| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | [-23860.00; -23731.60] | kJ/mol |
|
| ΔcH°solid | -23731.60 ± 1.80 | kJ/mol | NIST |
| ΔcH°solid | -23860.00 | kJ/mol | NIST |
| ΔfH°gas | -1748.57 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 106.35 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 180.00 ± 6.30 | kJ/mol | NIST |
| IE | 9.96 | eV | Relay (1.0) Calculated Property |
| log10WS | -10.17 | Relay (1.0) Calculated Property | |
| logPoct/wat | 11.747 | Crippen Calculated Property | |
| McVol | 582.690 | ml/mol | McGowan Calculated Property |
| Pc | 409.94 | kPa | Joback Calculated Property |
| S°liquid | 1071.50 | J/mol×K | NIST |
| Tboil | 747.95 | K | Relay (1.0) Calculated Property |
| Tc | 899.00 | K | Critical properties, heat capacities, and thermal diffusivities of four saturated triglycerides |
| Tfus | [319.50; 321.90] | K |
|
| Tfus | 321.90 | K | Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane |
| Tfus | 319.50 ± 0.20 | K | NIST |
| Tfus | 319.50 ± 0.20 | K | NIST |
| Ttriple | [287.40; 319.60] | K |
|
| Ttriple | 319.60 ± 1.00 | K | NIST |
| Ttriple | 287.40 ± 1.00 | K | NIST |
| Ttriple | 307.20 ± 1.00 | 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 | [2189.14; 2227.14] | J/mol×K | [1266.14; 1780.82] | |
| Cp,gas | 2194.63 | J/mol×K | 1266.14 | Joback Calculated Property |
| Cp,gas | 2215.08 | J/mol×K | 1351.92 | Joback Calculated Property |
| Cp,gas | 2225.56 | J/mol×K | 1437.70 | Joback Calculated Property |
| Cp,gas | 2227.14 | J/mol×K | 1523.48 | Joback Calculated Property |
| Cp,gas | 2220.89 | J/mol×K | 1609.26 | Joback Calculated Property |
| Cp,gas | 2207.87 | J/mol×K | 1695.04 | Joback Calculated Property |
| Cp,gas | 2189.14 | J/mol×K | 1780.82 | Joback Calculated Property |
| Cp,liquid | [1305.00; 1355.60] | J/mol×K | [323.00; 330.70] | |
| Cp,liquid | 1305.00 | J/mol×K | 323.00 | NIST |
| Cp,liquid | 1355.60 | J/mol×K | 330.70 | NIST |
| η | [0.0000009; 0.0000509] | Pa×s | [641.28; 1266.14] | |
| η | 0.0000509 | Pa×s | 641.28 | Joback Calculated Property |
| η | 0.0000164 | Pa×s | 745.42 | Joback Calculated Property |
| η | 0.0000070 | Pa×s | 849.57 | Joback Calculated Property |
| η | 0.0000036 | Pa×s | 953.71 | Joback Calculated Property |
| η | 0.0000021 | Pa×s | 1057.85 | Joback Calculated Property |
| η | 0.0000014 | Pa×s | 1162.00 | Joback Calculated Property |
| η | 0.0000009 | Pa×s | 1266.14 | Joback Calculated Property |
| ΔfusH | [123.51; 123.51] | kJ/mol | [319.50; 319.50] | |
| ΔfusH | 123.51 | kJ/mol | 319.50 | NIST |
| ΔfusH | 123.51 | kJ/mol | 319.50 | NIST |
| ΔvapH | [137.60; 147.10] | kJ/mol | [438.00; 489.00] | |
| ΔvapH | 147.10 | kJ/mol | 438.00 | NIST |
| ΔvapH | 137.60 | kJ/mol | 489.00 | NIST |
| ρl | [870.40; 905.10] | kg/m3 | [303.15; 353.15] | |
| ρl | 905.10 | kg/m3 | 303.15 | Thermodynamic Modeling of Triglycerides using PC-SAFT |
| ρl | 899.60 | kg/m3 | 313.15 | Thermodynamic Modeling of Triglycerides using PC-SAFT |
| ρl | 886.90 | kg/m3 | 333.15 | Thermodynamic Modeling of Triglycerides using PC-SAFT |
| ρl | 870.40 | kg/m3 | 353.15 | Thermodynamic Modeling of Triglycerides using PC-SAFT |
Find more compounds similar to Dodecanoic acid, 1,2,3-propanetriyl ester.
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