- InChI
- InChI=1S/C15H32/c1-4-5-6-7-8-9-10-11-12-13-14-15(2)3/h15H,4-14H2,1-3H3
- InChI Key
- KUVMKLCGXIYSNH-UHFFFAOYSA-N
- Formula
- C15H32
- SMILES
- CCCCCCCCCCCCC(C)C
- Molecular Weight1
- 212.41
- CAS
- 1560-95-8
- Other Names
-
- 2-Methyltetradecane
- 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° | 72.98 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -358.21 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 31.08 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 48.60 | kJ/mol | Joback Calculated Property |
| log10WS | -5.86 | Crippen Calculated Property | |
| logPoct/wat | 5.953 | Crippen Calculated Property | |
| McVol | 222.210 | ml/mol | McGowan Calculated Property |
| Pc | 1423.99 | kPa | Joback Calculated Property |
| Inp | [1454.00; 1480.00] |
|
|
| Inp | 1462.00 | NIST | |
| Inp | 1461.00 | NIST | |
| Inp | Outlier 1480.00 | NIST | |
| Inp | 1465.00 | NIST | |
| Inp | 1464.89 | NIST | |
| Inp | 1464.87 | NIST | |
| Inp | 1464.95 | NIST | |
| Inp | 1463.92 | NIST | |
| Inp | 1464.09 | NIST | |
| Inp | 1464.24 | NIST | |
| Inp | 1467.00 | NIST | |
| Inp | 1461.00 | NIST | |
| Inp | 1460.00 | NIST | |
| Inp | 1463.00 | NIST | |
| Inp | 1465.40 | NIST | |
| Inp | 1462.00 | NIST | |
| Inp | 1454.00 | NIST | |
| Inp | 1457.00 | NIST | |
| Inp | 1465.00 | NIST | |
| Inp | 1461.00 | NIST | |
| Inp | 1461.00 | NIST | |
| Inp | 1462.00 | NIST | |
| Inp | 1461.00 | NIST | |
| Inp | 1454.00 | NIST | |
| I | 1483.00 | NIST | |
| Tboil | 542.16 | K | Joback Calculated Property |
| Tc | 703.93 | K | Joback Calculated Property |
| Tfus | [264.30; 264.90] | K |
|
| Tfus | 264.30 ± 0.70 | K | NIST |
| Tfus | 264.90 ± 0.50 | K | NIST |
| Vc | 0.870 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [558.22; 661.59] | J/mol×K | [542.16; 703.93] |
|
| Cp,gas | 558.22 | J/mol×K | 542.16 | Joback Calculated Property |
| Cp,gas | 577.24 | J/mol×K | 569.12 | Joback Calculated Property |
| Cp,gas | 595.52 | J/mol×K | 596.08 | Joback Calculated Property |
| Cp,gas | 613.07 | J/mol×K | 623.04 | Joback Calculated Property |
| Cp,gas | 629.92 | J/mol×K | 650.00 | Joback Calculated Property |
| Cp,gas | 646.08 | J/mol×K | 676.97 | Joback Calculated Property |
| Cp,gas | 661.59 | J/mol×K | 703.93 | Joback Calculated Property |
| η | [0.0001577; 0.0083877] | Pa×s | [243.81; 542.16] |
|
| η | 0.0083877 | Pa×s | 243.81 | Joback Calculated Property |
| η | 0.0024681 | Pa×s | 293.53 | Joback Calculated Property |
| η | 0.0010352 | Pa×s | 343.26 | Joback Calculated Property |
| η | 0.0005409 | Pa×s | 392.99 | Joback Calculated Property |
| η | 0.0003270 | Pa×s | 442.71 | Joback Calculated Property |
| η | 0.0002189 | Pa×s | 492.43 | Joback Calculated Property |
| η | 0.0001577 | Pa×s | 542.16 | Joback Calculated Property |
| ΔvapH | 58.80 | kJ/mol | 469.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [406.32; 571.32] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42799e+01 | |||
| Coefficient B | -4.12141e+03 | |||
| Coefficient C | -1.11770e+02 | |||
| Temperature range, min. | 406.32 | |||
| Temperature range, max. | 571.32 | |||
| Pvap | 1.33 | kPa | 406.32 | Calculated Property |
| Pvap | 3.03 | kPa | 424.65 | Calculated Property |
| Pvap | 6.28 | kPa | 442.99 | Calculated Property |
| Pvap | 12.05 | kPa | 461.32 | Calculated Property |
| Pvap | 21.69 | kPa | 479.65 | Calculated Property |
| Pvap | 36.91 | kPa | 497.99 | Calculated Property |
| Pvap | 59.87 | kPa | 516.32 | Calculated Property |
| Pvap | 93.12 | kPa | 534.65 | Calculated Property |
| Pvap | 139.61 | kPa | 552.99 | Calculated Property |
| Pvap | 202.65 | kPa | 571.32 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetradecane, 2-methyl-.
Sources
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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