- 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
-
CCCCCCCCC=CCCCCCCCC(=O)OCC(COC
(=O)CCCCCCCC=CCCCCCCCC)OC(=O)C CCCCCCC=CCCCCCCCC - Molecular Weight1
- 885.43
- CAS
- 122-32-7
- 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).
- 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).
- 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).
- 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°liquid | -35099.60 ± 1.30 | kJ/mol | NIST |
| ΔfG° | -34.48 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -1607.83 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 148.83 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 169.43 | kJ/mol | Joback Calculated Property |
| log10WS | -19.94 | Crippen Calculated Property | |
| logPoct/wat | 18.097 | Crippen Calculated Property | |
| McVol | 823.410 | ml/mol | McGowan Calculated Property |
| Pc | 245.06 | kPa | Joback Calculated Property |
| Tboil | 1744.47 | K | Joback Calculated Property |
| Tc | 4418.33 | K | Joback Calculated Property |
| Tfus | [268.20; 279.22] | K |
|
| Tfus | 268.20 | K | Solid-L... |
| Tfus | 279.22 | K | Solid L... |
| Vc | 3.233 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [3418.56; 18829.83] | J/mol×K | [1744.47; 4418.33] |
|
| Cp,gas | 3418.56 | J/mol×K | 1744.47 | Joback Calculated Property |
| Cp,gas | 3789.05 | J/mol×K | 2190.11 | Joback Calculated Property |
| Cp,gas | 4601.71 | J/mol×K | 2635.76 | Joback Calculated Property |
| Cp,gas | 6184.33 | J/mol×K | 3081.40 | Joback Calculated Property |
| Cp,gas | 8864.70 | J/mol×K | 3527.04 | Joback Calculated Property |
| Cp,gas | 12970.60 | J/mol×K | 3972.68 | Joback Calculated Property |
| Cp,gas | 18829.83 | J/mol×K | 4418.33 | Joback Calculated Property |
| η | [4.4262050e-08; 0.0000014] | Pa×s | [918.39; 1744.47] |
|
| η | 0.0000014 | Pa×s | 918.39 | Joback Calculated Property |
| η | 0.0000006 | Pa×s | 1056.07 | Joback Calculated Property |
| η | 0.0000003 | Pa×s | 1193.75 | Joback Calculated Property |
| η | 0.0000001 | Pa×s | 1331.43 | Joback Calculated Property |
| η | 9.1401528e-08 | Pa×s | 1469.11 | Joback Calculated Property |
| η | 6.1659533e-08 | Pa×s | 1606.79 | Joback Calculated Property |
| η | 4.4262050e-08 | Pa×s | 1744.47 | Joback Calculated Property |
Similar Compounds
Find more compounds similar to Triolein.
Mixtures
- Triolein + n-Hexadecanoic acid
- Triolein + Tripalmitin
- Triolein + Methyl Alcohol
- Hydrogen + Triolein
- Triolein + Glycerin
- Triolein + Water
- Triolein + Carbon dioxide + «beta» Carotene
- Triolein + Tetradecanoic acid + 1-Hexanol
- Triolein + 1-Butanol + Tetradecanoic acid
- 1-Propanol + Triolein + Tetradecanoic acid
- Triolein + Isopropyl Alcohol + Tetradecanoic acid
- Oleic Acid + Triolein + Ethanol
- Triolein + Carbon dioxide
- Triolein + Sulfur hexafluoride
- Oleic Acid + Triolein
- Triolein + 9,12-Octadecadienoic acid (Z,Z)-
- Triolein + Dimethyl ether + Methyl Alcohol
Sources
- 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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