- InChI
- InChI=1S/C20H36O2/c1-3-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19-20(21)22-4-2/h8-9,11-12H,3-7,10,13-19H2,1-2H3/b9-8-,12-11-
- InChI Key
- FMMOOAYVCKXGMF-MURFETPASA-N
- Formula
- C20H36O2
- SMILES
- CCCCCC=CCC=CCCCCCCCC(=O)OCC
- Molecular Weight1
- 308.50
- CAS
- 544-35-4
- Other Names
-
- (Z,Z)-9,12-octadecadienoic acid, ethyl ester
- 9,12-Octadecadienoic acid (Z,Z)-, ethyl ester
- Ethyl cis,cis-9,12-octadecadienoate
- Ethyl linolate
- Mandenol
- ethyl (Z,Z)-9,12-octadecadienoate
- ethyl (Z,Z)-9,12-octadecadienoate
- ethyl linoleate
- linoleic acid, ethyl ester
- 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° | 44.04 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -466.49 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 50.75 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 69.19 | kJ/mol | Joback Calculated Property |
| log10WS | -6.76 | Crippen Calculated Property | |
| logPoct/wat | 6.363 | Crippen Calculated Property | |
| McVol | 291.500 | ml/mol | McGowan Calculated Property |
| Pc | 1120.05 | kPa | Joback Calculated Property |
| Inp | [2139.00; 2193.00] |
|
|
| Inp | 2139.00 | NIST | |
| Inp | 2155.00 | NIST | |
| Inp | 2159.00 | NIST | |
| Inp | 2177.00 | NIST | |
| Inp | 2159.00 | NIST | |
| Inp | 2162.00 | NIST | |
| Inp | 2145.00 | NIST | |
| Inp | 2151.00 | NIST | |
| Inp | 2141.00 | NIST | |
| Inp | 2141.00 | NIST | |
| Inp | 2139.00 | NIST | |
| Inp | 2162.90 | NIST | |
| Inp | Outlier 2193.00 | NIST | |
| Inp | 2140.00 | NIST | |
| Inp | 2155.00 | NIST | |
| Inp | 2159.00 | NIST | |
| Inp | 2152.00 | NIST | |
| Inp | 2165.00 | NIST | |
| Inp | 2164.00 | NIST | |
| Inp | 2144.00 | NIST | |
| Inp | 2177.00 | NIST | |
| Inp | 2156.00 | NIST | |
| Inp | 2155.00 | NIST | |
| Inp | 2151.00 | NIST | |
| Inp | 2169.00 | NIST | |
| Inp | 2162.00 | NIST | |
| Inp | 2166.00 | NIST | |
| Inp | 2171.00 | NIST | |
| Inp | 2140.00 | NIST | |
| Inp | 2162.00 | NIST | |
| Inp | 2162.00 | NIST | |
| Inp | 2162.00 | NIST | |
| I | [2486.00; 2553.00] |
|
|
| I | 2519.00 | NIST | |
| I | 2524.00 | NIST | |
| I | 2553.00 | NIST | |
| I | 2553.00 | NIST | |
| I | 2514.00 | NIST | |
| I | 2491.00 | NIST | |
| I | 2488.00 | NIST | |
| I | 2491.00 | NIST | |
| I | 2530.00 | NIST | |
| I | 2530.00 | NIST | |
| I | 2510.00 | NIST | |
| I | 2532.00 | NIST | |
| I | 2528.00 | NIST | |
| I | 2520.00 | NIST | |
| I | 2521.00 | NIST | |
| I | 2505.00 | NIST | |
| I | 2536.00 | NIST | |
| I | 2534.00 | NIST | |
| I | 2515.00 | NIST | |
| I | 2511.00 | NIST | |
| I | 2530.00 | NIST | |
| I | 2538.00 | NIST | |
| I | 2486.00 | NIST | |
| I | 2510.00 | NIST | |
| Tboil | 741.61 | K | Joback Calculated Property |
| Tc | 919.70 | K | Joback Calculated Property |
| Tfus | 377.16 | K | Joback Calculated Property |
| Vc | 1.139 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [862.13; 961.38] | J/mol×K | [741.61; 919.70] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 860 880 900 920 940 960 750 800 850 900 | ||||
| Cp,gas | 862.13 | J/mol×K | 741.61 | Joback Calculated Property |
| Cp,gas | 880.77 | J/mol×K | 771.29 | Joback Calculated Property |
| Cp,gas | 898.51 | J/mol×K | 800.97 | Joback Calculated Property |
| Cp,gas | 915.41 | J/mol×K | 830.65 | Joback Calculated Property |
| Cp,gas | 931.49 | J/mol×K | 860.34 | Joback Calculated Property |
| Cp,gas | 946.80 | J/mol×K | 890.02 | Joback Calculated Property |
| Cp,gas | 961.38 | J/mol×K | 919.70 | Joback Calculated Property |
| η | [0.0015685; 0.0081875] | Pa×s | [278.15; 363.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 7.00e-3 8.00e-3 300 350 | ||||
| η | 0.0081875 | Pa×s | 278.15 | Densiti... |
| η | 0.0070842 | Pa×s | 283.15 | Densiti... |
| η | 0.0061652 | Pa×s | 288.15 | Densiti... |
| η | 0.0054231 | Pa×s | 293.15 | Densiti... |
| η | 0.0048073 | Pa×s | 298.15 | Densiti... |
| η | 0.0043074 | Pa×s | 303.15 | Densiti... |
| η | 0.0038539 | Pa×s | 308.15 | Densiti... |
| η | 0.0034060 | Pa×s | 313.15 | Densiti... |
| η | 0.0031608 | Pa×s | 318.15 | Densiti... |
| η | 0.0028291 | Pa×s | 323.15 | Densiti... |
| η | 0.0026411 | Pa×s | 328.15 | Densiti... |
| η | 0.0024287 | Pa×s | 333.15 | Densiti... |
| η | 0.0022414 | Pa×s | 338.15 | Densiti... |
| η | 0.0020753 | Pa×s | 343.15 | Densiti... |
| η | 0.0019270 | Pa×s | 348.15 | Densiti... |
| η | 0.0017727 | Pa×s | 353.15 | Densiti... |
| η | 0.0016757 | Pa×s | 358.15 | Densiti... |
| η | 0.0015685 | Pa×s | 363.15 | Densiti... |
| ΔvapH | 72.60 | kJ/mol | 472.50 | NIST |
| Pvap | [1.33; 9.33] | kPa | [486.64; 537.69] |
|
|
T(K) Vapor pressure (kPa) 2 4 6 8 10 500 520 | ||||
| Pvap | 1.33 | kPa | 486.64 | Determi... |
| Pvap | 2.67 | kPa | 501.94 | Determi... |
| Pvap | 4.00 | kPa | 510.65 | Determi... |
| Pvap | 5.33 | kPa | 515.70 | Determi... |
| Pvap | 6.67 | kPa | 520.91 | Determi... |
| Pvap | 8.00 | kPa | 527.47 | Determi... |
| Pvap | 9.33 | kPa | 537.39 | Determi... |
| Pvap | 9.33 | kPa | 537.69 | Vapor l... |
Similar Compounds
Find more compounds similar to Linoleic acid ethyl ester.
Mixtures
Sources
- Crippen Method
- Crippen Method
- Determination of the vapor pressure of ethyl esters by Differential Scanning Calorimetry
- Vapor liquid equilibrium of fatty acid ethyl esters determined using DSC
- Densities and Viscosities of Minority Fatty Acid Methyl and Ethyl Esters Present in Biodiesel
- Joback Method
- McGowan Method
- NIST Webbook
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