| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4532 | Relay (1.0) Calculated Property | |
| ΔcH°solid | [-5859.70; -5836.30] | kJ/mol |
|
| ΔcH°solid | -5836.30 ± 4.70 | kJ/mol | NIST |
| ΔcH°solid | -5859.70 ± 4.20 | kJ/mol | NIST |
| ΔfG° | 167.99 | kJ/mol | Relay (1.0-beta) Calculated Property |
| ΔfH°gas | 47.30 ± 4.80 | kJ/mol | NIST |
| ΔfH°solid | -29.20 ± 4.80 | kJ/mol | NIST |
| ΔsubH° | [76.46; 88.70] | kJ/mol |
|
| ΔsubH° | 82.00 ± 0.20 | kJ/mol | NIST |
| ΔsubH° | 76.46 ± 0.16 | kJ/mol | NIST |
| ΔsubH° | 76.50 | kJ/mol | NIST |
| ΔsubH° | 84.40 ± 0.70 | kJ/mol | NIST |
| ΔsubH° | 76.50 ± 0.20 | kJ/mol | NIST |
| ΔsubH° | 88.70 | kJ/mol | NIST |
| ΔvapH° | 75.50 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [7.90; 8.77] | eV |
|
| IE | 8.77 | eV | NIST |
| IE | 8.22 | eV | NIST |
| IE | 7.90 ± 0.05 | eV | NIST |
| IE | 8.09 | eV | NIST |
| log10WS | [-4.60; -4.51] |
|
|
| log10WS | -4.51 | Aq. Solubility Prediction | |
| log10WS | -4.60 | Estimated Solubility | |
| logPoct/wat | 3.586 | Crippen Calculated Property | |
| McVol | 127.430 | ml/mol | McGowan Calculated Property |
| Pc | 3640.00 ± 100.00 | kPa | NIST |
| ρc | 339.75 ± 5.05 | kg/m3 | NIST |
| Inp | [251.74; 1549.20] |
|
|
| Inp | 1504.00 | NIST | |
| Inp | 1504.00 | NIST | |
| Inp | 1504.00 | NIST | |
| Inp | 1514.00 | NIST | |
| Inp | 1494.90 | NIST | |
| Inp | 1517.50 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | 1499.40 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1520.90 | NIST | |
| Inp | 1530.00 | NIST | |
| Inp | 1549.20 | NIST | |
| Inp | 1499.40 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1520.90 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | 1526.00 | NIST | |
| Inp | 1545.00 | NIST | |
| Inp | 1537.00 | NIST | |
| Inp | 1504.00 | NIST | |
| Inp | 1499.00 | NIST | |
| Inp | 1521.00 | NIST | |
| Inp | 1534.00 | NIST | |
| Inp | 1532.00 | NIST | |
| Inp | 1519.60 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1493.00 | NIST | |
| Inp | 1470.00 | NIST | |
| Inp | 1489.00 | NIST | |
| Inp | 1501.00 | NIST | |
| Inp | 1515.00 | NIST | |
| Inp | 1515.00 | NIST | |
| Inp | 1505.00 | NIST | |
| Inp | 1524.00 | NIST | |
| Inp | 1525.00 | NIST | |
| Inp | 1487.00 | NIST | |
| Inp | 260.30 | NIST | |
| Inp | 260.40 | NIST | |
| Inp | 252.13 | NIST | |
| Inp | 259.74 | NIST | |
| Inp | 258.72 | NIST | |
| Inp | 257.02 | NIST | |
| Inp | 259.70 | NIST | |
| Inp | 259.50 | NIST | |
| Inp | 258.80 | NIST | |
| Inp | 259.57 | NIST | |
| Inp | 257.12 | NIST | |
| Inp | 259.07 | NIST | |
| Inp | 259.75 | NIST | |
| Inp | 254.58 | NIST | |
| Inp | 252.50 | NIST | |
| Inp | 258.77 | NIST | |
| Inp | 257.17 | NIST | |
| Inp | 260.80 | NIST | |
| Inp | 259.63 | NIST | |
| Inp | 259.07 | NIST | |
| Inp | 259.63 | NIST | |
| Inp | 251.74 | NIST | |
| Inp | 258.70 | NIST | |
| Inp | 259.74 | NIST | |
| Inp | 263.31 | NIST | |
| Inp | 258.53 | NIST | |
| Inp | 261.30 | NIST | |
| Inp | 258.80 | NIST | |
| Inp | 259.10 | NIST | |
| Inp | 256.05 | NIST | |
| Inp | 257.17 | NIST | |
| Inp | 259.80 | NIST | |
| Inp | 1489.00 | NIST | |
| Inp | 1524.00 | NIST | |
| I | [256.99; 2308.00] |
|
|
| I | 2308.00 | NIST | |
| I | 2270.00 | NIST | |
| I | 256.99 | NIST | |
| I | 2308.00 | NIST | |
| S°solid,1 bar | 196.18 | J/mol×K | NIST |
| Tboil | [558.20; 560.20] | K |
|
| Tboil | 558.20 | K | NIST |
| Tboil | 560.20 | K | NIST |
| Tboil | 560.15 ± 0.60 | K | NIST |
| Tc | 824.00 ± 4.00 | K | NIST |
| Tfus | [355.66; 356.32] | K |
|
| Tfus | 356.32 | K | Aq. Solubility Prediction |
| Tfus | 355.66 | K | Solid-liquid equilibrium of some polycyclic aromatic hydrocarbons in wash oil |
| Ttriple | [355.31; 355.31] | K |
|
| Ttriple | 355.31 | K | KDB |
| Ttriple | 355.31 ± 0.02 | K | NIST |
| Vc | 0.496 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,solid | 199.01 | J/mol×K | 298.15 | NIST |
| ΔfusH | [17.60; 20.50] | kJ/mol | [354.70; 355.80] | |
| ΔfusH | 18.60 | kJ/mol | 354.70 | NIST |
| ΔfusH | 19.41 | kJ/mol | 355.10 | NIST |
| ΔfusH | 17.60 | kJ/mol | 355.20 | NIST |
| ΔfusH | 18.60 | kJ/mol | 355.70 | NIST |
| ΔfusH | 18.60 | kJ/mol | 355.70 | NIST |
| ΔfusH | 20.50 | kJ/mol | 355.80 | NIST |
| ΔsubH | [76.70; 85.60] | kJ/mol | [306.50; 323.50] | |
| ΔsubH | 82.10 ± 1.50 | kJ/mol | 306.50 | NIST |
| ΔsubH | 76.70 | kJ/mol | 322.50 | NIST |
| ΔsubH | 79.10 | kJ/mol | 323.00 | NIST |
| ΔsubH | 85.60 | kJ/mol | 323.50 | NIST |
| ΔvapH | [55.10; 66.20] | kJ/mol | [398.00; 481.00] | |
| ΔvapH | 66.20 | kJ/mol | 398.00 | NIST |
| ΔvapH | 66.20 | kJ/mol | 410.50 | NIST |
| ΔvapH | 55.10 | kJ/mol | 481.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.20; 202.65] | kPa | [355.65; 599.98] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45387e+01 | |||
| Coefficient B | -5.25976e+03 | |||
| Coefficient C | -2.99520e+01 | |||
| Temperature range, min. | 355.65 | |||
| Temperature range, max. | 599.98 | |||
| Pvap | 0.20 | kPa | 355.65 | Calculated Property |
| Pvap | 0.69 | kPa | 382.80 | Calculated Property |
| Pvap | 2.01 | kPa | 409.95 | Calculated Property |
| Pvap | 5.05 | kPa | 437.09 | Calculated Property |
| Pvap | 11.33 | kPa | 464.24 | Calculated Property |
| Pvap | 23.10 | kPa | 491.39 | Calculated Property |
| Pvap | 43.53 | kPa | 518.54 | Calculated Property |
| Pvap | 76.71 | kPa | 545.68 | Calculated Property |
| Pvap | 127.75 | kPa | 572.83 | Calculated Property |
| Pvap | 202.65 | kPa | 599.98 | Calculated Property |
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