- InChI
- InChI=1S/C7H6O2/c8-5-6-2-1-3-7(9)4-6/h1-5,9H
- InChI Key
- IAVREABSGIHHMO-UHFFFAOYSA-N
- Formula
- C7H6O2
- SMILES
- O=Cc1cccc(O)c1
- Molecular Weight1
- 122.12
- CAS
- 100-83-4
- Other Names
-
- 3-Formylphenol
- 3-hydroxybenzaldehyde
- Benzaldehyde, m-hydroxy-
- m-Formylphenol
- m-Hydroxybenzaldehyde
- meta-Hydroxybenzaldehyde
- 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).
- 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).
- 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).
- Psub : Sublimation pressure (kPa).
- Inp : Non-polar retention indices.
- 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 |
|---|---|---|---|
| ΔfG° | -133.67 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -214.17 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 24.10 | kJ/mol | Synthes... |
| ΔsubH° | 100.10 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | 53.19 | kJ/mol | Joback Calculated Property |
| log10WS | -1.26 | Crippen Calculated Property | |
| logPoct/wat | 1.205 | Crippen Calculated Property | |
| McVol | 93.170 | ml/mol | McGowan Calculated Property |
| Pc | 5602.57 | kPa | Joback Calculated Property |
| Inp | [1262.40; 1267.00] |
|
|
| Inp | 1262.40 | NIST | |
| Inp | 1267.00 | NIST | |
| Tboil | 513.20 | K | NIST |
| Tc | 749.54 | K | Joback Calculated Property |
| Tfus | 376.00 | K | Measure... |
| Vc | 0.302 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [197.64; 242.09] | J/mol×K | [515.52; 749.54] |
|
| Cp,gas | 197.64 | J/mol×K | 515.52 | Joback Calculated Property |
| Cp,gas | 206.73 | J/mol×K | 554.52 | Joback Calculated Property |
| Cp,gas | 215.05 | J/mol×K | 593.53 | Joback Calculated Property |
| Cp,gas | 222.66 | J/mol×K | 632.53 | Joback Calculated Property |
| Cp,gas | 229.65 | J/mol×K | 671.53 | Joback Calculated Property |
| Cp,gas | 236.10 | J/mol×K | 710.54 | Joback Calculated Property |
| Cp,gas | 242.09 | J/mol×K | 749.54 | Joback Calculated Property |
| η | [0.0000996; 0.0031017] | Pa×s | [348.79; 515.52] |
|
| η | 0.0031017 | Pa×s | 348.79 | Joback Calculated Property |
| η | 0.0014153 | Pa×s | 376.58 | Joback Calculated Property |
| η | 0.0007194 | Pa×s | 404.37 | Joback Calculated Property |
| η | 0.0003989 | Pa×s | 432.15 | Joback Calculated Property |
| η | 0.0002375 | Pa×s | 459.94 | Joback Calculated Property |
| η | 0.0001500 | Pa×s | 487.73 | Joback Calculated Property |
| η | 0.0000996 | Pa×s | 515.52 | Joback Calculated Property |
| ΔsubH | 99.70 ± 0.60 | kJ/mol | 321.00 | NIST |
| Psub | [1.31e-04; 1.14e-03] | kPa | [312.17; 330.19] |
|
| Psub | 1.34e-04 | kPa | 312.17 | Thermod... |
| Psub | 1.31e-04 | kPa | 312.17 | Thermod... |
| Psub | 1.39e-04 | kPa | 312.17 | Thermod... |
| Psub | 1.77e-04 | kPa | 314.20 | Thermod... |
| Psub | 1.71e-04 | kPa | 314.20 | Thermod... |
| Psub | 1.68e-04 | kPa | 314.20 | Thermod... |
| Psub | 2.16e-04 | kPa | 316.20 | Thermod... |
| Psub | 2.33e-04 | kPa | 316.20 | Thermod... |
| Psub | 2.20e-04 | kPa | 316.20 | Thermod... |
| Psub | 2.88e-04 | kPa | 318.19 | Thermod... |
| Psub | 2.80e-04 | kPa | 318.19 | Thermod... |
| Psub | 2.75e-04 | kPa | 318.19 | Thermod... |
| Psub | 3.77e-04 | kPa | 320.18 | Thermod... |
| Psub | 3.58e-04 | kPa | 320.18 | Thermod... |
| Psub | 3.53e-04 | kPa | 320.18 | Thermod... |
| Psub | 4.40e-04 | kPa | 322.20 | Thermod... |
| Psub | 4.53e-04 | kPa | 322.20 | Thermod... |
| Psub | 4.62e-04 | kPa | 322.20 | Thermod... |
| Psub | 5.81e-04 | kPa | 324.17 | Thermod... |
| Psub | 5.57e-04 | kPa | 324.17 | Thermod... |
| Psub | 5.42e-04 | kPa | 324.17 | Thermod... |
| Psub | 7.38e-04 | kPa | 326.22 | Thermod... |
| Psub | 7.12e-04 | kPa | 326.22 | Thermod... |
| Psub | 6.94e-04 | kPa | 326.22 | Thermod... |
| Psub | 9.07e-04 | kPa | 328.18 | Thermod... |
| Psub | 8.71e-04 | kPa | 328.18 | Thermod... |
| Psub | 8.49e-04 | kPa | 328.18 | Thermod... |
| Psub | 1.14e-03 | kPa | 330.19 | Thermod... |
| Psub | 1.09e-03 | kPa | 330.19 | Thermod... |
| Psub | 1.06e-03 | kPa | 330.19 | Thermod... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 464.20 | K | 6.70 | NIST |
Similar Compounds
![3-(3-[Trifluoromethyl]phenoxy)benzaldehyde.](data:image/png;base64,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)
Find more compounds similar to Benzaldehyde, 3-hydroxy-.
Mixtures
- Carbon dioxide + Benzaldehyde, 3-hydroxy-
- Carbon dioxide + Benzaldehyde, 3-hydroxy- + Benzaldehyde, 4-hydroxy-
- Biphenyl + Benzaldehyde, 3-hydroxy-
- Norflurane + Benzaldehyde, 3-hydroxy-
- Norflurane + Benzaldehyde, 3-hydroxy- + Benzaldehyde, 4-hydroxy-
Sources
- Crippen Method
- Crippen Method
- Measurement and modeling for solubility of 3-hydroxybenzaldehyde and its mixture with 4-hydroxybenzaldehyde in supercritical carbon dioxide
- Thermodynamic study on hydroxybenzaldehyde derivatives: 3- and 4-Hydroxybenzaldehyde isomers and 3,5-di-tert-butyl-2-hydroxybenzaldehyde
- Synthesis and characterization of novel binary organic monotectic and eutectic alloys
- Solubilities of hydroxybenzaldehyde isomers and their mixture in subcritical 1,1,1,2-tetrafluoroethane
- Joback 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.