- InChI
- InChI=1S/C7H6O3/c8-6-4-2-1-3-5(6)7(9)10/h1-4,8H,(H,9,10)
- InChI Key
- YGSDEFSMJLZEOE-UHFFFAOYSA-N
- Formula
- C7H6O3
- SMILES
- O=C(O)c1ccccc1O
- Molecular Weight1
- 138.12
- CAS
- 69-72-7
- Other Names
-
- 2-Carboxyphenol
- 2-Hydroxybenzenecarboxylic acid
- 2-Hydroxybenzoic acid
- 7681-06-3
- 8052-31-1
- Acido salicilico
- Advanced pain relief callus removers
- Advanced pain relief corn removers
- Benzoic acid, 2-hydroxy-
- Benzoic acid, o-hydroxy-
- Clear away wart remover
- Compound W
- Domerine
- Dr. Scholl's Callus Removers
- Dr. Scholl's Corn Removers
- Dr. Scholl's Wart Remover Kit
- Duofil Wart Remover
- Duofilm
- Duoplant
- Fostex
- Freezone
- Ionil
- Ionil plus
- Keralyt
- Kyselina 2-hydroxybenzoova
- Kyselina salicylova
- NSC 180
- Orthohydroxybenzoic acid
- Pernox
- Phenol-2-carboxylic acid
- Psoriacid-S-Stift
- Retarder SAX
- Retarder W
- Rutranex
- Salicyclic acid
- Salicylic acid & Sulfur Soap
- Salicylic acid collodion
- Salicylic acid soap
- Saligel
- Salonil
- Sebucare
- Sebulex
- Stri-Dex
- Trans-Ver-Sal
- component of Fostex medicated bar and cream
- component of Keralyt
- component of Solarcaine first aid spray
- component of Tinver
- o-Carboxyphenol
- o-Hydroxybenzoic acid
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid phase 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).
- ΔfH°solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (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).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ΔcH°solid | [-3029.60; -3020.00] | kJ/mol |
|
| ΔcH°solid | -3020.00 ± 1.30 | kJ/mol | NIST |
| ΔcH°solid | -3022.40 ± 0.50 | kJ/mol | NIST |
| ΔcH°solid | -3024.70 | kJ/mol | NIST |
| ΔcH°solid | -3024.70 | kJ/mol | NIST |
| ΔcH°solid | -3025.00 | kJ/mol | NIST |
| ΔcH°solid | -3023.60 | kJ/mol | NIST |
| ΔcH°solid | -3026.80 | kJ/mol | NIST |
| ΔcH°solid | -3026.80 | kJ/mol | NIST |
| ΔcH°solid | -3029.60 | kJ/mol | NIST |
| ΔcH°solid | -3029.00 ± 0.40 | kJ/mol | NIST |
| ΔcH°solid | -3027.29 | kJ/mol | NIST |
| ΔcH°solid | -3022.90 | kJ/mol | NIST |
| ΔfG° | -299.89 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-495.80; -489.00] | kJ/mol |
|
| ΔfH°gas | -495.80 ± 1.40 | kJ/mol | NIST |
| ΔfH°gas | -493.40 | kJ/mol | NIST |
| ΔfH°gas | -489.00 | kJ/mol | NIST |
| ΔfH°solid | [-592.10; -585.30] | kJ/mol |
|
| ΔfH°solid | -592.10 ± 1.30 | kJ/mol | NIST |
| ΔfH°solid | -589.70 ± 1.10 | kJ/mol | NIST |
| ΔfH°solid | -585.30 | kJ/mol | NIST |
| ΔfusH° | [24.06; 27.09] | kJ/mol |
|
| ΔfusH° | 24.06 | kJ/mol | Solubil... |
| ΔfusH° | 27.09 | kJ/mol | Solubil... |
| ΔsubH° | [81.75; 96.30] | kJ/mol |
|
| ΔsubH° | 94.40 ± 0.40 | kJ/mol | NIST |
| ΔsubH° | 96.27 ± 0.49 | kJ/mol | NIST |
| ΔsubH° | 96.30 | kJ/mol | NIST |
| ΔsubH° | 96.30 ± 0.50 | kJ/mol | NIST |
| ΔsubH° | 95.70 ± 0.10 | kJ/mol | NIST |
| ΔsubH° | 95.10 ± 0.40 | kJ/mol | NIST |
| ΔsubH° | Outlier 81.75 | kJ/mol | NIST |
| ΔvapH° | 69.89 | kJ/mol | Joback Calculated Property |
| log10WS | [-1.93; -1.85] |
|
|
| log10WS | -1.85 | Aq. Sol... | |
| log10WS | -1.93 | Aq. Sol... | |
| logPoct/wat | 1.090 | Crippen Calculated Property | |
| McVol | 99.040 | ml/mol | McGowan Calculated Property |
| Pc | 6349.11 | kPa | Joback Calculated Property |
| Inp | [1263.00; 1342.00] |
|
|
| Inp | 1277.00 | NIST | |
| Inp | 1266.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1330.00 | NIST | |
| Inp | 1295.80 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1263.00 | NIST | |
| Inp | 1330.00 | NIST | |
| Inp | 1330.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1342.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1295.80 | NIST | |
| Inp | 1277.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1311.00 | NIST | |
| S°solid,1 bar | [172.40; 178.20] | J/mol×K |
|
| S°solid,1 bar | 172.40 | J/mol×K | NIST |
| S°solid,1 bar | 178.20 | J/mol×K | NIST |
| Tboil | 612.91 | K | Joback Calculated Property |
| Tc | 833.23 | K | Joback Calculated Property |
| Tfus | [430.00; 432.70] | K |
|
| Tfus | 431.92 | K | Aq. Sol... |
| Tfus | 431.92 | K | Aq. Sol... |
| Tfus | 432.15 | K | Liquid ... |
| Tfus | 432.70 | K | Abraham... |
| Tfus | 432.00 | K | Polar M... |
| Tfus | 432.00 ± 1.50 | K | NIST |
| Tfus | 431.45 ± 0.50 | K | NIST |
| Tfus | Outlier 430.00 ± 4.00 | K | NIST |
| Tfus | 432.10 ± 0.80 | K | NIST |
| Tfus | 432.00 ± 0.80 | K | NIST |
| Tfus | 432.10 ± 0.80 | K | NIST |
| Tfus | 432.20 ± 0.80 | K | NIST |
| Vc | 0.310 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [233.10; 269.96] | J/mol×K | [612.91; 833.23] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 230 240 250 260 270 650 700 750 800 | ||||
| Cp,gas | 233.10 | J/mol×K | 612.91 | Joback Calculated Property |
| Cp,gas | 240.40 | J/mol×K | 649.63 | Joback Calculated Property |
| Cp,gas | 247.14 | J/mol×K | 686.35 | Joback Calculated Property |
| Cp,gas | 253.40 | J/mol×K | 723.07 | Joback Calculated Property |
| Cp,gas | 259.25 | J/mol×K | 759.79 | Joback Calculated Property |
| Cp,gas | 264.74 | J/mol×K | 796.51 | Joback Calculated Property |
| Cp,gas | 269.96 | J/mol×K | 833.23 | Joback Calculated Property |
| Cp,solid | [104.20; 177.50] | J/mol×K | [280.40; 405.50] |
|
|
T(K) Solid phase heat capacity (J/mol×K) 100 120 140 160 180 300 350 400 | ||||
| Cp,solid | 128.50 | J/mol×K | 280.40 | Determi... |
| Cp,solid | 130.00 | J/mol×K | 285.50 | Determi... |
| Cp,solid | 159.40 | J/mol×K | 288.60 | NIST |
| Cp,solid | 131.60 | J/mol×K | 290.50 | Determi... |
| Cp,solid | 104.20 | J/mol×K | 293.00 | NIST |
| Cp,solid | 133.50 | J/mol×K | 295.40 | Determi... |
| Cp,solid | 160.90 | J/mol×K | 298.15 | NIST |
| Cp,solid | 135.40 | J/mol×K | 300.40 | Determi... |
| Cp,solid | 137.40 | J/mol×K | 305.40 | Determi... |
| Cp,solid | 139.40 | J/mol×K | 310.40 | Determi... |
| Cp,solid | 141.40 | J/mol×K | 315.40 | Determi... |
| Cp,solid | 143.50 | J/mol×K | 320.40 | Determi... |
| Cp,solid | 145.50 | J/mol×K | 325.40 | Determi... |
| Cp,solid | 147.60 | J/mol×K | 330.40 | Determi... |
| Cp,solid | 149.80 | J/mol×K | 335.40 | Determi... |
| Cp,solid | 151.80 | J/mol×K | 340.40 | Determi... |
| Cp,solid | 154.10 | J/mol×K | 345.40 | Determi... |
| Cp,solid | 156.20 | J/mol×K | 350.40 | Determi... |
| Cp,solid | 158.20 | J/mol×K | 355.40 | Determi... |
| Cp,solid | 160.30 | J/mol×K | 360.40 | Determi... |
| Cp,solid | 162.30 | J/mol×K | 365.40 | Determi... |
| Cp,solid | 164.20 | J/mol×K | 370.40 | Determi... |
| Cp,solid | 165.90 | J/mol×K | 375.40 | Determi... |
| Cp,solid | 168.00 | J/mol×K | 380.40 | Determi... |
| Cp,solid | 170.10 | J/mol×K | 385.40 | Determi... |
| Cp,solid | 172.10 | J/mol×K | 390.40 | Determi... |
| Cp,solid | 173.80 | J/mol×K | 395.50 | Determi... |
| Cp,solid | 175.60 | J/mol×K | 400.50 | Determi... |
| Cp,solid | 177.50 | J/mol×K | 405.50 | Determi... |
| η | [0.0000161; 0.0010587] | Pa×s | [417.54; 612.91] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 450 500 550 600 | ||||
| η | 0.0010587 | Pa×s | 417.54 | Joback Calculated Property |
| η | 0.0004096 | Pa×s | 450.10 | Joback Calculated Property |
| η | 0.0001801 | Pa×s | 482.66 | Joback Calculated Property |
| η | 0.0000879 | Pa×s | 515.23 | Joback Calculated Property |
| η | 0.0000467 | Pa×s | 547.79 | Joback Calculated Property |
| η | 0.0000266 | Pa×s | 580.35 | Joback Calculated Property |
| η | 0.0000161 | Pa×s | 612.91 | Joback Calculated Property |
| ΔfusH | [23.05; 27.10] | kJ/mol | [431.10; 434.10] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 23 24 25 26 27 432 433 434 | ||||
| ΔfusH | 24.45 | kJ/mol | 431.10 | NIST |
| ΔfusH | 24.60 | kJ/mol | 431.80 | NIST |
| ΔfusH | 24.60 | kJ/mol | 431.80 | NIST |
| ΔfusH | 23.05 | kJ/mol | 432.50 | NIST |
| ΔfusH | 27.10 | kJ/mol | 434.10 | NIST |
| ΔsubH | [93.20; 99.00] | kJ/mol | [313.00; 388.00] |
|
|
T(K) Enthalpy of sublimation at a given temperature (kJ/mol) 93 94 95 96 97 98 99 320 340 360 380 | ||||
| ΔsubH | 99.00 ± 2.00 | kJ/mol | 313.00 | NIST |
| ΔsubH | 95.70 ± 0.80 | kJ/mol | 315.50 | NIST |
| ΔsubH | 94.90 ± 0.40 | kJ/mol | 322.00 | NIST |
| ΔsubH | 93.20 ± 0.80 | kJ/mol | 322.00 | NIST |
| ΔsubH | 95.10 ± 0.50 | kJ/mol | 333.00 | NIST |
| ΔsubH | 94.80 ± 0.40 | kJ/mol | 388.00 | NIST |
| ΔsubH | 95.10 ± 0.40 | kJ/mol | 388.00 | NIST |
| ΔvapH | 79.40 | kJ/mol | 474.50 | NIST |
| ΔfusS | 56.90 | J/mol×K | 431.80 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 484.20 | K | 2.70 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.71; 6185.51] | kPa | [431.75; 739.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.74158e+02 | |||
| Coefficient B | -3.34417e+04 | |||
| Coefficient C | -6.61599e+01 | |||
| Coefficient D | 3.08189e-05 | |||
| Temperature range, min. | 431.75 | |||
| Temperature range, max. | 739.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 500 600 700 | ||||
| Pvap | 2.71 | kPa | 431.75 | Calculated Property |
| Pvap | 13.24 | kPa | 465.89 | Calculated Property |
| Pvap | 45.69 | kPa | 500.03 | Calculated Property |
| Pvap | 123.34 | kPa | 534.17 | Calculated Property |
| Pvap | 280.60 | kPa | 568.31 | Calculated Property |
| Pvap | 568.93 | kPa | 602.44 | Calculated Property |
| Pvap | 1072.29 | kPa | 636.58 | Calculated Property |
| Pvap | 1940.48 | kPa | 670.72 | Calculated Property |
| Pvap | 3457.41 | kPa | 704.86 | Calculated Property |
| Pvap | 6185.51 | kPa | 739.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Salicylic acid.
Mixtures
- Choline chloride + Salicylic acid
- Salicylic acid + Water + tri-n-Amylphosphate
- Ethanol + Salicylic acid
- 1-Propanol + Salicylic acid
- Salicylic acid + 1-Butanol
- Salicylic acid + 1-Pentanol
- Salicylic acid + 1-Hexanol
- Acetic acid, pentyl ester + Salicylic acid
- Salicylic acid + Methyl Alcohol
- 1-Propanol + Salicylic acid + Water
- Salicylic acid + Ethyl Acetate
- Salicylic acid + Acetone
- Salicylic acid + Water
- Salicylic acid + Acetic acid
- Acetonitrile + Salicylic acid
- Carbon dioxide + Salicylic acid
- Benzoic acid + Carbon dioxide + Salicylic acid
- Carbon dioxide + Salicylic acid + Aspirin
- sodium chloride + Salicylic acid + Water
- potassium chloride + Salicylic acid + Water
Find more mixtures with Salicylic acid.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Solubility of salicylic acid in water + salt (NaCl, KCl, NaBr, Na2SO4 and K2SO4) at 293.5 to 313.3 K
- Liquid pharmaceuticals formulation by eutectic formation
- Strategy for extractant residual reduction: Experimental and computational investigation of fluorinated phosphate
- Construction, calibration and testing of a micro-combustion calorimeter
- Determination of the activity of a molecular solute in saturated solution
- Solubility of salicylic acid in pure alcohols at different temperatures
- Calibration and testing of an isoperibolic micro-combustion calorimeter developed to measure the enthalpy of combustion of organic compounds containing C, H, O and N
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Synthesis, characterization and standard molar enthalpy of formation of La(C7H5O3)2*(C9H6NO)
- Synthesis, Characterization and Standard Molar Enthalpy of Formation of Sm (C7H5O3)2 * (C9H6NO)
- Thermochemical Analysis on Rare Earth Complex of Gadolinium with Salicylic acid and 8-hydroxyquinoline
- Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
- Measurement and Correlation of the Solubility of 2,6-Dihydroxybenzoic Acid in Alcohols and Binary Solvents
- Solubility of Benzoin in Six Monosolvents and in Some Binary Solvent Mixtures at Various Temperatures
- Determination and Correlation of Solubility and Thermodynamic Properties of trans-Cinnamyl Alcohol in Pure and Binary Solvents from 253.15 K to 293.15 K
- Solubility and Melting Properties of Salicylic Acid
- Solubility of 2-Hydroxybenzoic Acid in Water, 1-Propanol, 2-Propanol, and 2-Propanone at (298.2 to 338.2) K and Their Aqueous Binary Mixtures at 298.2 K
- Solubility of Glycyrrhizin in supercritical carbon dioxide with and without cosolvent
- Polar Mixed-Solid Solute Systems in Supercritical Carbon Dioxide: Entrainer Effect and Its Influence on Solubility and Selectivity
- Solubility of Salicylic Acid in Water, Ethanol, Carbon Tetrachloride, Ethyl Acetate, and Xylene
- Solubilities of Salicylic Acid in Pure Solvents and Binary Mixtures Containing Cosolvent
- Solubility of Benzoic and Salicylic Acids in Subcritical Water at Temperatures Ranging from (298 to 473) K
- Joback Method
- Aqueous Solubility Prediction Method
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
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