- InChI
- InChI=1S/C10H20O/c1-7(2)9-5-4-8(3)6-10(9)11/h7-11H,4-6H2,1-3H3/t8-,9+,10-/m1/s1
- InChI Key
- NOOLISFMXDJSKH-KXUCPTDWSA-N
- Formula
- C10H20O
- SMILES
- CC1CCC(C(C)C)C(O)C1
- Molecular Weight1
- 156.27
- CAS
- 89-78-1
- Other Names
-
- (.+/-.)-Menthol
- 2-Isopropyl-5-methylcyclohexanol
- 2-Isopropyl-5-methylcyclohexanol, (1«alpha»,2«beta»,5«alpha»)-
- 3-p-Menthanol
- 5-Methyl-2-(1-methylethyl)cyclohexanol
- 5-Methyl-2-(1-methylethyl)cyclohexanol, (1«alpha»,2«beta»,5«alpha»)-
- 5«alpha»-Methyl-2«beta»-(1«alpha»-methylethyl)cyclohexanol
- Cyclohexanol, 2-isopropyl-5-methyl-
- Cyclohexanol, 2-isopropyl-5-methyl-, (1«alpha»,2«beta»,5«alpha»)-
- Cyclohexanol, 5-methyl-2-(1-methylethyl)-, (1R,2S,5R)-rel-
- Diterpene
- Fancol menthol
- Fisherman's friend lozenges
- Hexahydrothymol
- Menthacamphor
- Menthol
- Menthol terpine hydrate
- Menthol, cis-1,3,trans-1,4-
- Menthomenthol
- NCI-C50000
- NSC 2603
- Peppermint camphor
- Racementhol
- Racemic menthol
- Therapeutic mineral ice
- component of Dermoplast
- component of Minut-rub
- component of Robitussin cough drops
- component of Sarna
- component of Theragesic
- dl-Menthol
- l-Menthol
- p-Menthan-3-ol
- rac-Menthol
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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 a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- IE : Ionization energy (eV).
- 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.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (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 |
|---|---|---|---|
| ΔfH°gas | -347.50 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 16.20 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 74.01 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.15 | eV | Relay (1.0) Calculated Property |
| logPoct/wat | 2.440 | Crippen Calculated Property | |
| McVol | 146.770 | ml/mol | McGowan Calculated Property |
| Inp | [198.32; 1194.00] |
|
|
| Inp | 1166.60 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1163.00 | NIST | |
| Inp | 1161.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1150.20 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1140.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1180.78 | NIST | |
| Inp | 1180.91 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1167.00 | NIST | |
| Inp | 1153.30 | NIST | |
| Inp | 1153.30 | NIST | |
| Inp | 1153.30 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1180.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1149.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1188.00 | NIST | |
| Inp | 1179.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1173.70 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1191.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1152.00 | NIST | |
| Inp | 1153.00 | NIST | |
| Inp | 1155.00 | NIST | |
| Inp | 1168.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1163.00 | NIST | |
| Inp | 1163.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1148.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1158.00 | NIST | |
| Inp | Outlier 198.32 | NIST | |
| Inp | 1166.60 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1165.00 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1141.00 | NIST | |
| Inp | 1163.00 | NIST | |
| I | [1589.00; 1652.00] |
|
|
| I | 1641.00 | NIST | |
| I | 1636.00 | NIST | |
| I | 1637.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1631.00 | NIST | |
| I | 1640.00 | NIST | |
| I | 1642.00 | NIST | |
| I | 1619.00 | NIST | |
| I | 1632.00 | NIST | |
| I | 1631.00 | NIST | |
| I | 1618.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1632.00 | NIST | |
| I | 1612.00 | NIST | |
| I | 1630.00 | NIST | |
| I | 1637.00 | NIST | |
| I | 1636.00 | NIST | |
| I | 1642.00 | NIST | |
| I | 1646.00 | NIST | |
| I | 1627.00 | NIST | |
| I | 1615.00 | NIST | |
| I | 1644.00 | NIST | |
| I | 1637.00 | NIST | |
| I | 1641.00 | NIST | |
| I | 1639.00 | NIST | |
| I | 1645.00 | NIST | |
| I | 1652.00 | NIST | |
| I | 1636.00 | NIST | |
| I | 1636.00 | NIST | |
| I | Outlier 1589.00 | NIST | |
| I | 1631.00 | NIST | |
| I | 1628.00 | NIST | |
| I | 1641.00 | NIST | |
| I | 1637.00 | NIST | |
| I | 1614.00 | NIST | |
| I | 1637.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1651.00 | NIST | |
| I | 1612.00 | NIST | |
| I | 1640.00 | NIST | |
| I | 1642.00 | NIST | |
| I | Outlier 1600.00 | NIST | |
| I | 1631.00 | NIST | |
| I | 1649.00 | NIST | |
| I | 1635.00 | NIST | |
| I | 1637.00 | NIST | |
| I | 1638.00 | NIST | |
| I | 1608.00 | NIST | |
| I | 1652.00 | NIST | |
| I | 1612.00 | NIST | |
| I | 1638.00 | NIST | |
| I | 1636.00 | NIST | |
| I | 1612.00 | NIST | |
| I | 1642.00 | NIST | |
| I | 1649.00 | NIST | |
| I | 1652.00 | NIST | |
| Tboil | [489.45; 489.65] | K |
|
| Tboil | 489.50 | K | KDB |
| Tboil | 489.45 ± 0.60 | K | NIST |
| Tboil | 489.55 ± 0.40 | K | NIST |
| Tboil | 489.65 ± 0.30 | K | NIST |
| Tboil | 489.55 ± 0.50 | K | NIST |
| Tboil | 489.60 ± 0.50 | K | NIST |
| Tboil | 489.60 ± 0.50 | K | NIST |
| Tc | [694.00; 694.00] | K |
|
| Tc | 694.00 | K | KDB |
| Tc | 694.00 ± 5.00 | K | NIST |
| Tfus | [314.00; 315.15] | K |
|
| Tfus | 315.00 | K | KDB |
| Tfus | 314.00 ± 0.60 | K | NIST |
| Tfus | 315.15 ± 0.50 | K | NIST |
Cheméo can also estimate Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor, 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.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [10.25; 11.88] | kJ/mol | [301.20; 316.20] |
|
| ΔfusH | 10.25 | kJ/mol | 301.20 | NIST |
| ΔfusH | 11.88 | kJ/mol | 316.20 | NIST |
| ΔsubH | 79.00 ± 4.00 | kJ/mol | 289.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [196.22; 552.84] | 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 | -5.63200e+01 | |||
| Coefficient B | 1.06286e+00 | |||
| Coefficient C | -5.24000e-04 | |||
| Coefficient D | 7.03000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 196.22 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 257.23 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 312.37 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 361.87 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 405.95 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 444.84 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 478.74 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 507.90 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 532.52 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 552.84 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0043604; 0.0002277] | Pa×s | [314.72; 485.80] |
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 | -1.38184e+01 | |||
| Coefficient B | 2.63834e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 314.72 | |||
| Temperature range, max. | 485.80 | |||
| η | 0.0043604 | Pa×s | 314.72 | Calculated Property |
| η | 0.0027048 | Pa×s | 333.73 | Calculated Property |
| η | 0.0017665 | Pa×s | 352.74 | Calculated Property |
| η | 0.0012051 | Pa×s | 371.74 | Calculated Property |
| η | 0.0008532 | Pa×s | 390.75 | Calculated Property |
| η | 0.0006238 | Pa×s | 409.76 | Calculated Property |
| η | 0.0004689 | Pa×s | 428.77 | Calculated Property |
| η | 0.0003611 | Pa×s | 447.78 | Calculated Property |
| η | 0.0002841 | Pa×s | 466.79 | Calculated Property |
| η | 0.0002277 | Pa×s | 485.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.13; 101.24] | kPa | [329.15; 485.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 6.60468e+01 | |||
| Coefficient B | -9.08243e+03 | |||
| Coefficient C | -7.05284e+00 | |||
| Coefficient D | 3.86441e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 329.15 | |||
| Temperature range, max. | 485.15 | |||
| Pvap | 0.13 | kPa | 329.15 | Calculated Property |
| Pvap | 0.39 | kPa | 346.48 | Calculated Property |
| Pvap | 1.01 | kPa | 363.82 | Calculated Property |
| Pvap | 2.37 | kPa | 381.15 | Calculated Property |
| Pvap | 5.14 | kPa | 398.48 | Calculated Property |
| Pvap | 10.40 | kPa | 415.82 | Calculated Property |
| Pvap | 19.79 | kPa | 433.15 | Calculated Property |
| Pvap | 35.67 | kPa | 450.48 | Calculated Property |
| Pvap | 61.35 | kPa | 467.82 | Calculated Property |
| Pvap | 101.24 | kPa | 485.15 | Calculated Property |
| Pvap | [0.13; 100.65] | kPa | [329.00; 485.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.70011e+01 | |||
| Coefficient B | -5.53990e+03 | |||
| Coefficient C | -3.78530e+01 | |||
| Reference | Stull, 1947 | |||
| Temperature range, min. | 329.00 | |||
| Temperature range, max. | 485.00 | |||
| Pvap | 0.13 | kPa | 329.00 | Calculated Property |
| Pvap | 0.38 | kPa | 346.33 | Calculated Property |
| Pvap | 1.00 | kPa | 363.67 | Calculated Property |
| Pvap | 2.36 | kPa | 381.00 | Calculated Property |
| Pvap | 5.12 | kPa | 398.33 | Calculated Property |
| Pvap | 10.36 | kPa | 415.67 | Calculated Property |
| Pvap | 19.71 | kPa | 433.00 | Calculated Property |
| Pvap | 35.53 | kPa | 450.33 | Calculated Property |
| Pvap | 61.07 | kPa | 467.67 | Calculated Property |
| Pvap | 100.65 | kPa | 485.00 | Calculated Property |
Similar Compounds
![Cyclohexanol, 5-methyl-2-(1-methylethyl)-, [1S-(1«alpha»,2«beta»,5«beta»)]-.](data:image/png;base64,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)
Sources
- KDB Vapor Pressure Data
- 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
- Crippen Method
- Joback Method
- KDB
- 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.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.
These property values are available through the Cheméo API. A free account gives you an access key.