- 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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 340 360 380 400 500 550 600 650 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 0.02 0.04 0.06 0.08 300 400 500 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 | ||||
| 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
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.