- InChI
- InChI=1S/C57H110O6/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/h54H,4-53H2,1-3H3
- InChI Key
- DCXXMTOCNZCJGO-UHFFFAOYSA-N
- Formula
- C57H110O6
- SMILES
-
CCCCCCCCCCCCCCCCCC(=O)OCC(COC(
=O)CCCCCCCCCCCCCCCCC)OC(=O)CCC CCCCCCCCCCCCCC - Molecular Weight1
- 891.48
- CAS
- 555-43-1
- Other Names
-
- 1,2,3-Propanetriyl trioctadecanoate
- 1,2,3-propanetriyl tri(octadecanoate)
- Dynasan 118
- Glycowax S 932
- Hardened oil
- Octadecanoic acid, 1,1',1''-(1,2,3-propanetriyl) ester
- Spezialfett 118
- Stearic triglyceride
- Stearin
- Stearoyl triglyceride
- Trioctadecanoin
- glycerol trioctadecanoate
- glycerol tristearate
- glyceryl tristearate
- octadecanoic acid, 1,2,3-propanetriyl ester
- stearic acid triglyceride
- stearic acid triglycerin ester
- stearin, tri-
- 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).
- ΔfusH : Enthalpy of fusion 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).
- 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).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- 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.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 2.0894 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | -35806.70 ± 1.80 | kJ/mol | NIST |
| ΔfG° | -657.59 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -2176.93 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | [115.71; 197.55] | kJ/mol |
|
| ΔfusH° | 115.71 | kJ/mol | Measurement and modelling of binary (solid + liquid + vapour) equilibria involving lipids and CO2 |
| ΔfusH° | 197.55 | kJ/mol | Thermal Properties of Tristearin by Adiabatic and Differential Scanning Calorimetry |
| ΔvapH° | 236.20 ± 8.30 | kJ/mol | NIST |
| IE | 10.59 | eV | Relay (1.0) Calculated Property |
| log10WS | -15.24 | Relay (1.0) Calculated Property | |
| logPoct/wat | 18.769 | Crippen Calculated Property | |
| McVol | 836.310 | ml/mol | McGowan Calculated Property |
| Pc | 197.70 | kPa | ChemSep v8.3 pure component data Compiled value |
| S°liquid | 1534.70 | J/mol×K | NIST |
| Tboil | 898.30 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 936.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [328.15; 346.60] | K |
|
| Tfus | 346.60 | K | Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane |
| Tfus | 345.75 | K | Solid Liquid Equilibrium of Binary Mixtures Containing Fatty Acids and Triacylglycerols |
| Tfus | 328.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 346.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 344.60 ± 2.00 | K | NIST |
| Tfus | 330.00 ± 1.00 | K | NIST |
| Ttriple | [327.20; 346.30] | K |
|
| Ttriple | 345.94 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 336.70 ± 1.00 | K | NIST |
| Ttriple | 346.30 ± 1.00 | K | NIST |
| Ttriple | 328.30 ± 1.00 | K | NIST |
| Ttriple | 327.20 ± 0.20 | K | NIST |
| Ttriple | 345.70 ± 0.20 | K | NIST |
| Ttriple | 327.20 ± 0.20 | K | NIST |
| Ttriple | 345.70 ± 0.20 | K | NIST |
| UQi | 32.41 | ChemSep v8.3 pure component data Compiled value | |
| URi | 39.88 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 5.710 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.1450550 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [1969.00; 1975.00] | J/mol×K | [346.50; 353.00] |
|
| Cp,liquid | 1969.00 | J/mol×K | 346.50 | NIST |
| Cp,liquid | 1975.00 | J/mol×K | 353.00 | NIST |
| ΔfusH | [203.26; 203.26] | kJ/mol | [345.70; 345.70] |
|
| ΔfusH | 203.26 | kJ/mol | 345.70 | NIST |
| ΔfusH | 203.26 | kJ/mol | 345.70 | NIST |
| ΔvapH | [167.50; 174.90] | kJ/mol | [506.00; 554.50] |
|
| ΔvapH | 174.90 | kJ/mol | 506.00 | NIST |
| ΔvapH | 167.50 | kJ/mol | 554.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [1096.11; 3317.72] | 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 | 5.53040e+02 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 8.25801e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 1096.11 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 1635.32 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 2059.59 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 2382.45 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 2631.66 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 2828.29 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 2986.78 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 3116.97 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 3225.67 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 3317.72 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0169967; 0.0004890] | Pa×s | [345.94; 898.30] |
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 | -5.85260e+01 | |||
| Coefficient B | 5.52890e+03 | |||
| Coefficient C | 6.58010e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 345.94 | |||
| Temperature range, max. | 898.30 | |||
| η | 0.0169967 | Pa×s | 345.94 | Calculated Property |
| η | 0.0044794 | Pa×s | 407.31 | Calculated Property |
| η | 0.0019070 | Pa×s | 468.69 | Calculated Property |
| η | 0.0010935 | Pa×s | 530.06 | Calculated Property |
| η | 0.0007618 | Pa×s | 591.43 | Calculated Property |
| η | 0.0006057 | Pa×s | 652.81 | Calculated Property |
| η | 0.0005284 | Pa×s | 714.18 | Calculated Property |
| η | 0.0004926 | Pa×s | 775.55 | Calculated Property |
| η | 0.0004820 | Pa×s | 836.93 | Calculated Property |
| η | 0.0004890 | Pa×s | 898.30 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.00e-14; 197.73] | kPa | [346.00; 936.00] |
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 | 2.18881e+02 | |||
| Coefficient B | -3.39069e+04 | |||
| Coefficient C | -2.60721e+01 | |||
| Coefficient D | 1.49642e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 346.00 | |||
| Temperature range, max. | 936.00 | |||
| Pvap | 2.00e-14 | kPa | 346.00 | Calculated Property |
| Pvap | 1.31e-09 | kPa | 411.56 | Calculated Property |
| Pvap | 2.32e-06 | kPa | 477.11 | Calculated Property |
| Pvap | 4.41e-04 | kPa | 542.67 | Calculated Property |
| Pvap | 0.02 | kPa | 608.22 | Calculated Property |
| Pvap | 0.33 | kPa | 673.78 | Calculated Property |
| Pvap | 2.82 | kPa | 739.33 | Calculated Property |
| Pvap | 15.20 | kPa | 804.89 | Calculated Property |
| Pvap | 60.13 | kPa | 870.44 | Calculated Property |
| Pvap | 197.73 | kPa | 936.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [871.83; 156.26] | kg/m3 | [340.00; 936.00] |
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 | 2.26472e+01 | |||
| Coefficient B | 1.44930e-01 | |||
| Coefficient C | 9.36000e+02 | |||
| Coefficient D | 2.58160e-01 | |||
| Temperature range, min. | 340.00 | |||
| Temperature range, max. | 936.00 | |||
| ρl | 871.83 | kg/m3 | 340.00 | Calculated Property |
| ρl | 828.08 | kg/m3 | 406.22 | Calculated Property |
| ρl | 782.58 | kg/m3 | 472.44 | Calculated Property |
| ρl | 734.91 | kg/m3 | 538.67 | Calculated Property |
| ρl | 684.41 | kg/m3 | 604.89 | Calculated Property |
| ρl | 630.10 | kg/m3 | 671.11 | Calculated Property |
| ρl | 570.25 | kg/m3 | 737.33 | Calculated Property |
| ρl | 501.41 | kg/m3 | 803.56 | Calculated Property |
| ρl | 414.22 | kg/m3 | 869.78 | Calculated Property |
| ρl | 156.26 | kg/m3 | 936.00 | Calculated Property |
Similar Compounds
![Octadecanoic acid, 2-(acetyloxy)-1-[(acetyloxy)methyl]ethyl ester.](data:image/png;base64,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)
Find more compounds similar to Tristearin.
Mixtures
- Propane, 1-bromo- + Tristearin
- Hexadecane + Tristearin
- Carbon dioxide + Tristearin
- Tristearin + Sulfur hexafluoride
- Nitrogen + Tristearin
- Tripalmitin + Tristearin
- Tristearin + n-Hexadecanoic acid
- 9,12-Octadecadienoic acid (Z,Z)- + Tristearin
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
- Measurement and modelling of binary (solid + liquid + vapour) equilibria involving lipids and CO2
- Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane
- Thermal Properties of Tristearin by Adiabatic and Differential Scanning Calorimetry
- Solid Liquid Equilibrium of Binary Mixtures Containing Fatty Acids and Triacylglycerols
- Solubilities of Fatty Acids and Triglycerides in 1-Bromopropane
- Phase Equilibria of Glycerol Tristearate and Glycerol Trioleate in Carbon Dioxide and Sulfur Hexafluoride
- McGowan Method
- NIST Webbook
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.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.