- InChI
- InChI=1S/C9H20O/c1-3-5-6-8-9(10)7-4-2/h9-10H,3-8H2,1-2H3
- InChI Key
- IXUOEGRSQCCEHB-UHFFFAOYSA-N
- Formula
- C9H20O
- SMILES
- CCCCCC(O)CCC
- Molecular Weight1
- 144.25
- CAS
- 5932-79-6
- Other Names
-
- nonan-4-ol
- ω : Acentric Factor.
- 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).
- 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).
- ρc : Critical density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : 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 |
|---|---|---|---|
| ω | 0.6640 | Relay (1.0) Calculated Property | |
| Cp,liquid | 367.85 | J/mol×K | Vapour pressures and heat capacity measurements on the C7 C9 secondary aliphatic alcohols |
| ΔfG° | -114.36 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -399.98 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 19.63 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 71.50 ± 0.30 | kJ/mol | NIST |
| IE | 9.73 | eV | Relay (1.0) Calculated Property |
| log10WS | -2.50 | Relay (1.0) 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 | [251.00; 251.00] | kg/m3 |
|
| ρc | 251.00 | kg/m3 | NIST |
| ρc | 251.00 ± 5.77 | kg/m3 | NIST |
| Inp | 1078.00 | NIST | |
| Ip | [1467.00; 1479.00] |
|
|
| Ip | 1467.00 | NIST | |
| Ip | 1479.00 | NIST | |
| Ip | 1474.00 | NIST | |
| Ip | 1474.00 | NIST | |
| Ip | 1479.00 | NIST | |
| Tboil | 465.65 ± 3.00 | K | NIST |
| Tc | [645.00; 645.10] | K |
|
| Tc | 645.10 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value |
| Tc | 645.00 ± 1.00 | K | NIST |
| Tc | 645.10 | K | NIST |
| Tc | 645.10 ± 0.30 | K | NIST |
| Tfus | 255.91 | K | Relay (1.0) Calculated Property |
| Vc | [0.575; 0.575] | m3/kmol |
|
| Vc | 0.575 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value |
| Vc | 0.575 | m3/kmol | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [208.59; 502.86] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -1.68400e+00 | |||
| Coefficient B | 8.98740e-01 | |||
| Coefficient C | -4.99400e-04 | |||
| Coefficient D | 1.05200e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 208.59 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 258.42 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 303.20 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 343.24 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 378.89 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 410.48 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 438.33 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 462.79 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 484.19 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 502.86 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0878509; 0.0002545] | Pa×s | [237.01; 451.55] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.47324e+01 | |||
| Coefficient B | 2.91529e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 237.01 | |||
| Temperature range, max. | 451.55 | |||
| η | 0.0878509 | Pa×s | 237.01 | Calculated Property |
| η | 0.0285472 | Pa×s | 260.85 | Calculated Property |
| η | 0.0111979 | Pa×s | 284.69 | Calculated Property |
| η | 0.0050759 | Pa×s | 308.52 | Calculated Property |
| η | 0.0025774 | Pa×s | 332.36 | Calculated Property |
| η | 0.0014330 | Pa×s | 356.20 | Calculated Property |
| η | 0.0008576 | Pa×s | 380.04 | Calculated Property |
| η | 0.0005453 | Pa×s | 403.88 | Calculated Property |
| η | 0.0003647 | Pa×s | 427.71 | Calculated Property |
| η | 0.0002545 | Pa×s | 451.55 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [358.61; 490.54] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.64041e+01 | |||
| Coefficient B | -4.69496e+03 | |||
| Coefficient C | -6.72920e+01 | |||
| Temperature range, min. | 358.61 | |||
| Temperature range, max. | 490.54 | |||
| Pvap | 1.33 | kPa | 358.61 | Calculated Property |
| Pvap | 2.89 | kPa | 373.27 | Calculated Property |
| Pvap | 5.82 | kPa | 387.93 | Calculated Property |
| Pvap | 11.04 | kPa | 402.59 | Calculated Property |
| Pvap | 19.85 | kPa | 417.25 | Calculated Property |
| Pvap | 34.04 | kPa | 431.90 | Calculated Property |
| Pvap | 55.99 | kPa | 446.56 | Calculated Property |
| Pvap | 88.75 | kPa | 461.22 | Calculated Property |
| Pvap | 136.11 | kPa | 475.88 | Calculated Property |
| Pvap | 202.64 | kPa | 490.54 | Calculated Property |
Similar Compounds
Find more compounds similar to 4-Nonanol.
Sources
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 ChEDL chemicals 1.5.2, from Gude, M.; Teja, A. S. Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols. J. Chem. Eng. Data 1995, 40, 1025-1036.
- Cheméo Relay (1.0)
- 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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