- 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»)-
- 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-Methyl-2-(1-methylethyl)cyclohexanol, (1«alpha»,2«beta»,5«alpha»)-
- 5«alpha»-Methyl-2«beta»-(1«alpha»-methylethyl)cyclohexanol
- 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, 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
- MENTHOL
- MENTHOMENTHOL
- Menthacamphor
- Menthol terpine hydrate
- Menthol, cis-1,3,trans-1,4-
- 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).
- 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 a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- 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.
- 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 |
|---|---|---|---|
| ΔfG° | -96.91 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -393.60 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 16.20 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 53.96 | kJ/mol | Joback Calculated Property |
| log10WS | -2.55 | Crippen Calculated Property | |
| logPoct/wat | 2.440 | Crippen Calculated Property | |
| McVol | 146.770 | ml/mol | McGowan Calculated Property |
| Pc | 2659.77 | kPa | Joback 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 | 1173.00 | NIST | |
| Inp | 1175.00 | NIST | |
| Inp | 1182.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1165.00 | NIST | |
| I | [1589.00; 1652.00] |
|
|
| I | 1640.00 | NIST | |
| I | 1642.00 | NIST | |
| I | 1619.00 | NIST | |
| I | 1632.00 | NIST | |
| I | 1631.00 | 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 | |
| Tboil | 489.50 | K | KDB |
| 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 |
| Vc | 0.539 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [370.36; 463.40] | J/mol×K | [530.15; 719.67] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 380 400 420 440 460 550 600 650 700 | ||||
| Cp,gas | 370.36 | J/mol×K | 530.15 | Joback Calculated Property |
| Cp,gas | 387.84 | J/mol×K | 561.74 | Joback Calculated Property |
| Cp,gas | 404.52 | J/mol×K | 593.32 | Joback Calculated Property |
| Cp,gas | 420.40 | J/mol×K | 624.91 | Joback Calculated Property |
| Cp,gas | 435.50 | J/mol×K | 656.49 | Joback Calculated Property |
| Cp,gas | 449.82 | J/mol×K | 688.08 | Joback Calculated Property |
| Cp,gas | 463.40 | J/mol×K | 719.67 | Joback Calculated Property |
| η | [0.0001446; 0.0430815] | Pa×s | [247.18; 530.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.01 0.02 0.03 0.04 300 400 500 | ||||
| η | 0.0430815 | Pa×s | 247.18 | Joback Calculated Property |
| η | 0.0077902 | Pa×s | 294.34 | Joback Calculated Property |
| η | 0.0022592 | Pa×s | 341.50 | Joback Calculated Property |
| η | 0.0008847 | Pa×s | 388.66 | Joback Calculated Property |
| η | 0.0004244 | Pa×s | 435.83 | Joback Calculated Property |
| η | 0.0002350 | Pa×s | 482.99 | Joback Calculated Property |
| η | 0.0001446 | Pa×s | 530.15 | Joback Calculated Property |
| 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 |
|---|---|---|---|---|
| Pvap | [0.13; 101.24] | kPa | [329.15; 485.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.60468e+01 | |||
| Coefficient B | -9.08243e+03 | |||
| Coefficient C | -7.05284e+00 | |||
| Coefficient D | 3.86441e-06 | |||
| Temperature range, min. | 329.15 | |||
| Temperature range, max. | 485.15 | |||
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 350 400 450 | ||||
| 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 |
Similar Compounds
![Cyclohexanol, 5-methyl-2-(1-methylethyl)-, [1S-(1«alpha»,2«alpha»,5«beta»)]-.](data:image/png;base64,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)
Sources
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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.