- InChI
- InChI=1S/C7H14O/c8-6-7-4-2-1-3-5-7/h7-8H,1-6H2
- InChI Key
- VSSAZBXXNIABDN-UHFFFAOYSA-N
- Formula
- C7H14O
- SMILES
- OCC1CCCCC1
- Molecular Weight1
- 114.19
- CAS
- 100-49-2
- Other Names
-
- (hydroxymethyl)cyclohexane
- Benzyl alcohol, hexahydro-
- Cyclohexanecarbinol
- Cyclohexylmethyl alcohol
- Methanol, cyclohexyl-
- NSC 5288
- USAF DO-49
- cyclohexylcarbinol
- cyclohexylmethanol
- hexahydrobenzyl alcohol
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (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).
- ρl : Liquid Density (kg/m3).
- 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 |
|---|---|---|---|
| PAff | 802.10 | kJ/mol | NIST |
| BasG | 771.70 | kJ/mol | NIST |
| ΔcH°liquid | -4377.30 | kJ/mol | NIST |
| ΔfG° | -104.31 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -285.72 | kJ/mol | Joback Calculated Property |
| ΔfH°liquid | -378.00 | kJ/mol | NIST |
| ΔfusH° | 9.81 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 48.28 | kJ/mol | Joback Calculated Property |
| log10WS | -1.67 | Crippen Calculated Property | |
| logPoct/wat | 1.559 | Crippen Calculated Property | |
| McVol | 104.500 | ml/mol | McGowan Calculated Property |
| Pc | 3940.66 | kPa | Joback Calculated Property |
| Tboil | [454.20; 456.20] | K |
|
| Tboil | 454.20 | K | NIST |
| Tboil | 456.20 | K | NIST |
| Tc | 664.09 | K | Joback Calculated Property |
| Tfus | 236.85 | K | Joback Calculated Property |
| Vc | 0.380 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [230.52; 304.24] | J/mol×K | [471.29; 664.09] |
|
| Cp,gas | 230.52 | J/mol×K | 471.29 | Joback Calculated Property |
| Cp,gas | 244.45 | J/mol×K | 503.42 | Joback Calculated Property |
| Cp,gas | 257.70 | J/mol×K | 535.56 | Joback Calculated Property |
| Cp,gas | 270.29 | J/mol×K | 567.69 | Joback Calculated Property |
| Cp,gas | 282.23 | J/mol×K | 599.82 | Joback Calculated Property |
| Cp,gas | 293.54 | J/mol×K | 631.95 | Joback Calculated Property |
| Cp,gas | 304.24 | J/mol×K | 664.09 | Joback Calculated Property |
| Cp,liquid | [198.88; 296.83] | J/mol×K | [258.09; 355.09] |
|
| Cp,liquid | 198.88 | J/mol×K | 258.09 | Heat Ca... |
| Cp,liquid | 199.13 | J/mol×K | 258.09 | Heat Ca... |
| Cp,liquid | 202.87 | J/mol×K | 263.20 | Heat Ca... |
| Cp,liquid | 202.54 | J/mol×K | 263.20 | Heat Ca... |
| Cp,liquid | 206.61 | J/mol×K | 268.30 | Heat Ca... |
| Cp,liquid | 207.03 | J/mol×K | 268.30 | Heat Ca... |
| Cp,liquid | 211.52 | J/mol×K | 273.41 | Heat Ca... |
| Cp,liquid | 210.94 | J/mol×K | 273.41 | Heat Ca... |
| Cp,liquid | 215.68 | J/mol×K | 278.51 | Heat Ca... |
| Cp,liquid | 215.18 | J/mol×K | 278.51 | Heat Ca... |
| Cp,liquid | 219.83 | J/mol×K | 283.62 | Heat Ca... |
| Cp,liquid | 220.83 | J/mol×K | 283.62 | Heat Ca... |
| Cp,liquid | 225.32 | J/mol×K | 288.72 | Heat Ca... |
| Cp,liquid | 224.74 | J/mol×K | 288.72 | Heat Ca... |
| Cp,liquid | 230.56 | J/mol×K | 293.83 | Heat Ca... |
| Cp,liquid | 229.98 | J/mol×K | 293.83 | Heat Ca... |
| Cp,liquid | 236.46 | J/mol×K | 298.93 | Heat Ca... |
| Cp,liquid | 235.55 | J/mol×K | 298.93 | Heat Ca... |
| Cp,liquid | 242.28 | J/mol×K | 304.04 | Heat Ca... |
| Cp,liquid | 241.62 | J/mol×K | 304.04 | Heat Ca... |
| Cp,liquid | 247.36 | J/mol×K | 309.14 | Heat Ca... |
| Cp,liquid | 247.94 | J/mol×K | 309.14 | Heat Ca... |
| Cp,liquid | 254.26 | J/mol×K | 314.25 | Heat Ca... |
| Cp,liquid | 253.34 | J/mol×K | 314.25 | Heat Ca... |
| Cp,liquid | 260.24 | J/mol×K | 319.35 | Heat Ca... |
| Cp,liquid | 259.49 | J/mol×K | 319.35 | Heat Ca... |
| Cp,liquid | 265.98 | J/mol×K | 324.46 | Heat Ca... |
| Cp,liquid | 265.56 | J/mol×K | 324.46 | Heat Ca... |
| Cp,liquid | 271.38 | J/mol×K | 329.57 | Heat Ca... |
| Cp,liquid | 270.55 | J/mol×K | 329.57 | Heat Ca... |
| Cp,liquid | 276.54 | J/mol×K | 334.67 | Heat Ca... |
| Cp,liquid | 275.87 | J/mol×K | 334.67 | Heat Ca... |
| Cp,liquid | 281.78 | J/mol×K | 339.77 | Heat Ca... |
| Cp,liquid | 280.86 | J/mol×K | 339.77 | Heat Ca... |
| Cp,liquid | 287.35 | J/mol×K | 344.88 | Heat Ca... |
| Cp,liquid | 286.52 | J/mol×K | 344.88 | Heat Ca... |
| Cp,liquid | 292.34 | J/mol×K | 349.98 | Heat Ca... |
| Cp,liquid | 291.51 | J/mol×K | 349.98 | Heat Ca... |
| Cp,liquid | 296.83 | J/mol×K | 355.09 | Heat Ca... |
| Cp,liquid | 296.33 | J/mol×K | 355.09 | Heat Ca... |
| η | [0.0002056; 0.0757236] | Pa×s | [236.85; 471.29] |
|
| η | 0.0757236 | Pa×s | 236.85 | Joback Calculated Property |
| η | 0.0140832 | Pa×s | 275.92 | Joback Calculated Property |
| η | 0.0039756 | Pa×s | 315.00 | Joback Calculated Property |
| η | 0.0014837 | Pa×s | 354.07 | Joback Calculated Property |
| η | 0.0006736 | Pa×s | 393.14 | Joback Calculated Property |
| η | 0.0003527 | Pa×s | 432.22 | Joback Calculated Property |
| η | 0.0002056 | Pa×s | 471.29 | Joback Calculated Property |
| ρl | [900.67; 929.96] | kg/m3 | [293.15; 333.15] |
|
| ρl | 929.76 | kg/m3 | 293.15 | Density... |
| ρl | 929.96 | kg/m3 | 293.15 | Density... |
| ρl | 926.43 | kg/m3 | 298.15 | Density... |
| ρl | 926.25 | kg/m3 | 298.15 | Density... |
| ρl | 922.71 | kg/m3 | 303.15 | Density... |
| ρl | 922.87 | kg/m3 | 303.15 | Density... |
| ρl | 919.14 | kg/m3 | 308.15 | Density... |
| ρl | 919.28 | kg/m3 | 308.15 | Density... |
| ρl | 915.53 | kg/m3 | 313.15 | Density... |
| ρl | 915.66 | kg/m3 | 313.15 | Density... |
| ρl | 911.88 | kg/m3 | 318.15 | Density... |
| ρl | 912.00 | kg/m3 | 318.15 | Density... |
| ρl | 908.31 | kg/m3 | 323.15 | Density... |
| ρl | 908.19 | kg/m3 | 323.15 | Density... |
| ρl | 904.57 | kg/m3 | 328.15 | Density... |
| ρl | 904.45 | kg/m3 | 328.15 | Density... |
| ρl | 900.78 | kg/m3 | 333.15 | Density... |
| ρl | 900.67 | kg/m3 | 333.15 | Density... |
Similar Compounds
Find more compounds similar to Cyclohexanemethanol.
Mixtures
- Cyclohexanemethanol + Dodecane
- Cyclohexanemethanol + Cyclohexane, methyl-
- Cyclohexanemethanol + Adamantane, 1,3-dimethyl-
- Cyclohexanemethanol + 1-Ethyladamantane
- Cyclohexanemethanol + 1,3,5-Trimethyladamantane
Sources
- Crippen Method
- Crippen Method
- Heat Capacities of 2-Propenol and Selected Cyclohexylalcohols
- Density, Viscosity, and Freezing Point for Four Binary Systems of n-Dodecane or Methylcyclohexane Mixed with 1-Heptanol or Cyclohexylmethanol
- Density, Viscosity, Refractive Index, and Surface Tension for Six Binary Systems of Adamantane Derivatives with 1-Heptanol and Cyclohexylmethanol
- Joback Method
- 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.