- InChI
- InChI=1S/C8H16O/c9-7-6-8-4-2-1-3-5-8/h8-9H,1-7H2
- InChI Key
- QJQZRLXDLORINA-UHFFFAOYSA-N
- Formula
- C8H16O
- SMILES
- OCCC1CCCCC1
- Molecular Weight1
- 128.21
- CAS
- 4442-79-9
- Other Names
-
- (2-hydroxyethyl)cyclohexane
- .beta.-cyclohexylethyl alcohol
- 2-Cyclohexylethyl alcohol
- 2-cyclohexylethanol
- Ethanol, 2-cyclohexyl-
- Hexahydrophenylethyl alcohol
- NSC 30157
- cyclohexylethanol
- cyclohexylethyl alcohol
- «beta»-Cyclohexyl ethanol
- «beta»-Cyclohexylethyl alcohol
- 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).
- 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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | -95.89 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -306.36 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 12.40 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 50.51 | kJ/mol | Joback Calculated Property |
| log10WS | -2.09 | Crippen Calculated Property | |
| logPoct/wat | 1.949 | Crippen Calculated Property | |
| McVol | 118.590 | ml/mol | McGowan Calculated Property |
| Pc | 3505.43 | kPa | Joback Calculated Property |
| Inp | [1098.00; 1098.00] |
|
|
| Inp | 1098.00 | NIST | |
| Inp | 1098.00 | NIST | |
| I | [1668.00; 1668.00] |
|
|
| I | 1668.00 | NIST | |
| I | 1668.00 | NIST | |
| Tboil | 494.17 | K | Joback Calculated Property |
| Tc | 684.73 | K | Joback Calculated Property |
| Tfus | 248.12 | K | Joback Calculated Property |
| Vc | 0.435 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [274.70; 353.26] | J/mol×K | [494.17; 684.73] |
|
| Cp,gas | 274.70 | J/mol×K | 494.17 | Joback Calculated Property |
| Cp,gas | 289.54 | J/mol×K | 525.93 | Joback Calculated Property |
| Cp,gas | 303.66 | J/mol×K | 557.69 | Joback Calculated Property |
| Cp,gas | 317.07 | J/mol×K | 589.45 | Joback Calculated Property |
| Cp,gas | 329.79 | J/mol×K | 621.21 | Joback Calculated Property |
| Cp,gas | 341.85 | J/mol×K | 652.97 | Joback Calculated Property |
| Cp,gas | 353.26 | J/mol×K | 684.73 | Joback Calculated Property |
| Cp,liquid | [222.00; 323.27] | J/mol×K | [253.50; 352.54] |
|
| Cp,liquid | 223.33 | J/mol×K | 253.50 | Heat Ca... |
| Cp,liquid | 222.00 | J/mol×K | 253.50 | Heat Ca... |
| Cp,liquid | 226.07 | J/mol×K | 256.05 | Heat Ca... |
| Cp,liquid | 226.32 | J/mol×K | 256.05 | Heat Ca... |
| Cp,liquid | 229.40 | J/mol×K | 260.65 | Heat Ca... |
| Cp,liquid | 229.73 | J/mol×K | 260.65 | Heat Ca... |
| Cp,liquid | 233.72 | J/mol×K | 265.75 | Heat Ca... |
| Cp,liquid | 233.97 | J/mol×K | 265.75 | Heat Ca... |
| Cp,liquid | 238.29 | J/mol×K | 270.86 | Heat Ca... |
| Cp,liquid | 238.21 | J/mol×K | 270.86 | Heat Ca... |
| Cp,liquid | 242.20 | J/mol×K | 275.96 | Heat Ca... |
| Cp,liquid | 242.12 | J/mol×K | 275.96 | Heat Ca... |
| Cp,liquid | 246.19 | J/mol×K | 281.07 | Heat Ca... |
| Cp,liquid | 246.44 | J/mol×K | 281.07 | Heat Ca... |
| Cp,liquid | 251.60 | J/mol×K | 286.17 | Heat Ca... |
| Cp,liquid | 251.26 | J/mol×K | 286.17 | Heat Ca... |
| Cp,liquid | 256.67 | J/mol×K | 291.28 | Heat Ca... |
| Cp,liquid | 256.42 | J/mol×K | 291.28 | Heat Ca... |
| Cp,liquid | 261.91 | J/mol×K | 296.38 | Heat Ca... |
| Cp,liquid | 262.07 | J/mol×K | 296.38 | Heat Ca... |
| Cp,liquid | 267.56 | J/mol×K | 301.48 | Heat Ca... |
| Cp,liquid | 266.98 | J/mol×K | 301.48 | Heat Ca... |
| Cp,liquid | 273.21 | J/mol×K | 306.59 | Heat Ca... |
| Cp,liquid | 273.13 | J/mol×K | 306.59 | Heat Ca... |
| Cp,liquid | 278.70 | J/mol×K | 311.70 | Heat Ca... |
| Cp,liquid | 279.03 | J/mol×K | 311.70 | Heat Ca... |
| Cp,liquid | 284.35 | J/mol×K | 316.81 | Heat Ca... |
| Cp,liquid | 284.35 | J/mol×K | 316.81 | Heat Ca... |
| Cp,liquid | 290.17 | J/mol×K | 321.91 | Heat Ca... |
| Cp,liquid | 289.93 | J/mol×K | 321.91 | Heat Ca... |
| Cp,liquid | 295.50 | J/mol×K | 327.01 | Heat Ca... |
| Cp,liquid | 295.58 | J/mol×K | 327.01 | Heat Ca... |
| Cp,liquid | 300.82 | J/mol×K | 332.12 | Heat Ca... |
| Cp,liquid | 301.15 | J/mol×K | 332.12 | Heat Ca... |
| Cp,liquid | 307.39 | J/mol×K | 337.22 | Heat Ca... |
| Cp,liquid | 306.64 | J/mol×K | 337.22 | Heat Ca... |
| Cp,liquid | 312.71 | J/mol×K | 342.33 | Heat Ca... |
| Cp,liquid | 313.87 | J/mol×K | 342.33 | Heat Ca... |
| Cp,liquid | 318.61 | J/mol×K | 347.43 | Heat Ca... |
| Cp,liquid | 317.95 | J/mol×K | 347.43 | Heat Ca... |
| Cp,liquid | 322.60 | J/mol×K | 352.54 | Heat Ca... |
| Cp,liquid | 323.27 | J/mol×K | 352.54 | Heat Ca... |
| η | [0.0001736; 0.0593770] | Pa×s | [248.12; 494.17] |
|
| η | 0.0593770 | Pa×s | 248.12 | Joback Calculated Property |
| η | 0.0112664 | Pa×s | 289.13 | Joback Calculated Property |
| η | 0.0032306 | Pa×s | 330.14 | Joback Calculated Property |
| η | 0.0012208 | Pa×s | 371.14 | Joback Calculated Property |
| η | 0.0005599 | Pa×s | 412.15 | Joback Calculated Property |
| η | 0.0002957 | Pa×s | 453.16 | Joback Calculated Property |
| η | 0.0001736 | Pa×s | 494.17 | Joback Calculated Property |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 479.70 | K | 99.30 | NIST |
Similar Compounds
Find more compounds similar to Cyclohexaneethanol.
Mixtures
Sources
- Crippen Method
- Crippen Method
- (Solid + liquid) equilibrium phase diagrams in binary mixtures containing terpenes: New experimental data and analysis of several modelling strategies with modified UNIFAC (Dortmund) and PC-SAFT equation of state
- Solubility of fragrance raw materials in water: Experimental study, correlations, and Mod. UNIFAC (Do) predictions
- Heat Capacities of 2-Propenol and Selected Cyclohexylalcohols
- 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.