- InChI
- InChI=1S/C6H5NO3/c8-6-4-2-1-3-5(6)7(9)10/h1-4,8H
- InChI Key
- IQUPABOKLQSFBK-UHFFFAOYSA-N
- Formula
- C6H5NO3
- SMILES
- O=[N+]([O-])c1ccccc1O
- Molecular Weight1
- 139.11
- CAS
- 88-75-5
- Other Names
-
- 2-Hydroxynitrobenzene
- 2-Nitrophenol
- Phenol, o-nitro-
- UN 1663
- o-Hydroxynitrobenzene
- o-Nitrofenol
- o-Nitrophenol
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- 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).
- 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).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- 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 |
|---|---|---|---|
| ΔcH°solid | [-2887.00; -2871.00] | kJ/mol |
|
| ΔcH°solid | -2871.00 ± 1.30 | kJ/mol | NIST |
| ΔcH°solid | -2873.27 ± 0.62 | kJ/mol | NIST |
| ΔcH°solid | -2876.30 | kJ/mol | NIST |
| ΔcH°solid | -2887.00 | kJ/mol | NIST |
| ΔcH°solid | -2878.80 | kJ/mol | NIST |
| ΔfG° | -7.02 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-132.30; -128.80] | kJ/mol |
|
| ΔfH°gas | -132.30 ± 1.40 | kJ/mol | NIST |
| ΔfH°gas | -128.80 ± 1.60 | kJ/mol | NIST |
| ΔfH°solid | [-210.00; -199.30] | kJ/mol |
|
| ΔfH°solid | -204.60 ± 1.40 | kJ/mol | NIST |
| ΔfH°solid | -202.40 ± 1.00 | kJ/mol | NIST |
| ΔfH°solid | -199.30 | kJ/mol | NIST |
| ΔfH°solid | -210.00 | kJ/mol | NIST |
| ΔfusH° | 22.48 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [72.30; 73.30] | kJ/mol |
|
| ΔsubH° | 72.30 ± 0.28 | kJ/mol | NIST |
| ΔsubH° | 73.30 | kJ/mol | NIST |
| ΔvapH° | 58.40 ± 0.50 | kJ/mol | NIST |
| IE | [9.10; 9.29] | eV |
|
| IE | 9.10 | eV | NIST |
| IE | 9.29 | eV | NIST |
| log10WS | [-1.74; -1.74] |
|
|
| log10WS | -1.74 | Aq. Sol... | |
| log10WS | -1.74 | Estimat... | |
| logPoct/wat | 1.300 | Crippen Calculated Property | |
| McVol | 94.930 | ml/mol | McGowan Calculated Property |
| Pc | 5899.00 | kPa | Joback Calculated Property |
| Inp | [188.90; 1166.00] |
|
|
| Inp | 1166.00 | NIST | |
| Inp | 1149.00 | NIST | |
| Inp | 1136.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1133.00 | NIST | |
| Inp | 1154.10 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1126.00 | NIST | |
| Inp | 1149.00 | NIST | |
| Inp | Outlier 188.90 | NIST | |
| Inp | Outlier 189.22 | NIST | |
| I | [1812.00; 1818.00] |
|
|
| I | 1812.00 | NIST | |
| I | 1814.00 | NIST | |
| I | 1818.00 | NIST | |
| I | 1818.00 | NIST | |
| Tboil | [489.20; 490.40] | K |
|
| Tboil | 490.35 | K | KDB |
| Tboil | 489.20 | K | NIST |
| Tboil | 490.40 ± 0.70 | K | NIST |
| Tboil | 490.40 ± 0.40 | K | NIST |
| Tc | 861.12 | K | Joback Calculated Property |
| Tfus | [317.91; 318.05] | K |
|
| Tfus | 317.91 | K | Aq. Sol... |
| Tfus | 318.05 | K | KDB |
| Vc | 0.311 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [219.41; 261.56] | J/mol×K | [595.82; 861.12] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 220 230 240 250 260 600 700 800 | ||||
| Cp,gas | 219.41 | J/mol×K | 595.82 | Joback Calculated Property |
| Cp,gas | 228.08 | J/mol×K | 640.04 | Joback Calculated Property |
| Cp,gas | 235.93 | J/mol×K | 684.25 | Joback Calculated Property |
| Cp,gas | 243.08 | J/mol×K | 728.47 | Joback Calculated Property |
| Cp,gas | 249.65 | J/mol×K | 772.69 | Joback Calculated Property |
| Cp,gas | 255.77 | J/mol×K | 816.90 | Joback Calculated Property |
| Cp,gas | 261.56 | J/mol×K | 861.12 | Joback Calculated Property |
| ΔfusH | [17.05; 17.45] | kJ/mol | [316.30; 318.20] |
|
| ΔfusH | 17.05 | kJ/mol | 316.30 | NIST |
| ΔfusH | 17.45 | kJ/mol | 318.00 | NIST |
| ΔfusH | 17.45 | kJ/mol | 318.20 | NIST |
| ΔfusH | 17.45 | kJ/mol | 318.20 | NIST |
| ΔsubH | [54.80; 73.20] | kJ/mol | [282.50; 304.00] |
|
| ΔsubH | 54.80 | kJ/mol | 282.50 | NIST |
| ΔsubH | 73.00 ± 2.00 | kJ/mol | 303.00 | NIST |
| ΔsubH | 73.20 ± 1.30 | kJ/mol | 304.00 | NIST |
| ΔvapH | [54.40; 55.90] | kJ/mol | [339.50; 428.00] |
|
| ΔvapH | 54.40 | kJ/mol | 339.50 | NIST |
| ΔvapH | 55.90 | kJ/mol | 428.00 | NIST |
| ΔfusS | 54.86 | J/mol×K | 318.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [319.32; 541.31] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.07924e+01 | |||
| Coefficient B | -2.54411e+03 | |||
| Coefficient C | -7.71340e+01 | |||
| Temperature range, min. | 319.32 | |||
| Temperature range, max. | 541.31 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 500 | ||||
| Pvap | 1.33 | kPa | 319.32 | Calculated Property |
| Pvap | 3.52 | kPa | 343.99 | Calculated Property |
| Pvap | 7.89 | kPa | 368.65 | Calculated Property |
| Pvap | 15.58 | kPa | 393.32 | Calculated Property |
| Pvap | 27.89 | kPa | 417.98 | Calculated Property |
| Pvap | 46.15 | kPa | 442.65 | Calculated Property |
| Pvap | 71.66 | kPa | 467.31 | Calculated Property |
| Pvap | 105.60 | kPa | 491.98 | Calculated Property |
| Pvap | 148.99 | kPa | 516.64 | Calculated Property |
| Pvap | 202.64 | kPa | 541.31 | Calculated Property |
| Pvap | [1.13; 102.84] | kPa | [364.15; 495.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.39908e+02 | |||
| Coefficient B | -1.23899e+04 | |||
| Coefficient C | -1.81502e+01 | |||
| Coefficient D | 9.65481e-06 | |||
| Temperature range, min. | 364.15 | |||
| Temperature range, max. | 495.15 | |||
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 400 450 | ||||
| Pvap | 1.13 | kPa | 364.15 | Calculated Property |
| Pvap | 2.28 | kPa | 378.71 | Calculated Property |
| Pvap | 4.30 | kPa | 393.26 | Calculated Property |
| Pvap | 7.65 | kPa | 407.82 | Calculated Property |
| Pvap | 12.97 | kPa | 422.37 | Calculated Property |
| Pvap | 21.02 | kPa | 436.93 | Calculated Property |
| Pvap | 32.77 | kPa | 451.48 | Calculated Property |
| Pvap | 49.39 | kPa | 466.04 | Calculated Property |
| Pvap | 72.22 | kPa | 480.59 | Calculated Property |
| Pvap | 102.84 | kPa | 495.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Phenol, 2-nitro-.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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
that the value is more than 2 standard deviations away from the
property mean.