- InChI
- InChI=1S/C16H34/c1-4-5-6-7-8-9-10-11-12-13-14-15-16(2)3/h16H,4-15H2,1-3H3
- InChI Key
- BANXPJUEBPWEOT-UHFFFAOYSA-N
- Formula
- C16H34
- SMILES
- CCCCCCCCCCCCCC(C)C
- Molecular Weight1
- 226.44
- CAS
- 1560-93-6
- Other Names
-
- 2-Methylpentadecane
- 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).
- ρl : Liquid Density (kg/m3).
- Inp : Non-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° | 81.40 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -378.85 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 33.67 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 50.82 | kJ/mol | Joback Calculated Property |
| log10WS | -6.28 | Crippen Calculated Property | |
| logPoct/wat | 6.344 | Crippen Calculated Property | |
| McVol | 236.300 | ml/mol | McGowan Calculated Property |
| Pc | 1326.17 | kPa | Joback Calculated Property |
| Inp | [1533.00; 1569.00] |
|
|
| Inp | 1564.00 | NIST | |
| Inp | 1564.80 | NIST | |
| Inp | 1564.89 | NIST | |
| Inp | 1564.84 | NIST | |
| Inp | 1563.71 | NIST | |
| Inp | 1564.10 | NIST | |
| Inp | 1564.13 | NIST | |
| Inp | 1564.00 | NIST | |
| Inp | 1569.00 | NIST | |
| Inp | 1559.00 | NIST | |
| Inp | 1561.00 | NIST | |
| Inp | 1565.20 | NIST | |
| Inp | Outlier 1533.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1564.00 | NIST | |
| Inp | Outlier 1543.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1562.00 | NIST | |
| Inp | 1562.00 | NIST | |
| Inp | 1569.00 | NIST | |
| Inp | 1566.00 | NIST | |
| Inp | 1564.00 | NIST | |
| Inp | 1564.10 | NIST | |
| Tboil | 565.04 | K | Joback Calculated Property |
| Tc | 726.28 | K | Joback Calculated Property |
| Tfus | 262.40 ± 2.00 | K | NIST |
| Vc | 0.925 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [611.96; 717.90] | J/mol×K | [565.04; 726.28] |
|
| Cp,gas | 611.96 | J/mol×K | 565.04 | Joback Calculated Property |
| Cp,gas | 631.47 | J/mol×K | 591.91 | Joback Calculated Property |
| Cp,gas | 650.21 | J/mol×K | 618.79 | Joback Calculated Property |
| Cp,gas | 668.20 | J/mol×K | 645.66 | Joback Calculated Property |
| Cp,gas | 685.47 | J/mol×K | 672.53 | Joback Calculated Property |
| Cp,gas | 702.03 | J/mol×K | 699.40 | Joback Calculated Property |
| Cp,gas | 717.90 | J/mol×K | 726.28 | Joback Calculated Property |
| η | [0.0001427; 0.0077044] | Pa×s | [255.08; 565.04] |
|
| η | 0.0077044 | Pa×s | 255.08 | Joback Calculated Property |
| η | 0.0022640 | Pa×s | 306.74 | Joback Calculated Property |
| η | 0.0009470 | Pa×s | 358.40 | Joback Calculated Property |
| η | 0.0004934 | Pa×s | 410.06 | Joback Calculated Property |
| η | 0.0002974 | Pa×s | 461.72 | Joback Calculated Property |
| η | 0.0001985 | Pa×s | 513.38 | Joback Calculated Property |
| η | 0.0001427 | Pa×s | 565.04 | Joback Calculated Property |
| ΔvapH | 62.00 | kJ/mol | 485.50 | NIST |
| ρl | [718.90; 782.20] | kg/m3 | [283.15; 373.15] |
|
| ρl | 781.80 | kg/m3 | 283.15 | Density... |
| ρl | 782.20 | kg/m3 | 283.15 | Density... |
| ρl | 774.90 | kg/m3 | 293.15 | Density... |
| ρl | 775.00 | kg/m3 | 293.15 | Density... |
| ρl | 767.90 | kg/m3 | 303.15 | Density... |
| ρl | 768.00 | kg/m3 | 303.15 | Density... |
| ρl | 761.00 | kg/m3 | 313.15 | Density... |
| ρl | 761.00 | kg/m3 | 313.15 | Density... |
| ρl | 754.00 | kg/m3 | 323.15 | Density... |
| ρl | 754.10 | kg/m3 | 323.15 | Density... |
| ρl | 747.00 | kg/m3 | 333.15 | Density... |
| ρl | 740.00 | kg/m3 | 343.15 | Density... |
| ρl | 733.00 | kg/m3 | 353.15 | Density... |
| ρl | 726.00 | kg/m3 | 363.15 | Density... |
| ρl | 718.90 | kg/m3 | 373.15 | Density... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [419.73; 588.47] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42741e+01 | |||
| Coefficient B | -4.21040e+03 | |||
| Coefficient C | -1.18700e+02 | |||
| Temperature range, min. | 419.73 | |||
| Temperature range, max. | 588.47 | |||
| Pvap | 1.33 | kPa | 419.73 | Calculated Property |
| Pvap | 3.03 | kPa | 438.48 | Calculated Property |
| Pvap | 6.28 | kPa | 457.23 | Calculated Property |
| Pvap | 12.05 | kPa | 475.98 | Calculated Property |
| Pvap | 21.69 | kPa | 494.73 | Calculated Property |
| Pvap | 36.92 | kPa | 513.47 | Calculated Property |
| Pvap | 59.88 | kPa | 532.22 | Calculated Property |
| Pvap | 93.12 | kPa | 550.97 | Calculated Property |
| Pvap | 139.61 | kPa | 569.72 | Calculated Property |
| Pvap | 202.64 | kPa | 588.47 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentadecane, 2-methyl-.
Sources
- Crippen Method
- Crippen Method
- Density, Viscosity, Speed of Sound, and Bulk Modulus of Methyl Alkanes, Dimethyl Alkanes, and Hydrotreated Renewable Fuels
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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that the value is more than 2 standard deviations away from the
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