| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4900 | Relay (1.0) Calculated Property | |
| PAff | 907.00 | kJ/mol | NIST |
| BasG | 875.10 | kJ/mol | NIST |
| ΔcH°solid | [-5314.00; -5285.90] | kJ/mol |
|
| ΔcH°solid | -5285.90 ± 5.30 | kJ/mol | NIST |
| ΔcH°solid | -5314.00 | kJ/mol | NIST |
| ΔcH°solid | -5308.49 | kJ/mol | NIST |
| ΔcH°solid | -5289.00 ± 5.40 | kJ/mol | NIST |
| ΔcH°solid | -5312.80 | kJ/mol | NIST |
| ΔfG° | 309.20 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 160.86 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | [87.00; 92.50] | kJ/mol |
|
| ΔfH°solid | 92.50 | kJ/mol | NIST |
| ΔfH°solid | 87.00 | kJ/mol | NIST |
| ΔfH°solid | 91.60 | kJ/mol | NIST |
| ΔfusH° | 17.52 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 88.10 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 73.30 ± 0.40 | kJ/mol | NIST |
| IE | [7.09; 7.48] | eV |
|
| IE | Outlier 7.09 | eV | NIST |
| IE | 7.30 ± 0.10 | eV | NIST |
| IE | 7.39 | eV | NIST |
| IE | 7.30 | eV | NIST |
| IE | 7.40 | eV | NIST |
| IE | 7.48 | eV | NIST |
| IE | 7.46 | eV | NIST |
| log10WS | [-1.92; -1.92] |
|
|
| log10WS | -1.92 | Aq. Solubility Prediction | |
| log10WS | -1.92 | Estimated Solubility | |
| logPoct/wat | 2.422 | Crippen Calculated Property | |
| McVol | 118.520 | ml/mol | McGowan Calculated Property |
| Pc | 4109.14 | kPa | Joback Calculated Property |
| Inp | [261.01; 1550.00] |
|
|
| Inp | 1531.00 | NIST | |
| Inp | 1495.10 | NIST | |
| Inp | 1550.00 | NIST | |
| Inp | 1515.70 | NIST | |
| Inp | 1531.00 | NIST | |
| Inp | 262.17 | NIST | |
| Inp | 262.20 | NIST | |
| Inp | 261.01 | NIST | |
| Inp | 262.55 | NIST | |
| Inp | 262.98 | NIST | |
| Inp | 1531.00 | NIST | |
| Inp | 1495.10 | NIST | |
| Inp | 1515.70 | NIST | |
| Inp | 262.17 | NIST | |
| Tboil | [512.10; 574.00] | K |
|
| Tboil | 574.00 | K | NIST |
| Tboil | 573.15 ± 2.00 | K | NIST |
| Tboil | 573.95 ± 1.50 | K | NIST |
| Tboil | 512.10 ± 27.77 | K | NIST |
| Tc | 848.87 | K | Relay (1.0) Calculated Property |
| Tfus | [321.88; 323.00] | K |
|
| Tfus | 321.88 | K | Aq. Solubility Prediction |
| Tfus | 323.00 | K | Vapor Pressures and Phase Transitions of a Series of the Aminonaphthalenes |
| Vc | 0.431 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [262.52; 325.62] | J/mol×K | [551.37; 800.58] | |
| Cp,gas | 262.52 | J/mol×K | 551.37 | Joback Calculated Property |
| Cp,gas | 275.40 | J/mol×K | 592.90 | Joback Calculated Property |
| Cp,gas | 287.23 | J/mol×K | 634.44 | Joback Calculated Property |
| Cp,gas | 298.07 | J/mol×K | 675.97 | Joback Calculated Property |
| Cp,gas | 308.03 | J/mol×K | 717.51 | Joback Calculated Property |
| Cp,gas | 317.19 | J/mol×K | 759.04 | Joback Calculated Property |
| Cp,gas | 325.62 | J/mol×K | 800.58 | Joback Calculated Property |
| ΔfusH | [15.53; 15.53] | kJ/mol | [323.20; 323.20] | |
| ΔfusH | 15.53 | kJ/mol | 323.20 | NIST |
| ΔfusH | 15.53 | kJ/mol | 323.20 | NIST |
| ΔvapH | 63.60 | kJ/mol | 475.50 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [426.99; 608.54] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.60427e+01 | |||
| Coefficient B | -6.10996e+03 | |||
| Coefficient C | -3.91810e+01 | |||
| Temperature range, min. | 426.99 | |||
| Temperature range, max. | 608.54 | |||
| Pvap | 1.33 | kPa | 426.99 | Calculated Property |
| Pvap | 2.91 | kPa | 447.16 | Calculated Property |
| Pvap | 5.88 | kPa | 467.33 | Calculated Property |
| Pvap | 11.18 | kPa | 487.51 | Calculated Property |
| Pvap | 20.11 | kPa | 507.68 | Calculated Property |
| Pvap | 34.45 | kPa | 527.85 | Calculated Property |
| Pvap | 56.55 | kPa | 548.02 | Calculated Property |
| Pvap | 89.39 | kPa | 568.20 | Calculated Property |
| Pvap | 136.62 | kPa | 588.37 | Calculated Property |
| Pvap | 202.63 | kPa | 608.54 | Calculated Property |
| Pvap | [0.13; 101.87] | kPa | [377.15; 574.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.09079e+01 | |||
| Coefficient B | -1.03031e+04 | |||
| Coefficient C | -7.77314e+00 | |||
| Coefficient D | 3.16272e-06 | |||
| Temperature range, min. | 377.15 | |||
| Temperature range, max. | 574.15 | |||
| Pvap | 0.13 | kPa | 377.15 | Calculated Property |
| Pvap | 0.38 | kPa | 399.04 | Calculated Property |
| Pvap | 1.02 | kPa | 420.93 | Calculated Property |
| Pvap | 2.45 | kPa | 442.82 | Calculated Property |
| Pvap | 5.38 | kPa | 464.71 | Calculated Property |
| Pvap | 10.88 | kPa | 486.59 | Calculated Property |
| Pvap | 20.61 | kPa | 508.48 | Calculated Property |
| Pvap | 36.82 | kPa | 530.37 | Calculated Property |
| Pvap | 62.59 | kPa | 552.26 | Calculated Property |
| Pvap | 101.87 | kPa | 574.15 | Calculated Property |
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