- InChI
- InChI=1S/C6H5ClO/c7-5-2-1-3-6(8)4-5/h1-4,8H
- InChI Key
- HORNXRXVQWOLPJ-UHFFFAOYSA-N
- Formula
- C6H5ClO
- SMILES
- Oc1cccc(Cl)c1
- Molecular Weight1
- 128.56
- CAS
- 108-43-0
- Other Names
-
- 3-Chlorophenol
- 3-Hydroxychlorobenzene
- NSC 59700
- Phenol, m-chloro-
- m-Chlorophenic acid
- m-Chlorophenol
- meta-Chlorophenol
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- 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).
- 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).
- Psub : Sublimation 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°liquid | -2910.00 ± 8.40 | kJ/mol | NIST |
| ΔcH°solid | -2890.00 ± 8.00 | kJ/mol | NIST |
| ΔfG° | -54.50 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -123.69 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.32 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 76.90 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 63.50 ± 0.30 | kJ/mol | NIST |
| IE | [8.65; 8.68] | eV |
|
| IE | 8.65 ± 0.00 | eV | NIST |
| IE | 8.65 ± 0.00 | eV | NIST |
| IE | 8.68 ± 0.00 | eV | NIST |
| IE | 8.65 ± 0.03 | eV | NIST |
| log10WS | [-0.70; -0.70] |
|
|
| log10WS | -0.70 | Aq. Sol... | |
| log10WS | -0.70 | Estimat... | |
| logPoct/wat | 2.046 | Crippen Calculated Property | |
| McVol | 89.750 | ml/mol | McGowan Calculated Property |
| Pc | 5478.85 | kPa | Joback Calculated Property |
| Inp | [1157.00; 1207.00] |
|
|
| Inp | 1157.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1157.00 | NIST | |
| Inp | 1161.00 | NIST | |
| Inp | 1189.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1167.00 | NIST | |
| Inp | 1203.30 | NIST | |
| Inp | 1198.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1207.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1200.00 | NIST | |
| Inp | 1203.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1194.00 | NIST | |
| I | [2333.00; 2380.00] |
|
|
| I | 2371.00 | NIST | |
| I | 2371.00 | NIST | |
| I | 2371.00 | NIST | |
| I | 2380.00 | NIST | |
| I | 2364.00 | NIST | |
| I | 2333.00 | NIST | |
| I | 2350.00 | NIST | |
| I | 2345.00 | NIST | |
| I | 2378.00 | NIST | |
| I | 2345.00 | NIST | |
| Tboil | 487.20 | K | NIST |
| Tc | 721.38 | K | Joback Calculated Property |
| Tfus | [305.50; 306.08] | K |
|
| Tfus | 306.08 | K | Aq. Sol... |
| Tfus | 305.50 | K | Solid l... |
| Tfus | 305.80 ± 0.20 | K | NIST |
| Vc | 0.279 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [167.36; 208.73] | J/mol×K | [481.41; 721.38] |
|
| Cp,gas | 167.36 | J/mol×K | 481.41 | Joback Calculated Property |
| Cp,gas | 176.00 | J/mol×K | 521.40 | Joback Calculated Property |
| Cp,gas | 183.82 | J/mol×K | 561.40 | Joback Calculated Property |
| Cp,gas | 190.92 | J/mol×K | 601.39 | Joback Calculated Property |
| Cp,gas | 197.38 | J/mol×K | 641.39 | Joback Calculated Property |
| Cp,gas | 203.28 | J/mol×K | 681.38 | Joback Calculated Property |
| Cp,gas | 208.73 | J/mol×K | 721.38 | Joback Calculated Property |
| η | [0.0001241; 0.0044385] | Pa×s | [325.44; 481.41] |
|
| η | 0.0044385 | Pa×s | 325.44 | Joback Calculated Property |
| η | 0.0019615 | Pa×s | 351.44 | Joback Calculated Property |
| η | 0.0009700 | Pa×s | 377.43 | Joback Calculated Property |
| η | 0.0005253 | Pa×s | 403.42 | Joback Calculated Property |
| η | 0.0003064 | Pa×s | 429.42 | Joback Calculated Property |
| η | 0.0001900 | Pa×s | 455.41 | Joback Calculated Property |
| η | 0.0001241 | Pa×s | 481.41 | Joback Calculated Property |
| ΔfusH | [14.90; 14.91] | kJ/mol | [305.80; 305.80] |
|
| ΔfusH | 14.90 | kJ/mol | 305.80 | NIST |
| ΔfusH | 14.91 | kJ/mol | 305.80 | NIST |
| ΔfusH | 14.91 | kJ/mol | 305.80 | NIST |
| ΔsubH | 53.00 ± 1.00 | kJ/mol | 301.00 | NIST |
| ΔvapH | [53.10; 61.90] | kJ/mol | [321.50; 402.00] |
|
| ΔvapH | 61.90 | kJ/mol | 321.50 | NIST |
| ΔvapH | 53.10 | kJ/mol | 402.00 | NIST |
| Psub | [8.20e-04; 0.02] | kPa | [275.30; 306.00] |
|
| Psub | 8.20e-04 | kPa | 275.30 | Thermoc... |
| Psub | 9.50e-04 | kPa | 276.60 | Thermoc... |
| Psub | 1.15e-03 | kPa | 278.30 | Thermoc... |
| Psub | 1.49e-03 | kPa | 280.30 | Thermoc... |
| Psub | 2.12e-03 | kPa | 283.20 | Thermoc... |
| Psub | 2.62e-03 | kPa | 285.20 | Thermoc... |
| Psub | 3.66e-03 | kPa | 288.30 | Thermoc... |
| Psub | 5.09e-03 | kPa | 291.30 | Thermoc... |
| Psub | 7.21e-03 | kPa | 294.30 | Thermoc... |
| Psub | 9.99e-03 | kPa | 297.30 | Thermoc... |
| Psub | 0.01 | kPa | 300.30 | Thermoc... |
| Psub | 0.02 | kPa | 302.20 | Thermoc... |
| Psub | 0.02 | kPa | 306.00 | Thermoc... |
| ΔfusS | 48.74 | J/mol×K | 305.80 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [359.36; 454.72] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 2.34612e+01 | |||
| Coefficient B | -7.98338e+03 | |||
| Coefficient C | -1.48550e+01 | |||
| Temperature range, min. | 359.36 | |||
| Temperature range, max. | 454.72 | |||
| Pvap | 1.33 | kPa | 359.36 | Calculated Property |
| Pvap | 2.66 | kPa | 369.96 | Calculated Property |
| Pvap | 5.11 | kPa | 380.55 | Calculated Property |
| Pvap | 9.44 | kPa | 391.15 | Calculated Property |
| Pvap | 16.88 | kPa | 401.74 | Calculated Property |
| Pvap | 29.26 | kPa | 412.34 | Calculated Property |
| Pvap | 49.29 | kPa | 422.93 | Calculated Property |
| Pvap | 80.87 | kPa | 433.53 | Calculated Property |
| Pvap | 129.48 | kPa | 444.12 | Calculated Property |
| Pvap | 202.66 | kPa | 454.72 | Calculated Property |
Similar Compounds
Find more compounds similar to Phenol, 3-chloro-.
Mixtures
- Phenol, 3-chloro- + Phenol, 4-chloro-
- 2-Propanol, 2-methyl- + Phenol, 3-chloro-
- 2-Propanol, 2-methyl- + Phenol, 3-chloro- + Phenol, 4-chloro-
- Phenol, 3-chloro- + Water
Sources
- Crippen Method
- Solid liquid equilibria of mixtures containing tert-butanol, m-chlorophenol, and p-chlorophenol and development of adductive crystallization processes
- Investigating the solubility of chlorophenols in hydrophobic ionic liquids
- Thermochemistry of Chlorobenzenes and Chlorophenols: Ambient Temperature Vapor Pressures and Enthalpies of Phase Transitions
- Joback Method
- 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.