- InChI
- InChI=1S/C25H50O2/c1-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19-20-21-22-23-24-25(26)27-2/h3-24H2,1-2H3
- InChI Key
- XUDJZDNUVZHSKZ-UHFFFAOYSA-N
- Formula
- C25H50O2
- SMILES
- CCCCCCCCCCCCCCCCCCCCCCCC(=O)OC
- Molecular Weight1
- 382.66
- CAS
- 2442-49-1
- Other Names
-
- 24:0, Me ester
- Lignoceric acid methyl ester
- Methyl lignocerate
- Methyl tetracosanoate
- 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).
- ΔfusH : Enthalpy of fusion at a given temperature (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).
- Tboilr : Boiling point at reduced pressure (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° | -74.30 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -804.13 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 63.29 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 80.40 | kJ/mol | Joback Calculated Property |
| log10WS | -9.15 | Crippen Calculated Property | |
| logPoct/wat | 8.762 | Crippen Calculated Property | |
| McVol | 370.550 | ml/mol | McGowan Calculated Property |
| Pc | 783.75 | kPa | Joback Calculated Property |
| Inp | [450.20; 2740.00] |
|
|
| Inp | 2715.00 | NIST | |
| Inp | 2715.00 | NIST | |
| Inp | 2731.30 | NIST | |
| Inp | 2732.00 | NIST | |
| Inp | 2712.00 | NIST | |
| Inp | 2713.00 | NIST | |
| Inp | 2710.00 | NIST | |
| Inp | 2715.00 | NIST | |
| Inp | 2729.90 | NIST | |
| Inp | 2714.00 | NIST | |
| Inp | 2731.00 | NIST | |
| Inp | 2740.00 | NIST | |
| Inp | 2712.67 | NIST | |
| Inp | 2737.00 | NIST | |
| Inp | 2725.00 | NIST | |
| Inp | 2716.00 | NIST | |
| Inp | 2687.00 | NIST | |
| Inp | 2714.00 | NIST | |
| Inp | 2714.00 | NIST | |
| Inp | 2725.00 | NIST | |
| Inp | 2692.00 | NIST | |
| Inp | Outlier 450.20 | NIST | |
| Inp | Outlier 450.30 | NIST | |
| Inp | Outlier 450.20 | NIST | |
| I | [3024.00; 3053.00] |
|
|
| I | 3024.00 | NIST | |
| I | 3053.00 | NIST | |
| Tboil | 847.69 | K | Joback Calculated Property |
| Tc | 1038.15 | K | Joback Calculated Property |
| Tfus | 443.67 | K | Joback Calculated Property |
| Vc | 1.460 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [1220.77; 1336.53] | J/mol×K | [847.69; 1038.15] |
|
| Cp,gas | 1220.77 | J/mol×K | 847.69 | Joback Calculated Property |
| Cp,gas | 1243.05 | J/mol×K | 879.43 | Joback Calculated Property |
| Cp,gas | 1264.07 | J/mol×K | 911.18 | Joback Calculated Property |
| Cp,gas | 1283.89 | J/mol×K | 942.92 | Joback Calculated Property |
| Cp,gas | 1302.54 | J/mol×K | 974.66 | Joback Calculated Property |
| Cp,gas | 1320.07 | J/mol×K | 1006.41 | Joback Calculated Property |
| Cp,gas | 1336.53 | J/mol×K | 1038.15 | Joback Calculated Property |
| η | [0.0027066; 0.0051392] | Pa×s | [338.15; 373.15] |
|
| η | 0.0051392 | Pa×s | 338.15 | Densiti... |
| η | 0.0046279 | Pa×s | 343.15 | Densiti... |
| η | 0.0041894 | Pa×s | 348.15 | Densiti... |
| η | 0.0038102 | Pa×s | 353.15 | Densiti... |
| η | 0.0034797 | Pa×s | 358.15 | Densiti... |
| η | 0.0031895 | Pa×s | 363.15 | Densiti... |
| η | 0.0029327 | Pa×s | 368.15 | Densiti... |
| η | 0.0027066 | Pa×s | 373.15 | Densiti... |
| ΔfusH | 90.00 | kJ/mol | 331.20 | NIST |
| ΔvapH | [100.80; 146.20] | kJ/mol | [298.15; 512.50] |
|
| ΔvapH | 135.70 | kJ/mol | 298.15 | the vap... |
| ΔvapH | 146.20 | kJ/mol | 437.00 | NIST |
| ΔvapH | 100.80 | kJ/mol | 509.50 | NIST |
| ΔvapH | 136.60 ± 2.50 | kJ/mol | 512.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 505.20 | K | 0.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [605.20; 826.84] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54233e+01 | |||
| Coefficient B | -6.75201e+03 | |||
| Coefficient C | -1.59102e+02 | |||
| Temperature range, min. | 605.20 | |||
| Temperature range, max. | 826.84 | |||
| Pvap | 1.33 | kPa | 605.20 | Calculated Property |
| Pvap | 2.94 | kPa | 629.83 | Calculated Property |
| Pvap | 6.00 | kPa | 654.45 | Calculated Property |
| Pvap | 11.45 | kPa | 679.08 | Calculated Property |
| Pvap | 20.60 | kPa | 703.71 | Calculated Property |
| Pvap | 35.22 | kPa | 728.33 | Calculated Property |
| Pvap | 57.60 | kPa | 752.96 | Calculated Property |
| Pvap | 90.59 | kPa | 777.59 | Calculated Property |
| Pvap | 137.60 | kPa | 802.21 | Calculated Property |
| Pvap | 202.66 | kPa | 826.84 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetracosanoic acid, methyl ester.
Sources
- Crippen Method
- Crippen Method
- the vaporization enthaplies and vapor pressures of a series of unstaurated fatty acid methyl esters by correlation gas chromatography
- Densities and Viscosities of Minority Fatty Acid Methyl and Ethyl Esters Present in Biodiesel
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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