- InChI
- InChI=1S/C10H22O/c1-3-4-5-6-7-8-9-10(2)11/h10-11H,3-9H2,1-2H3
- InChI Key
- ACUZDYFTRHEKOS-UHFFFAOYSA-N
- Formula
- C10H22O
- SMILES
- CCCCCCCCC(C)O
- Molecular Weight1
- 158.28
- CAS
- 1120-06-5
- Other Names
-
- 2-Hydroxydecane
- Decan-2-ol
- Decanol-2
- Methyl-n-octyl carbinol
- 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).
- 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).
- ρc : Critical density (kg/m3).
- 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° | -105.94 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -407.24 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 22.22 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 54.14 | kJ/mol | Joback Calculated Property |
| log10WS | -3.38 | Crippen Calculated Property | |
| logPoct/wat | 3.118 | Crippen Calculated Property | |
| McVol | 157.630 | ml/mol | McGowan Calculated Property |
| Pc | 2315.84 | kPa | Joback Calculated Property |
| ρc | [245.34; 245.34] | kg/m3 |
|
| ρc | 245.34 | kg/m3 | NIST |
| ρc | 245.34 ± 6.33 | kg/m3 | NIST |
| Inp | [1185.00; 1211.00] |
|
|
| Inp | 1190.00 | NIST | |
| Inp | 1209.00 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1203.70 | NIST | |
| Inp | 1185.00 | NIST | |
| Inp | 1195.00 | NIST | |
| Inp | 1186.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1198.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1209.00 | NIST | |
| Inp | 1197.00 | NIST | |
| Inp | 1190.00 | NIST | |
| Inp | 1211.00 | NIST | |
| I | [1585.00; 1622.00] |
|
|
| I | 1592.00 | NIST | |
| I | 1596.00 | NIST | |
| I | 1613.00 | NIST | |
| I | 1606.00 | NIST | |
| I | 1621.00 | NIST | |
| I | 1622.00 | NIST | |
| I | 1585.00 | NIST | |
| I | 1585.00 | NIST | |
| I | 1621.00 | NIST | |
| I | 1585.00 | NIST | |
| Tboil | [482.15; 484.20] | K |
|
| Tboil | 484.20 | K | NIST |
| Tboil | 482.15 ± 3.00 | K | NIST |
| Tboil | 483.15 ± 3.00 | K | NIST |
| Tboil | 483.65 ± 3.00 | K | NIST |
| Tc | [668.59; 669.00] | K |
|
| Tc | 669.00 ± 1.00 | K | NIST |
| Tc | 668.60 | K | NIST |
| Tc | 668.59 ± 0.30 | K | NIST |
| Tfus | 270.80 ± 1.00 | K | NIST |
| Vc | 0.646 | m3/kmol | NIST |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [380.84; 454.40] | J/mol×K | [519.94; 681.25] |
|
| Cp,gas | 380.84 | J/mol×K | 519.94 | Joback Calculated Property |
| Cp,gas | 394.36 | J/mol×K | 546.83 | Joback Calculated Property |
| Cp,gas | 407.36 | J/mol×K | 573.71 | Joback Calculated Property |
| Cp,gas | 419.85 | J/mol×K | 600.60 | Joback Calculated Property |
| Cp,gas | 431.84 | J/mol×K | 627.48 | Joback Calculated Property |
| Cp,gas | 443.35 | J/mol×K | 654.37 | Joback Calculated Property |
| Cp,gas | 454.40 | J/mol×K | 681.25 | Joback Calculated Property |
| η | [0.0001173; 0.0660457] | Pa×s | [248.28; 519.94] |
|
| η | 0.0660457 | Pa×s | 248.28 | Joback Calculated Property |
| η | 0.0101842 | Pa×s | 293.56 | Joback Calculated Property |
| η | 0.0025882 | Pa×s | 338.83 | Joback Calculated Property |
| η | 0.0009085 | Pa×s | 384.11 | Joback Calculated Property |
| η | 0.0003977 | Pa×s | 429.39 | Joback Calculated Property |
| η | 0.0002038 | Pa×s | 474.66 | Joback Calculated Property |
| η | 0.0001173 | Pa×s | 519.94 | Joback Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.62] | kPa | [379.12; 508.21] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.70528e+01 | |||
| Coefficient B | -5.05821e+03 | |||
| Coefficient C | -7.74120e+01 | |||
| Temperature range, min. | 379.12 | |||
| Temperature range, max. | 508.21 | |||
| Pvap | 1.33 | kPa | 379.12 | Calculated Property |
| Pvap | 2.85 | kPa | 393.46 | Calculated Property |
| Pvap | 5.72 | kPa | 407.81 | Calculated Property |
| Pvap | 10.81 | kPa | 422.15 | Calculated Property |
| Pvap | 19.42 | kPa | 436.49 | Calculated Property |
| Pvap | 33.36 | kPa | 450.84 | Calculated Property |
| Pvap | 55.06 | kPa | 465.18 | Calculated Property |
| Pvap | 87.68 | kPa | 479.52 | Calculated Property |
| Pvap | 135.23 | kPa | 493.87 | Calculated Property |
| Pvap | 202.62 | kPa | 508.21 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Decanol.
Sources
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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