| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 1.9336 | Relay (1.0) Calculated Property | |
| ΔcH°solid | -27643.70 ± 1.80 | kJ/mol | NIST |
| ΔfG° | -376.18 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -1867.44 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 117.14 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 199.20 ± 6.90 | kJ/mol | NIST |
| IE | 10.17 | eV | Relay (1.0) Calculated Property |
| log10WS | -11.91 | Relay (1.0) Calculated Property | |
| logPoct/wat | 14.088 | Crippen Calculated Property | |
| McVol | 667.230 | ml/mol | McGowan Calculated Property |
| Pc | 343.95 | kPa | Joback Calculated Property |
| S°liquid | 1246.00 | J/mol×K | NIST |
| Tboil | 785.45 | K | Relay (1.0) Calculated Property |
| Tc | 925.00 | K | Critical properties, heat capacities, and thermal diffusivities of four saturated triglycerides |
| Tfus | 331.10 | K | Solid Liquid Equilibria in the Binary Systems of Saturated Fatty Acids or Triglycerides (C12 to C18) + Hexadecane |
| Ttriple | [305.10; 330.80] | K |
|
| Ttriple | 305.10 ± 1.00 | K | NIST |
| Ttriple | 319.70 ± 1.00 | K | NIST |
| Ttriple | 330.80 ± 1.00 | K | NIST |
| Ttriple | 305.50 ± 0.20 | K | NIST |
| Ttriple | 330.20 ± 0.20 | K | NIST |
| Vc | 2.568 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [2538.38; 2620.22] | J/mol×K | [1457.43; 2403.78] | |
| Cp,gas | 2603.95 | J/mol×K | 1457.43 | Joback Calculated Property |
| Cp,gas | 2620.22 | J/mol×K | 1615.15 | Joback Calculated Property |
| Cp,gas | 2615.17 | J/mol×K | 1772.88 | Joback Calculated Property |
| Cp,gas | 2596.65 | J/mol×K | 1930.60 | Joback Calculated Property |
| Cp,gas | 2572.46 | J/mol×K | 2088.33 | Joback Calculated Property |
| Cp,gas | 2550.43 | J/mol×K | 2246.05 | Joback Calculated Property |
| Cp,gas | 2538.38 | J/mol×K | 2403.78 | Joback Calculated Property |
| Cp,liquid | [1481.00; 1555.20] | J/mol×K | [331.50; 333.00] | |
| Cp,liquid | 1555.20 | J/mol×K | 331.50 | NIST |
| Cp,liquid | 1481.00 | J/mol×K | 333.00 | NIST |
| η | [0.0000005; 0.0000133] | Pa×s | [798.39; 1457.43] | |
| η | 0.0000133 | Pa×s | 798.39 | Joback Calculated Property |
| η | 0.0000056 | Pa×s | 908.23 | Joback Calculated Property |
| η | 0.0000028 | Pa×s | 1018.07 | Joback Calculated Property |
| η | 0.0000017 | Pa×s | 1127.91 | Joback Calculated Property |
| η | 0.0000011 | Pa×s | 1237.75 | Joback Calculated Property |
| η | 0.0000007 | Pa×s | 1347.59 | Joback Calculated Property |
| η | 0.0000005 | Pa×s | 1457.43 | Joback Calculated Property |
| ΔfusH | [152.20; 152.20] | kJ/mol | [330.20; 330.20] | |
| ΔfusH | 152.20 | kJ/mol | 330.20 | NIST |
| ΔfusH | 152.20 | kJ/mol | 330.20 | NIST |
| ΔvapH | [147.80; 155.80] | kJ/mol | [469.00; 519.50] | |
| ΔvapH | 155.80 | kJ/mol | 469.00 | NIST |
| ΔvapH | 147.80 | kJ/mol | 519.50 | NIST |
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