- InChI
- InChI=1S/C11H24/c1-4-7-8-9-10-11(5-2)6-3/h11H,4-10H2,1-3H3
- InChI Key
- FKJSIWPQZCKMIL-UHFFFAOYSA-N
- Formula
- C11H24
- SMILES
- CCCCCCC(CC)CC
- Molecular Weight1
- 156.31
- CAS
- 17302-11-3
- Other Names
-
- Nonane, 3-ethyl
- ω : Acentric Factor.
- 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).
- 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).
- 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 | 0.4814 | Relay (1.0) Calculated Property | |
| ΔfG° | 39.30 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -269.28 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 20.72 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 53.10 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.50 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.96 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.393 | Crippen Calculated Property | |
| McVol | 165.850 | ml/mol | McGowan Calculated Property |
| Pc | 1947.51 | kPa | Joback Calculated Property |
| Tboil | 458.95 | K | Relay (1.0) Calculated Property |
| Tc | 632.91 | K | Relay (1.0) Calculated Property |
| Tfus | 191.10 | K | Relay (1.0) Calculated Property |
| Vc | 0.622 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [238.52; 587.37] | 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 | -8.79300e+00 | |||
| Coefficient B | 1.05476e+00 | |||
| Coefficient C | -5.77800e-04 | |||
| Coefficient D | 1.19200e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 238.52 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 297.32 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 350.23 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 397.63 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 439.89 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 477.39 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 510.52 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 539.64 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 565.13 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 587.37 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0105797; 0.0002476] | Pa×s | [198.73; 431.23] |
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 | -1.15131e+01 | |||
| Coefficient B | 1.38402e+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. | 198.73 | |||
| Temperature range, max. | 431.23 | |||
| η | 0.0105797 | Pa×s | 198.73 | Calculated Property |
| η | 0.0047483 | Pa×s | 224.56 | Calculated Property |
| η | 0.0025141 | Pa×s | 250.40 | Calculated Property |
| η | 0.0014993 | Pa×s | 276.23 | Calculated Property |
| η | 0.0009768 | Pa×s | 302.06 | Calculated Property |
| η | 0.0006808 | Pa×s | 327.90 | Calculated Property |
| η | 0.0005002 | Pa×s | 353.73 | Calculated Property |
| η | 0.0003833 | Pa×s | 379.56 | Calculated Property |
| η | 0.0003038 | Pa×s | 405.40 | Calculated Property |
| η | 0.0002476 | Pa×s | 431.23 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [343.75; 490.63] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41465e+01 | |||
| Coefficient B | -3.57973e+03 | |||
| Coefficient C | -8.54500e+01 | |||
| Temperature range, min. | 343.75 | |||
| Temperature range, max. | 490.63 | |||
| Pvap | 1.33 | kPa | 343.75 | Calculated Property |
| Pvap | 3.04 | kPa | 360.07 | Calculated Property |
| Pvap | 6.31 | kPa | 376.39 | Calculated Property |
| Pvap | 12.13 | kPa | 392.71 | Calculated Property |
| Pvap | 21.84 | kPa | 409.03 | Calculated Property |
| Pvap | 37.14 | kPa | 425.35 | Calculated Property |
| Pvap | 60.18 | kPa | 441.67 | Calculated Property |
| Pvap | 93.46 | kPa | 457.99 | Calculated Property |
| Pvap | 139.88 | kPa | 474.31 | Calculated Property |
| Pvap | 202.67 | kPa | 490.63 | Calculated Property |
Similar Compounds
Find more compounds similar to 3-ethylnonane.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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