- InChI
- InChI=1S/C57H104O6/c1-4-7-10-13-16-19-22-25-28-31-34-37-40-43-46-49-55(58)61-52-54(63-57(60)51-48-45-42-39-36-33-30-27-24-21-18-15-12-9-6-3)53-62-56(59)50-47-44-41-38-35-32-29-26-23-20-17-14-11-8-5-2/h25-30,54H,4-24,31-53H2,1-3H3/b28-25-,29-26-,30-27-
- InChI Key
- PHYFQTYBJUILEZ-IUPFWZBJSA-N
- Formula
- C57H104O6
- SMILES
-
CCCCCCCC/C=C\CCCCCCCC(=O)OCC(C
OC(=O)CCCCCCC/C=C\CCCCCCCC)OC( =O)CCCCCCC/C=C\CCCCCCCC - Molecular Weight1
- 885.45
- Other Names
-
- 1,2,3-propanetriyl trioleate
- 1,2,3-tri(cis-9-octadecenoyl)glycerol
- 2,3-Bis[(9Z)-9-octadecenoyloxy]propyl (9Z)-9-octadecenoate
- 9-Octadecenoic acid (9Z)-, 1,1',1''-(1,2,3-propanetriyl) ester
- 9-Octadecenoic acid (9Z)-, 1,2,3-propanetriyl ester
- 9-Octadecenoic acid 1,2,3-propanetriyl ester, (Z)-
- 9-octadecenoic acid (Z)-, 1,2,3-propanetriyl ester
- Aldo TO
- Emerest 2423
- Emery 2423
- Emery oleic acid ester 2230
- Glycerin trioleate
- Glycerol triolein
- Kemester 1000
- Oleic triglyceride
- Olein, tri-
- Priolube 1435
- Radia 7363
- Raoline
- Trioleoylglyceride
- glycerol trioleate
- glyceryl trioleate
- glyceryl tris[(Z)-9-octadecenoate]
- glyceryl-1,2,3-trioleate
- oleic acid triglyceride
- oleyl triglyceride
- trioleoylglycerol
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- 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).
- 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -35099.60 ± 1.30 | kJ/mol | NIST |
| ΔfH°gas | -1938.19 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 153.58 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 250.01 | kJ/mol | Relay (1.0) Calculated Property |
| log10WS | -13.91 | Relay (1.0) Calculated Property | |
| logPoct/wat | 18.097 | Crippen Calculated Property | |
| McVol | 823.410 | ml/mol | McGowan Calculated Property |
| Pc | 235.89 | kPa | Joback Calculated Property |
| Tboil | 857.33 | K | Relay (1.0) Calculated Property |
| Tc | 1013.25 | K | Relay (1.0) Calculated Property |
| Tfus | [268.20; 279.22] | K |
|
| Tfus | 268.20 | K | Solid-Liquid Equilibria in Fatty Acid/Triglycerol Systems |
| Tfus | 279.22 | K | Solid Liquid Equilibrium of Binary Mixtures Containing Fatty Acids and Triacylglycerols |
Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation, Acentric Factor, Ionization energy for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [3346.97; 13529.68] | J/mol×K | [1690.46; 4019.77] |
|
| Cp,gas | 3346.97 | J/mol×K | 1690.46 | Joback Calculated Property |
| Cp,gas | 3599.02 | J/mol×K | 2078.68 | Joback Calculated Property |
| Cp,gas | 4130.69 | J/mol×K | 2466.90 | Joback Calculated Property |
| Cp,gas | 5165.79 | J/mol×K | 2855.12 | Joback Calculated Property |
| Cp,gas | 6928.13 | J/mol×K | 3243.34 | Joback Calculated Property |
| Cp,gas | 9641.49 | J/mol×K | 3631.56 | Joback Calculated Property |
| Cp,gas | 13529.68 | J/mol×K | 4019.77 | Joback Calculated Property |
| η | [2.6096024e-08; 0.0000017] | Pa×s | [828.90; 1690.46] |
|
| η | 0.0000017 | Pa×s | 828.90 | Joback Calculated Property |
| η | 0.0000005 | Pa×s | 972.49 | Joback Calculated Property |
| η | 0.0000002 | Pa×s | 1116.09 | Joback Calculated Property |
| η | 0.0000001 | Pa×s | 1259.68 | Joback Calculated Property |
| η | 5.9538754e-08 | Pa×s | 1403.27 | Joback Calculated Property |
| η | 3.7936764e-08 | Pa×s | 1546.87 | Joback Calculated Property |
| η | 2.6096024e-08 | Pa×s | 1690.46 | Joback Calculated Property |
Similar Compounds
Find more compounds similar to Triolein.
Mixtures
- Triolein + Methyl Alcohol
- Triolein + Glycerin
- Triolein + Water
- Triolein + Tetradecanoic acid + 1-Hexanol
- Triolein + 1-Butanol + Tetradecanoic acid
- 1-Propanol + Triolein + Tetradecanoic acid
- Triolein + 2-Propanol + Tetradecanoic acid
- Oleic Acid + Triolein + Ethanol
- Triolein + Carbon dioxide + «beta» Carotene
- Hydrogen + Triolein
- Triolein + Dimethyl ether + Methyl Alcohol
- Triolein + n-Hexadecanoic acid
- Triolein + Tripalmitin
- Triolein + Carbon dioxide
- Triolein + Sulfur hexafluoride
- Oleic Acid + Triolein
- Triolein + 9,12-Octadecadienoic acid (Z,Z)-
Sources
- Cheméo Relay (1.0)
- Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
- Crippen Method
- Crippen Method
- Phase equilibria of methanol triolein system at elevated temperature and pressure
- Hydrogen solubility in triolein, and propane solubility in oleic acid for second generation BDF synthesis by use of hydrodeoxygenation reaction
- Phase equilibria of triolein to biodiesel reactor systems
- Solubility of b-carotene in ethanol- and triolein-modified CO2
- Effect of triolein addition of the solubility of capsanthin in supercritical carbon dioxide
- Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
- Solid-Liquid Equilibria in Fatty Acid/Triglycerol Systems
- Solid Liquid Equilibrium of Binary Mixtures Containing Fatty Acids and Triacylglycerols
- Phase Equilibria of Glycerol Tristearate and Glycerol Trioleate in Carbon Dioxide and Sulfur Hexafluoride
- Solubility of .beta.-Carotene and Glyceryl Trioleate Mixture in Supercritical CO2
- Viscosities of Fatty Mixtures: Experimental Data and Prediction
- Phase Equilibrium of Biodiesel Compounds for the Triolein + Palmitic Acid + Methanol System with Dimethyl Ether as Cosolvent
- Joback Method
- McGowan Method
- NIST Webbook
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