| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 2.1433 | Relay (1.0) Calculated Property | |
| ΔcH°solid | -31605.90 ± 1.80 | kJ/mol | NIST |
| ΔfG° | -325.66 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -1986.74 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 121.00 | kJ/mol | Binary solid liquid gas equilibrium of the tripalmitin/CO2 and ubiquinone/CO2 systems |
| ΔvapH° | 217.10 ± 7.60 | kJ/mol | NIST |
| IE | 10.38 | eV | Relay (1.0) Calculated Property |
| log10WS | -13.59 | Relay (1.0) Calculated Property | |
| logPoct/wat | 16.429 | Crippen Calculated Property | |
| McVol | 751.770 | ml/mol | McGowan Calculated Property |
| Pc | 280.76 | kPa | Joback Calculated Property |
| S°liquid | 1387.40 | J/mol×K | NIST |
| Tboil | 822.74 | K | Relay (1.0) Calculated Property |
| Tc | 962.22 | K | Relay (1.0) Calculated Property |
| Tfus | [337.95; 340.70] | K |
|
| Tfus | 337.95 | K | KDB |
| Tfus | 339.44 | K | Solid-liquid phase equilibrium diagrams of binary mixtures containing fatty acids, fatty alcohol compounds and tripalmitin using differential scanning calorimetry |
| Tfus | 340.70 | K | Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane |
| Tfus | 339.00 | K | Solid-Liquid Equilibria in Fatty Acid/Triglycerol Systems |
| Tfus | 338.82 | K | Solid Liquid Equilibrium of Binary Mixtures Containing Fatty Acids and Triacylglycerols |
| Tfus | 338.80 ± 2.00 | K | NIST |
| Tfus | 339.40 ± 0.70 | K | NIST |
| Ttriple | [317.90; 339.50] | K |
|
| Ttriple | 318.40 ± 1.00 | K | NIST |
| Ttriple | 329.30 ± 1.00 | K | NIST |
| Ttriple | 339.50 ± 1.00 | K | NIST |
| Ttriple | 317.90 ± 0.20 | K | NIST |
| Ttriple | 338.90 ± 0.20 | K | NIST |
| Vc | 2.892 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [2982.50; 3839.85] | J/mol×K | [1594.71; 3258.54] | |
| Cp,gas | 2982.50 | J/mol×K | 1594.71 | Joback Calculated Property |
| Cp,gas | 2990.76 | J/mol×K | 1872.02 | Joback Calculated Property |
| Cp,gas | 2984.01 | J/mol×K | 2149.32 | Joback Calculated Property |
| Cp,gas | 3013.89 | J/mol×K | 2426.63 | Joback Calculated Property |
| Cp,gas | 3132.06 | J/mol×K | 2703.93 | Joback Calculated Property |
| Cp,gas | 3390.16 | J/mol×K | 2981.24 | Joback Calculated Property |
| Cp,gas | 3839.85 | J/mol×K | 3258.54 | Joback Calculated Property |
| Cp,liquid | [1665.00; 1753.10] | J/mol×K | [338.80; 343.00] | |
| Cp,liquid | 1753.10 | J/mol×K | 338.80 | NIST |
| Cp,liquid | 1665.00 | J/mol×K | 343.00 | NIST |
| η | [0.0000002; 0.0000049] | Pa×s | [866.01; 1594.71] | |
| η | 0.0000049 | Pa×s | 866.01 | Joback Calculated Property |
| η | 0.0000020 | Pa×s | 987.46 | Joback Calculated Property |
| η | 0.0000010 | Pa×s | 1108.91 | Joback Calculated Property |
| η | 0.0000006 | Pa×s | 1230.36 | Joback Calculated Property |
| η | 0.0000004 | Pa×s | 1351.81 | Joback Calculated Property |
| η | 0.0000003 | Pa×s | 1473.26 | Joback Calculated Property |
| η | 0.0000002 | Pa×s | 1594.71 | Joback Calculated Property |
| ΔfusH | [121.00; 179.37] | kJ/mol | [337.40; 340.50] | |
| ΔfusH | 121.00 | kJ/mol | 337.40 | NIST |
| ΔfusH | 179.37 | kJ/mol | 338.90 | NIST |
| ΔfusH | 179.37 | kJ/mol | 338.90 | NIST |
| ΔfusH | 162.60 | kJ/mol | 340.50 | NIST |
| ΔvapH | [160.80; 166.30] | kJ/mol | [483.00; 539.00] | |
| ΔvapH | 166.30 | kJ/mol | 483.00 | NIST |
| ΔvapH | 160.80 | kJ/mol | 539.00 | NIST |
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