- InChI
- InChI=1S/C6H4Cl2O/c7-4-1-5(8)3-6(9)2-4/h1-3,9H
- InChI Key
- VPOMSPZBQMDLTM-UHFFFAOYSA-N
- Formula
- C6H4Cl2O
- SMILES
- Oc1cc(Cl)cc(Cl)c1
- Molecular Weight1
- 163.00
- CAS
- 591-35-5
- Other Names
-
- 3,5-Dichlorophenol
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- 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).
- 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).
- Tboilr : Boiling point at reduced pressure (K).
- Tfus : Normal melting (fusion) point (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | -2749.10 ± 0.60 | kJ/mol | NIST |
| ΔfH°gas | -148.20 ± 1.50 | kJ/mol | NIST |
| ΔfH°solid | -231.00 ± 1.00 | kJ/mol | NIST |
| ΔfusH° | 19.13 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [82.80; 82.80] | kJ/mol |
|
| ΔsubH° | 82.80 ± 1.10 | kJ/mol | NIST |
| ΔsubH° | 82.80 ± 1.10 | kJ/mol | NIST |
| ΔvapH° | 71.21 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.95 | eV | Relay (1.0) Calculated Property |
| log10WS | [-1.34; -1.34] |
|
|
| log10WS | -1.34 | Aq. Solubility Prediction | |
| log10WS | -1.34 | Estimated Solubility | |
| logPoct/wat | 2.699 | Crippen Calculated Property | |
| McVol | 101.990 | ml/mol | McGowan Calculated Property |
| Inp | [1358.00; 1400.00] |
|
|
| Inp | 1375.00 | NIST | |
| Inp | 1358.00 | NIST | |
| Inp | 1375.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1367.00 | NIST | |
| Inp | 1362.00 | NIST | |
| Inp | 1362.00 | NIST | |
| Inp | 1399.90 | NIST | |
| Inp | 1370.00 | NIST | |
| Inp | 1400.00 | NIST | |
| Inp | 1395.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1375.00 | NIST | |
| Inp | 1370.00 | NIST | |
| Inp | 1367.00 | NIST | |
| Inp | 1391.00 | NIST | |
| I | [2670.00; 2713.00] |
|
|
| I | 2675.00 | NIST | |
| I | 2675.00 | NIST | |
| I | 2691.00 | NIST | |
| I | 2713.00 | NIST | |
| I | 2707.00 | NIST | |
| I | 2670.00 | NIST | |
| I | 2700.00 | NIST | |
| I | 2675.00 | NIST | |
| Tboil | 506.20 | K | NIST |
| Tfus | [340.48; 341.00] | K |
|
| Tfus | 340.48 | K | Aq. Solubility Prediction |
| Tfus | 341.00 ± 0.20 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [20.51; 20.51] | kJ/mol | [341.00; 341.00] |
|
| ΔfusH | 20.51 | kJ/mol | 341.00 | NIST |
| ΔfusH | 20.51 | kJ/mol | 341.00 | NIST |
| ΔfusH | 20.51 | kJ/mol | 341.00 | NIST |
| ΔsubH | 71.80 | kJ/mol | 284.00 | NIST |
| ΔfusS | 60.14 | J/mol×K | 341.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 396.20 | K | 1.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [121.76; 246.27] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -5.31000e+00 | |||
| Coefficient B | 6.03600e-01 | |||
| Coefficient C | -5.63920e-04 | |||
| Coefficient D | 2.11900e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 121.76 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 147.03 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 167.89 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 184.99 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 199.00 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 210.60 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 220.46 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 229.24 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 237.62 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 246.27 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0039922; 0.0000721] | Pa×s | [340.74; 539.51] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.64202e+01 | |||
| Coefficient B | 3.71298e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 340.74 | |||
| Temperature range, max. | 539.51 | |||
| η | 0.0039922 | Pa×s | 340.74 | Calculated Property |
| η | 0.0020566 | Pa×s | 362.83 | Calculated Property |
| η | 0.0011432 | Pa×s | 384.91 | Calculated Property |
| η | 0.0006773 | Pa×s | 407.00 | Calculated Property |
| η | 0.0004235 | Pa×s | 429.08 | Calculated Property |
| η | 0.0002773 | Pa×s | 451.17 | Calculated Property |
| η | 0.0001889 | Pa×s | 473.25 | Calculated Property |
| η | 0.0001331 | Pa×s | 495.34 | Calculated Property |
| η | 0.0000967 | Pa×s | 517.42 | Calculated Property |
| η | 0.0000721 | Pa×s | 539.51 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.68] | kPa | [403.69; 522.25] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.24185e+01 | |||
| Coefficient B | -8.93405e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Temperature range, min. | 403.69 | |||
| Temperature range, max. | 522.25 | |||
| Pvap | 1.33 | kPa | 403.69 | Calculated Property |
| Pvap | 2.68 | kPa | 416.86 | Calculated Property |
| Pvap | 5.17 | kPa | 430.04 | Calculated Property |
| Pvap | 9.59 | kPa | 443.21 | Calculated Property |
| Pvap | 17.16 | kPa | 456.38 | Calculated Property |
| Pvap | 29.72 | kPa | 469.56 | Calculated Property |
| Pvap | 49.96 | kPa | 482.73 | Calculated Property |
| Pvap | 81.68 | kPa | 495.90 | Calculated Property |
| Pvap | 130.19 | kPa | 509.08 | Calculated Property |
| Pvap | 202.68 | kPa | 522.25 | Calculated Property |
Similar Compounds
Find more compounds similar to Phenol, 3,5-dichloro-.
Sources
- Cheméo Relay (1.0)
- Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
- Crippen Method
- Joback Method
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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