- InChI
- InChI=1S/C11H24/c1-4-6-7-8-9-10-11(3)5-2/h11H,4-10H2,1-3H3
- InChI Key
- JJRUZTXRDDMYGM-UHFFFAOYSA-N
- Formula
- C11H24
- SMILES
- CCCCCCCC(C)CC
- Molecular Weight1
- 156.31
- CAS
- 13151-34-3
- Other Names
-
- 2-Ethylnonane
- 3-Methyldecane
- 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).
- 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).
- 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° | 39.30 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -275.65 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 20.72 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 39.69 | kJ/mol | Joback Calculated Property |
| log10WS | -4.19 | Crippen Calculated Property | |
| logPoct/wat | 4.393 | Crippen Calculated Property | |
| McVol | 165.850 | ml/mol | McGowan Calculated Property |
| Pc | 1947.51 | kPa | Joback Calculated Property |
| Inp | [1063.90; 1074.00] |
|
|
| Inp | 1073.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1072.40 | NIST | |
| Inp | Outlier 1063.90 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1071.41 | NIST | |
| Inp | 1071.58 | NIST | |
| Inp | 1071.88 | NIST | |
| Inp | 1070.96 | NIST | |
| Inp | 1071.31 | NIST | |
| Inp | 1071.49 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1072.10 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1071.20 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1073.00 | NIST | |
| I | [1048.00; 1070.00] |
|
|
| I | 1048.00 | NIST | |
| I | 1070.00 | NIST | |
| Tboil | 450.64 | K | Joback Calculated Property |
| Tc | 615.77 | K | Joback Calculated Property |
| Tfus | 198.73 | K | Joback Calculated Property |
| Vc | 0.645 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [360.10; 449.44] | J/mol×K | [450.64; 615.77] |
|
| Cp,gas | 360.10 | J/mol×K | 450.64 | Joback Calculated Property |
| Cp,gas | 376.48 | J/mol×K | 478.16 | Joback Calculated Property |
| Cp,gas | 392.24 | J/mol×K | 505.68 | Joback Calculated Property |
| Cp,gas | 407.41 | J/mol×K | 533.20 | Joback Calculated Property |
| Cp,gas | 421.98 | J/mol×K | 560.73 | Joback Calculated Property |
| Cp,gas | 435.99 | J/mol×K | 588.25 | Joback Calculated Property |
| Cp,gas | 449.44 | J/mol×K | 615.77 | Joback Calculated Property |
| η | [0.0002156; 0.0105797] | Pa×s | [198.73; 450.64] |
|
| η | 0.0105797 | Pa×s | 198.73 | Joback Calculated Property |
| η | 0.0031400 | Pa×s | 240.72 | Joback Calculated Property |
| η | 0.0013369 | Pa×s | 282.70 | Joback Calculated Property |
| η | 0.0007098 | Pa×s | 324.69 | Joback Calculated Property |
| η | 0.0004357 | Pa×s | 366.67 | Joback Calculated Property |
| η | 0.0002956 | Pa×s | 408.65 | Joback Calculated Property |
| η | 0.0002156 | Pa×s | 450.64 | Joback Calculated Property |
| ΔvapH | 46.50 | kJ/mol | 402.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [337.36; 493.69] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.50345e+01 | |||
| Coefficient B | -4.46160e+03 | |||
| Coefficient C | -3.48170e+01 | |||
| Temperature range, min. | 337.36 | |||
| Temperature range, max. | 493.69 | |||
| Pvap | 1.33 | kPa | 337.36 | Calculated Property |
| Pvap | 2.97 | kPa | 354.73 | Calculated Property |
| Pvap | 6.09 | kPa | 372.10 | Calculated Property |
| Pvap | 11.64 | kPa | 389.47 | Calculated Property |
| Pvap | 20.94 | kPa | 406.84 | Calculated Property |
| Pvap | 35.76 | kPa | 424.21 | Calculated Property |
| Pvap | 58.32 | kPa | 441.58 | Calculated Property |
| Pvap | 91.39 | kPa | 458.95 | Calculated Property |
| Pvap | 138.25 | kPa | 476.32 | Calculated Property |
| Pvap | 202.67 | kPa | 493.69 | Calculated Property |
Similar Compounds
Find more compounds similar to Decane, 3-methyl-.
Sources
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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