- InChI
- InChI=1S/C8H18O2/c1-2-3-4-5-7-10-8-6-9/h9H,2-8H2,1H3
- InChI Key
- UPGSWASWQBLSKZ-UHFFFAOYSA-N
- Formula
- C8H18O2
- SMILES
- CCCCCCOCCO
- Molecular Weight1
- 146.23
- CAS
- 112-25-4
- Other Names
-
- 2-(Hexyloxy)ethanol
- 2-Hexoxyethanol
- 2-hexyloxyethanol
- 3-oxa-1-nonanol
- Cellosolve, n-hexyl-
- Ethylene glycol mono-n-hexyl ether
- Ethylene glycol monohexyl ether
- Ethylene glycol n-hexyl ether
- Glycol monohexyl ether
- Hexyl cellosolve
- ethanol, 2-hexyloxy-
- ethyleneglycol, hexyl ether
- hexylglycol
- n-Hexyl Cellosolve
- 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (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.
- 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° | -225.34 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -492.90 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 21.75 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 52.49 | kJ/mol | Joback Calculated Property |
| log10WS | -1.52 | Crippen Calculated Property | |
| logPoct/wat | 1.576 | Crippen Calculated Property | |
| McVol | 135.320 | ml/mol | McGowan Calculated Property |
| Pc | 2738.28 | kPa | Joback Calculated Property |
| Inp | [1090.00; 1106.00] |
|
|
| Inp | 1090.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1106.00 | NIST | |
| Tboil | [481.20; 532.25] | K |
|
| Tboil | 481.20 | K | NIST |
| Tboil | 532.25 | K | NIST |
| Tc | 656.87 | K | Joback Calculated Property |
| Tfus | 232.95 | K | NIST |
| Vc | 0.520 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [314.61; 377.28] | J/mol×K | [497.04; 656.87] |
|
| Cp,gas | 314.61 | J/mol×K | 497.04 | Joback Calculated Property |
| Cp,gas | 325.99 | J/mol×K | 523.68 | Joback Calculated Property |
| Cp,gas | 337.00 | J/mol×K | 550.32 | Joback Calculated Property |
| Cp,gas | 347.62 | J/mol×K | 576.95 | Joback Calculated Property |
| Cp,gas | 357.88 | J/mol×K | 603.59 | Joback Calculated Property |
| Cp,gas | 367.76 | J/mol×K | 630.23 | Joback Calculated Property |
| Cp,gas | 377.28 | J/mol×K | 656.87 | Joback Calculated Property |
| η | [0.0001328; 0.0241515] | Pa×s | [262.97; 497.04] |
|
| η | 0.0241515 | Pa×s | 262.97 | Joback Calculated Property |
| η | 0.0057953 | Pa×s | 301.98 | Joback Calculated Property |
| η | 0.0019277 | Pa×s | 340.99 | Joback Calculated Property |
| η | 0.0008038 | Pa×s | 380.00 | Joback Calculated Property |
| η | 0.0003945 | Pa×s | 419.02 | Joback Calculated Property |
| η | 0.0002185 | Pa×s | 458.03 | Joback Calculated Property |
| η | 0.0001328 | Pa×s | 497.04 | Joback Calculated Property |
| ΔvapH | 54.60 | kJ/mol | 423.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [371.26; 506.85] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.62888e+01 | |||
| Coefficient B | -4.74063e+03 | |||
| Coefficient C | -7.49930e+01 | |||
| Temperature range, min. | 371.26 | |||
| Temperature range, max. | 506.85 | |||
| Pvap | 1.33 | kPa | 371.26 | Calculated Property |
| Pvap | 2.89 | kPa | 386.33 | Calculated Property |
| Pvap | 5.84 | kPa | 401.39 | Calculated Property |
| Pvap | 11.08 | kPa | 416.46 | Calculated Property |
| Pvap | 19.93 | kPa | 431.52 | Calculated Property |
| Pvap | 34.17 | kPa | 446.59 | Calculated Property |
| Pvap | 56.17 | kPa | 461.65 | Calculated Property |
| Pvap | 88.96 | kPa | 476.72 | Calculated Property |
| Pvap | 136.28 | kPa | 491.78 | Calculated Property |
| Pvap | 202.65 | kPa | 506.85 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethanol, 2-(hexyloxy)-.
Mixtures
Sources
- Crippen Method
- Crippen Method
- Mutual Solubility and Lower Critical Solution Temperature for Water + Glycol Ether Systems
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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