| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4812 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -6426.20 | kJ/mol | NIST |
| ΔcH°solid | [-6436.71; -6409.50] | kJ/mol |
|
| ΔcH°solid | -6424.20 ± 1.40 | kJ/mol | NIST |
| ΔcH°solid | -6436.71 | kJ/mol | NIST |
| ΔcH°solid | -6411.10 | kJ/mol | NIST |
| ΔcH°solid | -6409.50 ± 5.40 | kJ/mol | NIST |
| ΔcH°solid | -6429.72 | kJ/mol | NIST |
| ΔcH°solid | -6424.50 | kJ/mol | NIST |
| ΔcH°solid | -6431.60 | kJ/mol | NIST |
| ΔfG° | 364.37 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 202.00 | kJ/mol | NIST |
| ΔfH°liquid | 132.00 | kJ/mol | NIST |
| ΔfH°solid | [109.00; 142.50] | kJ/mol |
|
| ΔfH°solid | 130.00 ± 1.50 | kJ/mol | NIST |
| ΔfH°solid | 142.50 | kJ/mol | NIST |
| ΔfH°solid | 117.40 ± 2.10 | kJ/mol | NIST |
| ΔfH°solid | 131.00 | kJ/mol | NIST |
| ΔfH°solid | 109.00 | kJ/mol | NIST |
| ΔfusH° | 19.68 | kJ/mol | Measurement and prediction of (solid + liquid) equilibria of gun powder's and propellant's stabilizers mixtures |
| ΔsubH° | 110.00 | kJ/mol | NIST |
| ΔvapH° | [55.23; 70.00] | kJ/mol |
|
| ΔvapH° | 55.23 | kJ/mol | NIST |
| ΔvapH° | 69.90 | kJ/mol | NIST |
| ΔvapH° | 70.00 | kJ/mol | NIST |
| IE | [7.14; 7.44] | eV |
|
| IE | 7.19 ± 0.05 | eV | NIST |
| IE | 7.18 ± 0.01 | eV | NIST |
| IE | 7.14 ± 0.03 | eV | NIST |
| IE | 7.25 ± 0.03 | eV | NIST |
| IE | 7.44 | eV | NIST |
| log10WS | [-3.51; -3.50] |
|
|
| log10WS | -3.51 | Aq. Solubility Prediction | |
| log10WS | -3.50 | Estimated Solubility | |
| logPoct/wat | 3.430 | Crippen Calculated Property | |
| McVol | 142.400 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 3 | KDB | |
| Pc | 8409.97 ± 405.30 | kPa | NIST |
| Inp | [274.57; 1637.00] |
|
|
| Inp | 1619.00 | NIST | |
| Inp | 1567.00 | NIST | |
| Inp | 1621.00 | NIST | |
| Inp | 1625.00 | NIST | |
| Inp | 1622.00 | NIST | |
| Inp | 1637.00 | NIST | |
| Inp | 1588.00 | NIST | |
| Inp | 1602.00 | NIST | |
| Inp | 1637.00 | NIST | |
| Inp | 1568.00 | NIST | |
| Inp | 1617.00 | NIST | |
| Inp | 1634.00 | NIST | |
| Inp | 1575.00 | NIST | |
| Inp | 1575.00 | NIST | |
| Inp | 1601.00 | NIST | |
| Inp | 274.57 | NIST | |
| Inp | 276.00 | NIST | |
| Inp | 279.32 | NIST | |
| Inp | 275.74 | NIST | |
| Inp | 279.27 | NIST | |
| Inp | 1634.00 | NIST | |
| Inp | 1602.00 | NIST | |
| I | [2517.00; 2521.00] |
|
|
| I | 2517.00 | NIST | |
| I | 2517.00 | NIST | |
| I | 2521.00 | NIST | |
| I | 2521.00 | NIST | |
| I | 2517.00 | NIST | |
| I | 2521.00 | NIST | |
| Tboil | [575.15; 582.15] | K |
|
| Tboil | 575.15 | K | KDB |
| Tboil | 575.20 | K | NIST |
| Tboil | 582.15 ± 2.00 | K | NIST |
| Tc | 931.15 ± 3.00 | K | NIST |
| Tfus | [323.85; 327.40] | K |
|
| Tfus | 325.60 | K | Experimental and modeling studies of binary organic eutectic systems to be used as stabilizers for nitrate esters-based energetic materials |
| Tfus | 326.65 | K | DSC measurement and prediction of phase diagrams for binary mixtures of energetic materials' stabilizers |
| Tfus | 325.85 | K | KDB |
| Tfus | 326.23 | K | Aq. Solubility Prediction |
| Tfus | 326.40 ± 0.20 | K | NIST |
| Tfus | 326.40 ± 0.50 | K | NIST |
| Tfus | 326.30 ± 0.20 | K | NIST |
| Tfus | 326.15 ± 0.30 | K | NIST |
| Tfus | 326.25 ± 0.40 | K | NIST |
| Tfus | 326.15 ± 0.50 | K | NIST |
| Tfus | 327.40 ± 3.00 | K | NIST |
| Tfus | 326.35 ± 0.50 | K | NIST |
| Tfus | 326.09 ± 0.25 | K | NIST |
| Tfus | 326.15 ± 0.15 | K | NIST |
| Tfus | 326.15 ± 1.00 | K | NIST |
| Tfus | 327.15 ± 2.00 | K | NIST |
| Tfus | 325.95 ± 0.50 | K | NIST |
| Tfus | Outlier 324.05 ± 0.30 | K | NIST |
| Tfus | Outlier 323.85 ± 0.30 | K | NIST |
| Tfus | 327.15 ± 2.00 | K | NIST |
| Tfus | 326.15 ± 1.50 | K | NIST |
| Tfus | 325.15 ± 0.60 | K | NIST |
| Tfus | 326.08 ± 1.00 | K | NIST |
| Tfus | 326.00 ± 1.50 | K | NIST |
| Tfus | 327.15 ± 1.50 | K | NIST |
| Vc | 0.515 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [428.54; 610.47] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53095e+01 | |||
| Coefficient B | -5.43887e+03 | |||
| Coefficient C | -6.64740e+01 | |||
| Temperature range, min. | 428.54 | |||
| Temperature range, max. | 610.47 | |||
| Pvap | 1.33 | kPa | 428.54 | Calculated Property |
| Pvap | 2.95 | kPa | 448.75 | Calculated Property |
| Pvap | 6.03 | kPa | 468.97 | Calculated Property |
| Pvap | 11.51 | kPa | 489.18 | Calculated Property |
| Pvap | 20.70 | kPa | 509.40 | Calculated Property |
| Pvap | 35.37 | kPa | 529.61 | Calculated Property |
| Pvap | 57.81 | kPa | 549.83 | Calculated Property |
| Pvap | 90.81 | kPa | 570.04 | Calculated Property |
| Pvap | 137.78 | kPa | 590.26 | Calculated Property |
| Pvap | 202.66 | kPa | 610.47 | Calculated Property |
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