- InChI
- InChI=1S/C7H14O/c1-6-4-2-3-5-7(6)8/h6-8H,2-5H2,1H3
- InChI Key
- NDVWOBYBJYUSMF-UHFFFAOYSA-N
- Formula
- C7H14O
- SMILES
- CC1CCCCC1O
- Molecular Weight1
- 114.19
- CAS
- 583-59-5
- Other Names
-
- 1-Methyl-2-cyclohexanol
- 2-Methyl-1-cyclohexanol
- 2-Methylcyclohexyl alcohol
- 2-methylcyclohexanol
- 2-methylcyclohexanol, mixed isomers
- Cyclohexanol, o-methyl-
- NSC 75845
- o-Methylcyclohexanol
- ω : Acentric Factor.
- 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).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- 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).
- n0 : Refractive Index.
- Inp : Non-polar retention indices.
- γ : Surface Tension (N/m).
- 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 |
|---|---|---|---|
| ω | 0.4657 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -4380.20 | kJ/mol | NIST |
| ΔfG° | -112.02 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -295.47 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 10.88 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 63.30 | kJ/mol | NIST |
| IE | 9.64 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.16 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.557 | Crippen Calculated Property | |
| McVol | 104.500 | ml/mol | McGowan Calculated Property |
| Pc | 3782.33 | kPa | Joback Calculated Property |
| Inp | [941.00; 973.00] |
|
|
| Inp | 946.00 | NIST | |
| Inp | 973.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 941.00 | NIST | |
| Inp | 941.00 | NIST | |
| Tboil | [437.70; 441.65] | K |
|
| Tboil | 437.70 | K | NIST |
| Tboil | 441.65 ± 0.50 | K | NIST |
| Tboil | 440.70 ± 1.00 | K | NIST |
| Tc | 650.27 | K | Relay (1.0) Calculated Property |
| Tfus | 253.36 | K | Relay (1.0) Calculated Property |
| Vc | 0.368 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [231.31; 307.19] | J/mol×K | [466.82; 659.38] |
|
| Cp,gas | 231.31 | J/mol×K | 466.82 | Joback Calculated Property |
| Cp,gas | 245.55 | J/mol×K | 498.91 | Joback Calculated Property |
| Cp,gas | 259.14 | J/mol×K | 531.01 | Joback Calculated Property |
| Cp,gas | 272.09 | J/mol×K | 563.10 | Joback Calculated Property |
| Cp,gas | 284.40 | J/mol×K | 595.19 | Joback Calculated Property |
| Cp,gas | 296.10 | J/mol×K | 627.28 | Joback Calculated Property |
| Cp,gas | 307.19 | J/mol×K | 659.38 | Joback Calculated Property |
| Cp,liquid | [199.60; 267.44] | J/mol×K | [290.00; 298.15] |
|
| Cp,liquid | 199.60 | J/mol×K | 290.00 | NIST |
| Cp,liquid | 267.44 | J/mol×K | 298.15 | NIST |
| η | [0.0002174; 0.0550246] | Pa×s | [232.61; 466.82] |
|
| η | 0.0550246 | Pa×s | 232.61 | Joback Calculated Property |
| η | 0.0112769 | Pa×s | 271.64 | Joback Calculated Property |
| η | 0.0034419 | Pa×s | 310.68 | Joback Calculated Property |
| η | 0.0013692 | Pa×s | 349.72 | Joback Calculated Property |
| η | 0.0006554 | Pa×s | 388.75 | Joback Calculated Property |
| η | 0.0003589 | Pa×s | 427.78 | Joback Calculated Property |
| η | 0.0002174 | Pa×s | 466.82 | Joback Calculated Property |
| ΔvapH | 51.70 | kJ/mol | 400.00 | NIST |
| n0 | 1.46313 | 293.10 | Vapor-Liquid Equilibria in the 2-Methylcyclohexanol + 2-Methylcyclohexyl Ethanoate System at 101.325 kPa | |
| γ | [0.03; 0.03] | N/m | [293.15; 323.15] |
|
| γ | 0.03 | N/m | 293.15 | Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols |
| γ | 0.03 | N/m | 298.15 | Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols |
| γ | 0.03 | N/m | 303.15 | Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols |
| γ | 0.03 | N/m | 308.15 | Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols |
| γ | 0.03 | N/m | 313.15 | Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols |
| γ | 0.03 | N/m | 318.15 | Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols |
| γ | 0.03 | N/m | 323.15 | Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [341.12; 459.80] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.70042e+01 | |||
| Coefficient B | -4.61743e+03 | |||
| Coefficient C | -6.49020e+01 | |||
| Temperature range, min. | 341.12 | |||
| Temperature range, max. | 459.80 | |||
| Pvap | 1.33 | kPa | 341.12 | Calculated Property |
| Pvap | 2.86 | kPa | 354.31 | Calculated Property |
| Pvap | 5.72 | kPa | 367.49 | Calculated Property |
| Pvap | 10.82 | kPa | 380.68 | Calculated Property |
| Pvap | 19.45 | kPa | 393.87 | Calculated Property |
| Pvap | 33.41 | kPa | 407.05 | Calculated Property |
| Pvap | 55.13 | kPa | 420.24 | Calculated Property |
| Pvap | 87.77 | kPa | 433.43 | Calculated Property |
| Pvap | 135.31 | kPa | 446.61 | Calculated Property |
| Pvap | 202.65 | kPa | 459.80 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclohexanol, 2-methyl-.
Mixtures
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Surface Properties of Pure Liquids and Binary Liquid Mixtures of Ethylene Glycol + Methylcyclohexanols
- Vapor-Liquid Equilibria in the 2-Methylcyclohexanol + 2-Methylcyclohexyl Ethanoate System at 101.325 kPa
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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