- InChI
- InChI=1S/C27H50O6/c1-4-7-10-13-16-19-25(28)31-22-24(33-27(30)21-18-15-12-9-6-3)23-32-26(29)20-17-14-11-8-5-2/h24H,4-23H2,1-3H3
- InChI Key
- VLPFTAMPNXLGLX-UHFFFAOYSA-N
- Formula
- C27H50O6
- SMILES
-
CCCCCCCC(=O)OCC(COC(=O)CCCCCCC
)OC(=O)CCCCCCC - Molecular Weight1
- 470.69
- Other Names
-
- 1,2,3-propanetriol trioctanoate
- Caprylic acid triglyceride
- Caprylic triglyceride
- Caprylin
- Captex 8000
- Emalex KTG
- Glycerin tricaprylate
- Glycerol trioctanoate
- Maceight
- Miglyol 808
- NSC 4059
- Octanoic acid triglyceride
- Octanoic acid, 1,1',1''-(1,2,3-propanetriyl) ester
- Octanoic acid, 1,2,3-propanetriyl ester
- Octanoin, tri-
- Panacete 800
- RATO
- Sefsol 810
- Tricaprylic Glyceride
- Tricapryloylglycerol
- Tricaprylyl glycerin
- Trioctanoylglycerol
- glyceryl tricaprylate
- glyceryl trioctanoate
- tricaprilin
- tricaprylin
- trioctanoin
- ω : Acentric Factor.
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase 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).
- IE : Ionization energy (eV).
- 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).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 1.2174 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | -15259.00 ± 1.80 | kJ/mol | NIST |
| ΔfG° | -914.70 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -1557.73 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 75.27 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 135.40 ± 4.70 | kJ/mol | NIST |
| IE | 9.61 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.52 | Relay (1.0) Calculated Property | |
| logPoct/wat | 7.066 | Crippen Calculated Property | |
| McVol | 413.610 | ml/mol | McGowan Calculated Property |
| Pc | 593.20 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | 2958.00 | NIST | |
| Tboil | 737.50 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | [836.00; 850.70] | K |
|
| Tc | 836.00 | K | Critical properties, heat capacities, and thermal diffusivities of four saturated triglycerides |
| Tc | 850.70 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [283.05; 283.15] | K |
|
| Tfus | 283.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 283.05 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 283.05 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 16.21 | ChemSep v8.3 pure component data Compiled value | |
| URi | 19.64 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 2.210 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.1853460 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | 920.00 | J/mol×K | 338.00 | NIST |
| ΔvapH | [116.00; 118.70] | kJ/mol | [386.00; 424.50] |
|
| ΔvapH | 118.70 | kJ/mol | 386.00 | NIST |
| ΔvapH | 116.00 | kJ/mol | 424.50 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 102.00 | 952.7 |
| 298.15 | 102.00 | 948.9 |
| 303.15 | 102.00 | 944.9 |
| 313.15 | 102.00 | 937.4 |
| 333.15 | 102.00 | 922.5 |
| 353.15 | 102.00 | 907.7 |
| 298.15 | 120.00 | 949.9 |
| 298.15 | 9830.00 | 955.5 |
| 298.15 | 20100.00 | 961.3 |
| 298.15 | 30020.00 | 966.6 |
| 298.15 | 40050.00 | 971.9 |
| 298.15 | 50040.00 | 977.1 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [542.84; 1609.98] | J/mol×K | [255.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.81981e+02 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 7.52476e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 542.84 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 801.85 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 1005.64 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 1160.73 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 1280.44 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 1374.89 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 1451.02 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 1513.55 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 1565.77 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 1609.98 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0447753; 0.0002222] | Pa×s | [277.00; 737.50] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -5.04980e+01 | |||
| Coefficient B | 4.70300e+03 | |||
| Coefficient C | 5.40780e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 277.00 | |||
| Temperature range, max. | 737.50 | |||
| η | 0.0447753 | Pa×s | 277.00 | Calculated Property |
| η | 0.0079335 | Pa×s | 328.17 | Calculated Property |
| η | 0.0025133 | Pa×s | 379.33 | Calculated Property |
| η | 0.0011414 | Pa×s | 430.50 | Calculated Property |
| η | 0.0006565 | Pa×s | 481.67 | Calculated Property |
| η | 0.0004437 | Pa×s | 532.83 | Calculated Property |
| η | 0.0003362 | Pa×s | 584.00 | Calculated Property |
| η | 0.0002768 | Pa×s | 635.17 | Calculated Property |
| η | 0.0002423 | Pa×s | 686.33 | Calculated Property |
| η | 0.0002222 | Pa×s | 737.50 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [3.28e-11; 587.34] | kPa | [283.00; 850.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.31561e+02 | |||
| Coefficient B | -1.97698e+04 | |||
| Coefficient C | -1.52062e+01 | |||
| Coefficient D | 1.70320e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 283.00 | |||
| Temperature range, max. | 850.00 | |||
| Pvap | 3.28e-11 | kPa | 283.00 | Calculated Property |
| Pvap | 5.17e-07 | kPa | 346.00 | Calculated Property |
| Pvap | 2.71e-04 | kPa | 409.00 | Calculated Property |
| Pvap | 0.02 | kPa | 472.00 | Calculated Property |
| Pvap | 0.41 | kPa | 535.00 | Calculated Property |
| Pvap | 3.88 | kPa | 598.00 | Calculated Property |
| Pvap | 21.10 | kPa | 661.00 | Calculated Property |
| Pvap | 79.09 | kPa | 724.00 | Calculated Property |
| Pvap | 232.07 | kPa | 787.00 | Calculated Property |
| Pvap | 587.34 | kPa | 850.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [960.62; 212.65] | kg/m3 | [283.05; 850.70] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 3.94747e+01 | |||
| Coefficient B | 1.85630e-01 | |||
| Coefficient C | 8.50700e+02 | |||
| Coefficient D | 2.72990e-01 | |||
| Temperature range, min. | 283.05 | |||
| Temperature range, max. | 850.70 | |||
| ρl | 960.62 | kg/m3 | 283.05 | Calculated Property |
| ρl | 915.86 | kg/m3 | 346.12 | Calculated Property |
| ρl | 869.22 | kg/m3 | 409.19 | Calculated Property |
| ρl | 820.23 | kg/m3 | 472.27 | Calculated Property |
| ρl | 768.19 | kg/m3 | 535.34 | Calculated Property |
| ρl | 712.04 | kg/m3 | 598.41 | Calculated Property |
| ρl | 649.92 | kg/m3 | 661.48 | Calculated Property |
| ρl | 578.13 | kg/m3 | 724.56 | Calculated Property |
| ρl | 486.57 | kg/m3 | 787.63 | Calculated Property |
| ρl | 212.65 | kg/m3 | 850.70 | Calculated Property |
Similar Compounds
![Hexadecanoic acid, 2-(acetyloxy)-1-[(acetyloxy)methyl]ethyl ester.](data:image/png;base64,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)
Find more compounds similar to GLYCEROL TRICAPRYLATE.
Mixtures
- n-Hexane + n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE
- n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE + 1-Hexanol
- n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE + 1-Pentanol
- 1-Butanol + n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE
- 1-Propanol + n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE
- 2-Propanol + n-Hexadecanoic acid + GLYCEROL TRICAPRYLATE
- 9,12-Octadecadienoic acid (Z,Z)- + Ethanol + GLYCEROL TRICAPRYLATE
- n-Decanoic acid + GLYCEROL TRICAPRYLATE
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Crippen Method
- Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
- Critical properties, heat capacities, and thermal diffusivities of four saturated triglycerides
- Thermodynamic Modeling of Triglycerides using PC-SAFT
- Viscosities of Fatty Mixtures: Experimental Data and Prediction
- Joback Method
- McGowan Method
- NIST Webbook
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