.40 | Calculated Property |
| Cp,liquid | 374.58 | J/mol×K | 481.70 | Calculated Property |
| Cp,liquid | 400.41 | J/mol×K | 519.00 | Calculated Property |
| Cp,liquid | 426.23 | J/mol×K | 556.30 | Calculated Property |
| Cp,liquid | 452.05 | J/mol×K | 593.60 | Calculated Property |
| Cp,liquid | 477.88 | J/mol×K | 630.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0054849; 0.0003041] | Pa×s | [265.15; 496.65] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -2.76980e+01 | |||
| Coefficient B | 2.48480e+03 | |||
| Coefficient C | 2.35130e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 265.15 | |||
| Temperature range, max. | 496.65 | |||
| η | 0.0054849 | Pa×s | 265.15 | Calculated Property |
| η | 0.0029772 | Pa×s | 290.87 | Calculated Property |
| η | 0.0018152 | Pa×s | 316.59 | Calculated Property |
| η | 0.0012094 | Pa×s | 342.32 | Calculated Property |
| η | 0.0008634 | Pa×s | 368.04 | Calculated Property |
| η | 0.0006511 | Pa×s | 393.76 | Calculated Property |
| η | 0.0005131 | Pa×s | 419.48 | Calculated Property |
| η | 0.0004192 | Pa×s | 445.21 | Calculated Property |
| η | 0.0003526 | Pa×s | 470.93 | Calculated Property |
| η | 0.0003041 | Pa×s | 496.65 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [62.70; 0.00] | kJ/mol | [265.15; 701.00] |
ChemSep v8.3 pure component data
|
| 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 | 7.51400e+01 | |||
| Coefficient B | 3.80750e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.01000e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization, ChemSep Tmax 709 K | |||
| Temperature range, min. | 265.15 | |||
| Temperature range, max. | 701.00 | |||
| ΔvapH | 62.70 | kJ/mol | 265.15 | Calculated Property |
| ΔvapH | 59.95 | kJ/mol | 313.58 | Calculated Property |
| ΔvapH | 56.98 | kJ/mol | 362.01 | Calculated Property |
| ΔvapH | 53.73 | kJ/mol | 410.43 | Calculated Property |
| ΔvapH | 50.13 | kJ/mol | 458.86 | Calculated Property |
| ΔvapH | 46.05 | kJ/mol | 507.29 | Calculated Property |
| ΔvapH | 41.27 | kJ/mol | 555.72 | Calculated Property |
| ΔvapH | 35.37 | kJ/mol | 604.14 | Calculated Property |
| ΔvapH | 27.16 | kJ/mol | 652.57 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 701.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [5.49e-05; 4080.98] | kPa | [265.15; 709.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 6.61942e+02 | |||
| Coefficient B | -3.20790e+04 | |||
| Coefficient C | -1.03420e+02 | |||
| Coefficient D | 9.93670e-02 | |||
| Coefficient E | 1.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 265.15 | |||
| Temperature range, max. | 709.00 | |||
| Pvap | 5.49e-05 | kPa | 265.15 | Calculated Property |
| Pvap | 0.03 | kPa | 314.47 | Calculated Property |
| Pvap | 1.09 | kPa | 363.78 | Calculated Property |
| Pvap | 10.66 | kPa | 413.10 | Calculated Property |
| Pvap | 48.68 | kPa | 462.42 | Calculated Property |
| Pvap | 147.09 | kPa | 511.73 | Calculated Property |
| Pvap | 360.12 | kPa | 561.05 | Calculated Property |
| Pvap | 807.18 | kPa | 610.37 | Calculated Property |
| Pvap | 1785.24 | kPa | 659.68 | Calculated Property |
| Pvap | 4080.98 | kPa | 709.00 | Calculated Property |
| Pvap | [4.82e-05; 4237.31] | kPa | [265.15; 701.00] |
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 | 4.51315e+02 | |||
| Coefficient B | -2.72868e+04 | |||
| Coefficient C | -6.47318e+01 | |||
| Coefficient D | 4.09395e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 265.15 | |||
| Temperature range, max. | 701.00 | |||
| Pvap | 4.82e-05 | kPa | 265.15 | Calculated Property |
| Pvap | 0.02 | kPa | 313.58 | Calculated Property |
| Pvap | 0.93 | kPa | 362.01 | Calculated Property |
| Pvap | 9.24 | kPa | 410.43 | Calculated Property |
| Pvap | 42.26 | kPa | 458.86 | Calculated Property |
| Pvap | 126.66 | kPa | 507.29 | Calculated Property |
| Pvap | 309.32 | kPa | 555.72 | Calculated Property |
| Pvap | 707.17 | kPa | 604.14 | Calculated Property |
| Pvap | 1657.86 | kPa | 652.57 | Calculated Property |
| Pvap | 4237.31 | kPa | 701.00 | Calculated Property |
| Pvap | [0.56; 101.13] | kPa | [352.00; 493.70] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.38720e+01 | |||
| Coefficient B | -3.65161e+03 | |||
| Coefficient C | -9.91730e+01 | |||
| Reference | Matthews, Sumner, et al., 1950 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 352.00 | |||
| Temperature range, max. | 493.70 | |||
| Pvap | 0.56 | kPa | 352.00 | Calculated Property |
| Pvap | 1.32 | kPa | 367.74 | Calculated Property |
| Pvap | 2.80 | kPa | 383.49 | Calculated Property |
| Pvap | 5.49 | kPa | 399.23 | Calculated Property |
| Pvap | 10.07 | kPa | 414.98 | Calculated Property |
| Pvap | 17.43 | kPa | 430.72 | Calculated Property |
| Pvap | 28.72 | kPa | 446.47 | Calculated Property |
| Pvap | 45.31 | kPa | 462.21 | Calculated Property |
| Pvap | 68.83 | kPa | 477.96 | Calculated Property |
| Pvap | 101.13 | kPa | 493.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1205.58; 371.34] | kg/m3 | [265.15; 709.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 9.74471e+01 | |||
| Coefficient B | 2.62420e-01 | |||
| Coefficient C | 7.09000e+02 | |||
| Coefficient D | 2.72350e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 265.15 | |||
| Temperature range, max. | 709.00 | |||
| ρl | 1205.58 | kg/m3 | 265.15 | Calculated Property |
| ρl | 1161.58 | kg/m3 | 314.47 | Calculated Property |
| ρl | 1115.22 | kg/m3 | 363.78 | Calculated Property |
| ρl | 1065.92 | kg/m3 | 413.10 | Calculated Property |
| ρl | 1012.84 | kg/m3 | 462.42 | Calculated Property |
| ρl | 954.66 | kg/m3 | 511.73 | Calculated Property |
| ρl | 889.09 | kg/m3 | 561.05 | Calculated Property |
| ρl | 811.52 | kg/m3 | 610.37 | Calculated Property |
| ρl | 709.40 | kg/m3 | 659.68 | Calculated Property |
| ρl | 371.34 | kg/m3 | 709.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.00] | N/m | [265.15; 701.00] |
ChemSep v8.3 pure component data
|
| 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 | 7.94610e-02 | |||
| Coefficient B | 1.25450e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.01000e+02 | |||
| Comment | ChemSep eq 106, SurfaceTension, ChemSep Tmax 709 K | |||
| Temperature range, min. | 265.15 | |||
| Temperature range, max. | 701.00 | |||
| γ | 0.04 | N/m | 265.15 | Calculated Property |
| γ | 0.04 | N/m | 313.58 | Calculated Property |
| γ | 0.03 | N/m | 362.01 | Calculated Property |
| γ | 0.03 | N/m | 410.43 | Calculated Property |
| γ | 0.02 | N/m | 458.86 | Calculated Property |
| γ | 0.02 | N/m | 507.29 | Calculated Property |
| γ | 0.01 | N/m | 555.72 | Calculated Property |
| γ | 0.01 | N/m | 604.14 | Calculated Property |
| γ | 0.00 | N/m | 652.57 | Calculated Property |
| γ | 0.00 | N/m | 701.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.02; 0.05] | W/m×K | [493.90; 1000.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 1.54240e-04 | |||
| Coefficient B | 9.19790e-01 | |||
| Coefficient C | 7.20580e+02 | |||
| Coefficient D | 0.00000e+00 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 493.90 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.02 | W/m×K | 493.90 | Calculated Property |
| λ | 0.02 | W/m×K | 550.13 | Calculated Property |
| λ | 0.03 | W/m×K | 606.37 | Calculated Property |
| λ | 0.03 | W/m×K | 662.60 | Calculated Property |
| λ | 0.03 | W/m×K | 718.83 | Calculated Property |
| λ | 0.04 | W/m×K | 775.07 | Calculated Property |
| λ | 0.04 | W/m×K | 831.30 | Calculated Property |
| λ | 0.04 | W/m×K | 887.53 | Calculated Property |
| λ | 0.05 | W/m×K | 943.77 | Calculated Property |
| λ | 0.05 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.15; 0.10] | W/m×K | [265.15; 493.90] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ in W/m×K, T in K | |||
| Coefficient A | 2.05330e-01 | |||
| Coefficient B | -2.07280e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidThermalConductivity | |||
| Temperature range, min. | 265.15 | |||
| Temperature range, max. | 493.90 | |||
| λ | 0.15 | W/m×K | 265.15 | Calculated Property |
| λ | 0.15 | W/m×K | 290.57 | Calculated Property |
| λ | 0.14 | W/m×K | 315.98 | Calculated Property |
| λ | 0.13 | W/m×K | 341.40 | Calculated Property |
| λ | 0.13 | W/m×K | 366.82 | Calculated Property |
| λ | 0.12 | W/m×K | 392.23 | Calculated Property |
| λ | 0.12 | W/m×K | 417.65 | Calculated Property |
| λ | 0.11 | W/m×K | 443.07 | Calculated Property |
| λ | 0.11 | W/m×K | 468.48 | Calculated Property |
| λ | 0.10 | W/m×K | 493.90 | Calculated Property |
Similar Compounds
![2-[(2-Hydroxybenzoyl)oxy]ethyl salicylate.](data:image/png;base64,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)
Find more compounds similar to methyl salicylate.
Mixtures
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Experimental and theoretical study of methyl n-hydroxybenzoates
- Solute-Solvent and Solvent-Solvent Interactions of Menthol in Isopropyl Alcohol and its Binary Mixtures with Methyl Salicylate by Volumetric, Viscometric, Interferometric and Refractive Index Techniques.
- 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
- Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
- Green Leaf Volatiles on Atmospheric Air/Water Interfaces: A Combined Experimental and Molecular Simulation Study
- Solubility of Methyl Salicylate in Supercritical Carbon Dioxide at Several Temperatures
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
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
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property mean.
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