| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | -35806.70 ± 1.80 | kJ/mol | NIST |
| ΔfH°gas | -2107.15 | kJ/mol | Relay (1.0) Calculated Property |
| 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 | 224.98 | kPa | Joback Calculated Property |
| S°liquid | 1534.70 | J/mol×K | NIST |
| Tboil | 859.77 | K | Relay (1.0) Calculated Property |
| Tc | 994.17 | K | Relay (1.0) Calculated Property |
| Tfus | [330.00; 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 | 344.60 ± 2.00 | K | NIST |
| Tfus | 330.00 ± 1.00 | K | NIST |
| Ttriple | [327.20; 346.30] | K |
|
| 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 |
Cheméo can also estimate Critical Volume, Standard Gibbs free energy of formation, Acentric Factor 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.
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [3318.88; 12078.54] | J/mol×K | [1677.98; 4487.59] | |
| Cp,gas | 3318.88 | J/mol×K | 1677.98 | Joback Calculated Property |
| Cp,gas | 3331.13 | J/mol×K | 2146.25 | Joback Calculated Property |
| Cp,gas | 3515.60 | J/mol×K | 2614.52 | Joback Calculated Property |
| Cp,gas | 4177.43 | J/mol×K | 3082.78 | Joback Calculated Property |
| Cp,gas | 5621.77 | J/mol×K | 3551.05 | Joback Calculated Property |
| Cp,gas | 8153.76 | J/mol×K | 4019.32 | Joback Calculated Property |
| Cp,gas | 12078.54 | J/mol×K | 4487.59 | Joback Calculated Property |
| 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 |
| η | [3.6563340e-08; 0.0000021] | Pa×s | [844.14; 1677.98] | |
| η | 0.0000021 | Pa×s | 844.14 | Joback Calculated Property |
| η | 0.0000007 | Pa×s | 983.11 | Joback Calculated Property |
| η | 0.0000003 | Pa×s | 1122.09 | Joback Calculated Property |
| η | 0.0000001 | Pa×s | 1261.06 | Joback Calculated Property |
| η | 8.2564837e-08 | Pa×s | 1400.03 | Joback Calculated Property |
| η | 5.2960075e-08 | Pa×s | 1539.01 | Joback Calculated Property |
| η | 3.6563340e-08 | Pa×s | 1677.98 | Joback Calculated Property |
| 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 |
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