- InChI
- InChI=1S/C21H42O2/c1-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19-20-21(22)23-2/h3-20H2,1-2H3
- InChI Key
- QGBRLVONZXHAKJ-UHFFFAOYSA-N
- Formula
- C21H42O2
- SMILES
- CCCCCCCCCCCCCCCCCCCC(=O)OC
- Molecular Weight1
- 326.56
- CAS
- 1120-28-1
- Other Names
-
- Arachidic acid methyl ester
- Kemester 2050
- Methyl arachidate
- Methyl arachisate
- Methyl aracidate
- Methyl eicosanoate
- Methyl eicosenate
- methyl icosanoate
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- 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).
- ΔsubH : Enthalpy of sublimation 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 |
|---|---|---|---|
| ΔcH°solid | -13263.00 ± 0.40 | kJ/mol | NIST |
| ΔfG° | -107.98 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -721.57 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 78.79 | kJ/mol | Heat Ca... |
| ΔvapH° | [116.20; 120.90] | kJ/mol |
|
| ΔvapH° | 120.90 ± 2.50 | kJ/mol | NIST |
| ΔvapH° | 116.40 ± 1.50 | kJ/mol | NIST |
| ΔvapH° | 116.20 | kJ/mol | NIST |
| log10WS | -7.48 | Crippen Calculated Property | |
| logPoct/wat | 7.201 | Crippen Calculated Property | |
| McVol | 314.190 | ml/mol | McGowan Calculated Property |
| Pc | 983.93 | kPa | Joback Calculated Property |
| Inp | [376.90; 2339.00] |
|
|
| Inp | 2295.60 | NIST | |
| Inp | 2296.70 | NIST | |
| Inp | 2297.80 | NIST | |
| Inp | 2299.00 | NIST | |
| Inp | 2300.20 | NIST | |
| Inp | 2301.40 | NIST | |
| Inp | 2302.70 | NIST | |
| Inp | 2312.00 | NIST | |
| Inp | 2314.00 | NIST | |
| Inp | 2314.00 | NIST | |
| Inp | 2318.00 | NIST | |
| Inp | 2339.00 | NIST | |
| Inp | 2310.00 | NIST | |
| Inp | 2310.00 | NIST | |
| Inp | 2311.59 | NIST | |
| Inp | 2302.00 | NIST | |
| Inp | 2329.00 | NIST | |
| Inp | 2332.00 | NIST | |
| Inp | 2311.00 | NIST | |
| Inp | 2311.00 | NIST | |
| Inp | 2317.00 | NIST | |
| Inp | 2311.00 | NIST | |
| Inp | 2335.00 | NIST | |
| Inp | 2305.00 | NIST | |
| Inp | 2333.00 | NIST | |
| Inp | 2309.00 | NIST | |
| Inp | 2313.00 | NIST | |
| Inp | 2307.00 | NIST | |
| Inp | 2307.00 | NIST | |
| Inp | 2312.00 | NIST | |
| Inp | 2324.00 | NIST | |
| Inp | 2329.00 | NIST | |
| Inp | 376.90 | NIST | |
| Inp | 380.64 | NIST | |
| Inp | 390.60 | NIST | |
| Inp | 390.60 | NIST | |
| Inp | 379.61 | NIST | |
| Inp | 378.87 | NIST | |
| Inp | 378.87 | NIST | |
| Inp | 378.87 | NIST | |
| Inp | 2332.00 | NIST | |
| Inp | 376.90 | NIST | |
| Inp | 378.87 | NIST | |
| I | [2617.00; 2646.00] |
|
|
| I | 2617.00 | NIST | |
| I | 2646.00 | NIST | |
| I | 2638.00 | NIST | |
| I | 2640.00 | NIST | |
| I | 2638.00 | NIST | |
| I | 2617.00 | NIST | |
| Tboil | 756.17 | K | Joback Calculated Property |
| Tc | 929.77 | K | Joback Calculated Property |
| Tfus | 398.59 | K | Joback Calculated Property |
| Vc | 1.236 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [969.32; 1075.99] | J/mol×K | [756.17; 929.77] |
|
| Cp,gas | 969.32 | J/mol×K | 756.17 | Joback Calculated Property |
| Cp,gas | 989.43 | J/mol×K | 785.10 | Joback Calculated Property |
| Cp,gas | 1008.57 | J/mol×K | 814.04 | Joback Calculated Property |
| Cp,gas | 1026.77 | J/mol×K | 842.97 | Joback Calculated Property |
| Cp,gas | 1044.06 | J/mol×K | 871.90 | Joback Calculated Property |
| Cp,gas | 1060.46 | J/mol×K | 900.83 | Joback Calculated Property |
| Cp,gas | 1075.99 | J/mol×K | 929.77 | Joback Calculated Property |
| η | [0.0019591; 0.0048319] | Pa×s | [323.15; 373.15] |
|
| η | 0.0048319 | Pa×s | 323.15 | Densiti... |
| η | 0.0043226 | Pa×s | 328.15 | Densiti... |
| η | 0.0038888 | Pa×s | 333.15 | Densiti... |
| η | 0.0035170 | Pa×s | 338.15 | Densiti... |
| η | 0.0031964 | Pa×s | 343.15 | Densiti... |
| η | 0.0029177 | Pa×s | 348.15 | Densiti... |
| η | 0.0026745 | Pa×s | 353.15 | Densiti... |
| η | 0.0024612 | Pa×s | 358.15 | Densiti... |
| η | 0.0022726 | Pa×s | 363.15 | Densiti... |
| η | 0.0021066 | Pa×s | 368.15 | Densiti... |
| η | 0.0019591 | Pa×s | 373.15 | Densiti... |
| ΔfusH | [73.70; 74.30] | kJ/mol | [319.20; 319.20] |
|
| ΔfusH | 74.30 | kJ/mol | 319.20 | NIST |
| ΔfusH | 73.70 | kJ/mol | 319.20 | NIST |
| ΔfusH | 73.70 | kJ/mol | 319.20 | NIST |
| ΔsubH | 191.00 ± 10.00 | kJ/mol | 314.50 | NIST |
| ΔvapH | [76.90; 116.00] | kJ/mol | [298.00; 498.00] |
|
| ΔvapH | 111.10 | kJ/mol | 298.00 | A Compa... |
| ΔvapH | 116.00 | kJ/mol | 298.15 | the vap... |
| ΔvapH | 109.20 | kJ/mol | 350.00 | NIST |
| ΔvapH | 97.80 ± 0.20 | kJ/mol | 406.00 | NIST |
| ΔvapH | 92.40 | kJ/mol | 495.00 | NIST |
| ΔvapH | 76.90 | kJ/mol | 498.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [461.20; 488.70] | K | [0.30; 1.30] |
|
| Tboilr | 461.20 | K | 0.30 | NIST |
| Tboilr | 488.70 | K | 1.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [533.80; 659.59] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 2.12669e+01 | |||
| Coefficient B | -8.38143e+03 | |||
| Coefficient C | -1.34290e+02 | |||
| Temperature range, min. | 533.80 | |||
| Temperature range, max. | 659.59 | |||
| Pvap | 1.33 | kPa | 533.80 | Calculated Property |
| Pvap | 2.71 | kPa | 547.78 | Calculated Property |
| Pvap | 5.26 | kPa | 561.75 | Calculated Property |
| Pvap | 9.78 | kPa | 575.73 | Calculated Property |
| Pvap | 17.51 | kPa | 589.71 | Calculated Property |
| Pvap | 30.30 | kPa | 603.68 | Calculated Property |
| Pvap | 50.77 | kPa | 617.66 | Calculated Property |
| Pvap | 82.65 | kPa | 631.64 | Calculated Property |
| Pvap | 131.01 | kPa | 645.61 | Calculated Property |
| Pvap | 202.63 | kPa | 659.59 | Calculated Property |
Similar Compounds
Find more compounds similar to Eicosanoic 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
- A Comparison of Results by Correlation Gas Chromatography with Another Gas Chromatographic Retention Time Technique. The Effects of Retention Time Coincidence on Vaporization Enthalpy and Vapor Pressure
- Heat Capacity Measurements of 13 Methyl Esters of n-Carboxylic Acids from Methyloctanoate to Methyleicosanoate between 5 K and 350 K
- 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.