- InChI
- InChI=1S/C10H18O/c1-9(2)7-4-5-10(3,6-7)8(9)11/h7-8,11H,4-6H2,1-3H3/t7-,8+,10?/m0/s1
- InChI Key
- IAIHUHQCLTYTSF-VLCSVPMDSA-N
- Formula
- C10H18O
- SMILES
- CC12CCC(C1)C(C)(C)C2O
- Molecular Weight1
- 154.25
- CAS
- 1632-73-1
- Other Names
-
- Bicyclo[2.2.1]heptan-2-ol, 1,3,3-trimethyl-
- 2-Norbornanol, 1,3,3-trimethyl-
- Fenchyl alcohol
- 1,3,3-Trimethyl-2-norbornanol
- 2-Fenchanol
- 1,3,3-Trimethylbicyclo[2.2.1]heptan-2-ol
- Fenchylic alcohol
- D-Fenchyl alcohol
- (+)-Fenchol
- 3,3-dimethyl-8,9-dinorbornan-2-ol
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- 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.
- 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 |
|---|---|---|---|
| ΔfusH° | 9.46 | kJ/mol | Joback Calculated Property |
| logPoct/wat | 2.194 | Crippen Calculated Property | |
| McVol | 135.910 | ml/mol | McGowan Calculated Property |
| Inp | [1084.00; 1138.00] |
|
|
| Inp | 1120.00 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1107.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | 1119.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1121.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1125.60 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1124.00 | NIST | |
| Inp | 1121.00 | NIST | |
| Inp | 1121.00 | NIST | |
| Inp | 1119.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1112.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1115.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1110.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1103.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1098.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1105.00 | NIST | |
| Inp | Outlier 1084.00 | NIST | |
| Inp | 1121.00 | NIST | |
| Inp | Outlier 1138.00 | NIST | |
| Inp | Outlier 1088.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1111.00 | NIST | |
| Inp | 1101.00 | NIST | |
| Inp | 1100.00 | NIST | |
| Inp | Outlier 1084.00 | NIST | |
| Inp | 1117.00 | NIST | |
| I | [1548.00; 1605.00] |
|
|
| I | 1580.00 | NIST | |
| I | 1574.00 | NIST | |
| I | 1571.00 | NIST | |
| I | 1582.00 | NIST | |
| I | 1597.00 | NIST | |
| I | 1582.00 | NIST | |
| I | 1573.00 | NIST | |
| I | 1570.00 | NIST | |
| I | 1577.00 | NIST | |
| I | 1588.00 | NIST | |
| I | 1581.00 | NIST | |
| I | 1582.00 | NIST | |
| I | 1580.00 | NIST | |
| I | 1571.00 | NIST | |
| I | 1584.00 | NIST | |
| I | 1574.00 | NIST | |
| I | 1588.00 | NIST | |
| I | 1591.00 | NIST | |
| I | 1589.00 | NIST | |
| I | Outlier 1549.00 | NIST | |
| I | 1589.00 | NIST | |
| I | 1573.00 | NIST | |
| I | Outlier 1548.00 | NIST | |
| I | 1574.00 | NIST | |
| I | 1585.00 | NIST | |
| I | 1571.00 | NIST | |
| I | 1591.00 | NIST | |
| I | Outlier 1554.00 | NIST | |
| I | 1576.00 | NIST | |
| I | 1598.00 | NIST | |
| I | 1598.00 | NIST | |
| I | 1598.00 | NIST | |
| I | 1598.00 | NIST | |
| I | 1598.00 | NIST | |
| I | 1598.00 | NIST | |
| I | 1598.00 | NIST | |
| I | 1570.00 | NIST | |
| I | 1580.00 | NIST | |
| I | 1591.00 | NIST | |
| I | 1591.00 | NIST | |
| I | 1605.00 | NIST | |
| I | 1584.00 | NIST | |
| I | 1591.00 | NIST | |
| I | 1580.00 | NIST | |
| I | 1588.00 | NIST | |
| I | 1573.00 | NIST | |
| I | 1598.00 | NIST | |
| I | 1570.00 | NIST | |
| Tfus | [314.65; 319.15] | K |
|
| Tfus | 319.15 ± 1.50 | K | NIST |
| Tfus | 314.65 ± 0.20 | K | NIST |
Cheméo can also estimate Normal Boiling Point Temperature, Critical Temperature, Critical Pressure, Critical Volume, Enthalpy of formation at standard conditions, Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, Ionization energy, Log10 of Water solubility in mol/l 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.
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [175.02; 543.14] | 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 | -1.94620e+02 | |||
| Coefficient B | 1.81086e+00 | |||
| Coefficient C | -1.89900e-03 | |||
| Coefficient D | 8.25900e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 175.02 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 244.92 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 301.47 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 347.29 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 385.00 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 417.19 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 446.49 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 475.51 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 506.85 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 543.14 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.34; 103.05] | kPa | [332.30; 472.40] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.31645e+01 | |||
| Coefficient B | -2.97546e+03 | |||
| Coefficient C | -1.23546e+02 | |||
| Reference | Pickett and Peterson, 1929 | |||
| Temperature range, min. | 332.30 | |||
| Temperature range, max. | 472.40 | |||
| Pvap | 0.34 | kPa | 332.30 | Calculated Property |
| Pvap | 0.90 | kPa | 347.87 | Calculated Property |
| Pvap | 2.14 | kPa | 363.43 | Calculated Property |
| Pvap | 4.56 | kPa | 379.00 | Calculated Property |
| Pvap | 8.90 | kPa | 394.57 | Calculated Property |
| Pvap | 16.15 | kPa | 410.13 | Calculated Property |
| Pvap | 27.58 | kPa | 425.70 | Calculated Property |
| Pvap | 44.68 | kPa | 441.27 | Calculated Property |
| Pvap | 69.19 | kPa | 456.83 | Calculated Property |
| Pvap | 103.05 | kPa | 472.40 | Calculated Property |
Similar Compounds
Find more compounds similar to Fenchol.
Sources
- 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
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
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