- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
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] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 1220 1240 1260 1280 1300 1320 1340 850 900 950 1000 | ||||
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.50e-3 3.00e-3 3.50e-3 4.00e-3 4.50e-3 5.00e-3 340 350 360 370 | ||||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 600 700 800 | ||||
| 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
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.