| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 1.4286 | Relay (1.0) Calculated Property | |
| ΔfG° | 252.24 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -793.50 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | [81.55; 102.51] | kJ/mol |
|
| ΔfusH° | 81.55 | kJ/mol | Solid liquid equilibria and purity determination for binary n-alkane + naphthalene systems |
| ΔfusH° | 102.51 | kJ/mol | Observation of multiple phase transitions in some even n-alkanes using a high resolution and super-sensitive DSC |
| ΔvapH° | 182.80 | kJ/mol | NIST |
| IE | 10.46 | eV | Relay (1.0) Calculated Property |
| log10WS | -13.02 | Relay (1.0) Calculated Property | |
| logPoct/wat | 14.290 | Crippen Calculated Property | |
| McVol | 518.100 | ml/mol | McGowan Calculated Property |
| Pc | 457.74 | kPa | Joback Calculated Property |
| Tboil | 673.22 | K | Relay (1.0) Calculated Property |
| Tc | 888.00 | K | Critical temperatures and pressures of C40, C44, and C60 normal alkanes measured by the pulse-heating technique |
| Tfus | [348.00; 351.70] | K |
|
| Tfus | 349.20 ± 0.30 | K | NIST |
| Tfus | 349.05 ± 0.50 | K | NIST |
| Tfus | 349.00 ± 0.40 | K | NIST |
| Tfus | 348.70 ± 1.00 | K | NIST |
| Tfus | 349.10 ± 0.50 | K | NIST |
| Tfus | 349.00 ± 3.00 | K | NIST |
| Tfus | 350.00 ± 2.00 | K | NIST |
| Tfus | 349.10 ± 0.50 | K | NIST |
| Tfus | 348.88 ± 0.20 | K | NIST |
| Tfus | 349.90 ± 1.00 | K | NIST |
| Tfus | 349.90 ± 1.00 | K | NIST |
| Tfus | 349.40 ± 1.00 | K | NIST |
| Tfus | 348.30 ± 1.00 | K | NIST |
| Tfus | 350.00 ± 6.00 | K | NIST |
| Tfus | 349.20 ± 0.60 | K | NIST |
| Tfus | 349.00 ± 0.05 | K | NIST |
| Tfus | 349.00 ± 2.00 | K | NIST |
| Tfus | 349.20 ± 0.50 | K | NIST |
| Tfus | 349.20 ± 2.00 | K | NIST |
| Tfus | 349.20 ± 0.60 | K | NIST |
| Tfus | 348.00 ± 2.00 | K | NIST |
| Tfus | 349.00 ± 3.00 | K | NIST |
| Tfus | 349.00 ± 0.60 | K | NIST |
| Tfus | 348.40 ± 4.00 | K | NIST |
| Tfus | Outlier 351.70 ± 4.00 | K | NIST |
| Tfus | 349.00 ± 2.00 | K | NIST |
| Tfus | 349.00 ± 2.00 | K | NIST |
| Vc | 2.091 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.07; 101.61] | kPa | [535.15; 771.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.30292e+02 | |||
| Coefficient B | -4.15156e+04 | |||
| Coefficient C | -5.72371e+01 | |||
| Coefficient D | 1.45802e-05 | |||
| Temperature range, min. | 535.15 | |||
| Temperature range, max. | 771.15 | |||
| Pvap | 0.07 | kPa | 535.15 | Calculated Property |
| Pvap | 0.25 | kPa | 561.37 | Calculated Property |
| Pvap | 0.76 | kPa | 587.59 | Calculated Property |
| Pvap | 2.03 | kPa | 613.82 | Calculated Property |
| Pvap | 4.77 | kPa | 640.04 | Calculated Property |
| Pvap | 10.13 | kPa | 666.26 | Calculated Property |
| Pvap | 19.79 | kPa | 692.48 | Calculated Property |
| Pvap | 36.04 | kPa | 718.71 | Calculated Property |
| Pvap | 61.96 | kPa | 744.93 | Calculated Property |
| Pvap | 101.61 | kPa | 771.15 | Calculated Property |
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