- InChI
- InChI=1S/C9H20O/c1-3-5-6-7-8-9(10)4-2/h9-10H,3-8H2,1-2H3
- InChI Key
- GYSCXPVAKHVAAY-UHFFFAOYSA-N
- Formula
- C9H20O
- SMILES
- CCCCCCC(O)CC
- Molecular Weight1
- 144.25
- CAS
- 624-51-1
- Other Names
-
- Hexylethylcarbinol
- nonan-3-ol
- 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).
- 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 |
|---|---|---|---|
| Cp,liquid | 373.62 | J/mol×K | Vapour ... |
| ΔfG° | -114.36 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -386.60 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 19.63 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 70.90 ± 0.30 | kJ/mol | NIST |
| log10WS | -2.97 | Crippen Calculated Property | |
| logPoct/wat | 2.728 | Crippen Calculated Property | |
| McVol | 143.540 | ml/mol | McGowan Calculated Property |
| Pc | 2545.61 | kPa | Joback Calculated Property |
| ρc | [249.56; 249.56] | kg/m3 |
|
| ρc | 249.56 | kg/m3 | NIST |
| ρc | 249.56 ± 5.77 | kg/m3 | NIST |
| Inp | [1069.00; 1099.00] |
|
|
| Inp | 1099.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1090.00 | NIST | |
| Inp | 1099.00 | NIST | |
| I | [1459.00; 1496.00] |
|
|
| I | 1459.00 | NIST | |
| I | 1461.00 | NIST | |
| I | 1493.00 | NIST | |
| I | 1489.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1496.00 | NIST | |
| I | 1493.00 | NIST | |
| Tboil | 467.90 ± 3.00 | K | NIST |
| Tc | [648.00; 648.00] | K |
|
| Tc | 648.00 ± 1.00 | K | NIST |
| Tc | 648.00 | K | NIST |
| Tc | 648.00 ± 0.30 | K | NIST |
| Tfus | 237.01 | K | Joback Calculated Property |
| Vc | 0.577 | m3/kmol | NIST |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [334.58; 403.87] | J/mol×K | [497.06; 659.14] |
|
| Cp,gas | 334.58 | J/mol×K | 497.06 | Joback Calculated Property |
| Cp,gas | 347.30 | J/mol×K | 524.07 | Joback Calculated Property |
| Cp,gas | 359.54 | J/mol×K | 551.09 | Joback Calculated Property |
| Cp,gas | 371.30 | J/mol×K | 578.10 | Joback Calculated Property |
| Cp,gas | 382.60 | J/mol×K | 605.11 | Joback Calculated Property |
| Cp,gas | 393.45 | J/mol×K | 632.13 | Joback Calculated Property |
| Cp,gas | 403.87 | J/mol×K | 659.14 | Joback Calculated Property |
| η | [0.0001409; 0.0878509] | Pa×s | [237.01; 497.06] |
|
| η | 0.0878509 | Pa×s | 237.01 | Joback Calculated Property |
| η | 0.0131188 | Pa×s | 280.35 | Joback Calculated Property |
| η | 0.0032599 | Pa×s | 323.69 | Joback Calculated Property |
| η | 0.0011254 | Pa×s | 367.03 | Joback Calculated Property |
| η | 0.0004864 | Pa×s | 410.38 | Joback Calculated Property |
| η | 0.0002468 | Pa×s | 453.72 | Joback Calculated Property |
| η | 0.0001409 | Pa×s | 497.06 | Joback Calculated Property |
| ΔvapH | [57.10; 75.50] | kJ/mol | [313.00; 417.00] |
|
| ΔvapH | 75.50 | kJ/mol | 313.00 | NIST |
| ΔvapH | 57.10 | kJ/mol | 417.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [356.53; 493.43] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.69298e+01 | |||
| Coefficient B | -5.26910e+03 | |||
| Coefficient C | -3.99180e+01 | |||
| Temperature range, min. | 356.53 | |||
| Temperature range, max. | 493.43 | |||
| Pvap | 1.33 | kPa | 356.53 | Calculated Property |
| Pvap | 2.86 | kPa | 371.74 | Calculated Property |
| Pvap | 5.74 | kPa | 386.95 | Calculated Property |
| Pvap | 10.85 | kPa | 402.16 | Calculated Property |
| Pvap | 19.50 | kPa | 417.37 | Calculated Property |
| Pvap | 33.48 | kPa | 432.59 | Calculated Property |
| Pvap | 55.23 | kPa | 447.80 | Calculated Property |
| Pvap | 87.88 | kPa | 463.01 | Calculated Property |
| Pvap | 135.39 | kPa | 478.22 | Calculated Property |
| Pvap | 202.63 | kPa | 493.43 | Calculated Property |
Similar Compounds
Find more compounds similar to 3-Nonanol.
Sources
- Crippen Method
- Crippen Method
- Vapour pressures and heat capacity measurements on the C7 C9 secondary aliphatic alcohols
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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