| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4810 | KDB | |
| ΔcH°liquid | -5315.90 ± 2.40 | kJ/mol | NIST |
| ΔfG° | 248.49 | kJ/mol | Relay (1.0-beta) Calculated Property |
| ΔfH°gas | 162.10 ± 3.20 | kJ/mol | NIST |
| ΔfH°liquid | 94.50 ± 2.60 | kJ/mol | NIST |
| ΔvapH° | [67.60; 67.60] | kJ/mol |
|
| ΔvapH° | 67.60 ± 1.80 | kJ/mol | NIST |
| ΔvapH° | 67.60 | kJ/mol | NIST |
| ΔvapH° | 67.60 ± 1.80 | kJ/mol | NIST |
| IE | 8.56 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.84 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.543 | Crippen Calculated Property | |
| McVol | 118.520 | ml/mol | McGowan Calculated Property |
| Pc | 4900.00 | kPa | KDB |
| Inp | [235.54; 1399.00] |
|
|
| Inp | 1357.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1357.00 | NIST | |
| Inp | 1376.00 | NIST | |
| Inp | 1357.00 | NIST | |
| Inp | 1399.00 | NIST | |
| Inp | 1384.00 | NIST | |
| Inp | 1347.00 | NIST | |
| Inp | 1383.00 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1398.00 | NIST | |
| Inp | 235.54 | NIST | |
| Inp | 236.61 | NIST | |
| Inp | 235.77 | NIST | |
| Inp | 235.54 | NIST | |
| Inp | 1399.00 | NIST | |
| Inp | 1347.00 | NIST | |
| Inp | 1357.00 | NIST | |
| I | [2037.00; 2108.00] |
|
|
| I | 2098.00 | NIST | |
| I | 2037.00 | NIST | |
| I | 2065.00 | NIST | |
| I | 2037.00 | NIST | |
| I | 2065.00 | NIST | |
| I | 2037.00 | NIST | |
| I | 2065.00 | NIST | |
| I | 2066.00 | NIST | |
| I | 2080.00 | NIST | |
| I | 2108.00 | NIST | |
| I | 2098.00 | NIST | |
| I | 2037.00 | NIST | |
| I | 2080.00 | NIST | |
| Tboil | [530.15; 538.80] | K |
|
| Tboil | 538.80 | K | KDB |
| Tboil | 535.20 | K | NIST |
| Tboil | 538.80 ± 0.20 | K | NIST |
| Tboil | 530.15 ± 0.70 | K | NIST |
| Tboil | 534.00 ± 6.00 | K | NIST |
| Tboil | 534.00 ± 5.00 | K | NIST |
| Tboil | 538.80 ± 0.30 | K | NIST |
| Tboil | 534.00 ± 5.00 | K | NIST |
| Tc | 797.00 | K | KDB |
| Tfus | [282.00; 282.70] | K |
|
| Tfus | 282.00 | K | KDB |
| Tfus | 282.70 ± 0.20 | K | NIST |
| Tfus | 282.00 ± 1.50 | K | NIST |
| Vc | 0.444 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 58.20 | kJ/mol | 501.00 | NIST |
| ρl | 1088.23 | kg/m3 | 293.10 | KDB |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [405.28; 566.61] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.49235e+01 | |||
| Coefficient B | -4.51779e+03 | |||
| Coefficient C | -9.65980e+01 | |||
| Temperature range, min. | 405.28 | |||
| Temperature range, max. | 566.61 | |||
| Pvap | 1.33 | kPa | 405.28 | Calculated Property |
| Pvap | 2.98 | kPa | 423.21 | Calculated Property |
| Pvap | 6.11 | kPa | 441.13 | Calculated Property |
| Pvap | 11.70 | kPa | 459.06 | Calculated Property |
| Pvap | 21.04 | kPa | 476.98 | Calculated Property |
| Pvap | 35.91 | kPa | 494.91 | Calculated Property |
| Pvap | 58.53 | kPa | 512.83 | Calculated Property |
| Pvap | 91.62 | kPa | 530.76 | Calculated Property |
| Pvap | 138.42 | kPa | 548.68 | Calculated Property |
| Pvap | 202.63 | kPa | 566.61 | Calculated Property |
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