| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | [-3434.00; -3388.60] | kJ/mol |
|
| ΔcH°solid | -3406.00 ± 3.00 | kJ/mol | NIST |
| ΔcH°solid | -3388.60 ± 3.00 | kJ/mol | NIST |
| ΔcH°solid | -3407.00 | kJ/mol | NIST |
| ΔcH°solid | -3404.50 ± 2.10 | kJ/mol | NIST |
| ΔcH°solid | -3401.80 ± 3.40 | kJ/mol | NIST |
| ΔcH°solid | -3402.30 ± 3.40 | kJ/mol | NIST |
| ΔcH°solid | -3419.18 | kJ/mol | NIST |
| ΔcH°solid | Outlier -3434.00 | kJ/mol | NIST |
| ΔfH°gas | 24.10 ± 3.50 | kJ/mol | NIST |
| ΔfH°solid | [-80.50; -49.96] | kJ/mol |
|
| ΔfH°solid | -63.20 ± 5.00 | kJ/mol | NIST |
| ΔfH°solid | -80.50 ± 3.10 | kJ/mol | NIST |
| ΔfH°solid | -49.96 | kJ/mol | NIST |
| ΔfusH° | 40.84 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [104.60; 118.00] | kJ/mol |
|
| ΔsubH° | 113.20 ± 1.50 | kJ/mol | NIST |
| ΔsubH° | 105.00 ± 2.00 | kJ/mol | NIST |
| ΔsubH° | 104.60 ± 1.70 | kJ/mol | NIST |
| ΔsubH° | 118.00 | kJ/mol | NIST |
| ΔvapH° | 87.00 ± 1.90 | kJ/mol | NIST |
| IE | 10.59 ± 0.04 | eV | NIST |
| log10WS | [-3.22; -3.22] |
|
|
| log10WS | -3.22 | Aq. Solubility Prediction | |
| log10WS | -3.22 | Estimated Solubility | |
| logPoct/wat | 1.720 | Crippen Calculated Property | |
| McVol | 137.990 | ml/mol | McGowan Calculated Property |
| Inp | [287.66; 1717.67] |
|
|
| Inp | 1707.07 | NIST | |
| Inp | 1714.08 | NIST | |
| Inp | 1693.00 | NIST | |
| Inp | 1704.00 | NIST | |
| Inp | 1708.67 | NIST | |
| Inp | 1717.67 | NIST | |
| Inp | 1704.00 | NIST | |
| Inp | 1709.00 | NIST | |
| Inp | Outlier 287.66 | NIST | |
| Inp | 1708.67 | NIST | |
| Inp | 1704.00 | NIST | |
| Tboil | 544.75 | K | Relay (1.0) Calculated Property |
| Tfus | [352.00; 355.10] | K |
|
| Tfus | 353.55 | K | HP-DSC study of energetic materials. Part I. Overview of pressure influence on thermal behavior |
| Tfus | 353.20 | K | Aq. Solubility Prediction |
| Tfus | 355.10 ± 0.10 | K | NIST |
| Tfus | 352.00 ± 0.10 | K | NIST |
| Tfus | 354.00 ± 2.00 | K | NIST |
| Tfus | 354.30 ± 0.50 | K | NIST |
| Tfus | 353.42 ± 0.30 | K | NIST |
| Tfus | 353.42 ± 0.30 | K | NIST |
| Ttriple | 353.95 | K | Thermo-analytical study of a melt cast composition based on cis -1,3,4,6-tetranitrooctahydroimidazo-[4,5 d]imidazole (BCHMX)/trinitrotoluene (TNT) compared with traditional compositions |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [371.64; 404.39] | J/mol×K | [856.70; 1146.44] | |
| Cp,gas | 371.64 | J/mol×K | 856.70 | Joback Calculated Property |
| Cp,gas | 379.23 | J/mol×K | 904.99 | Joback Calculated Property |
| Cp,gas | 385.89 | J/mol×K | 953.28 | Joback Calculated Property |
| Cp,gas | 391.69 | J/mol×K | 1001.57 | Joback Calculated Property |
| Cp,gas | 396.66 | J/mol×K | 1049.86 | Joback Calculated Property |
| Cp,gas | 400.88 | J/mol×K | 1098.15 | Joback Calculated Property |
| Cp,gas | 404.39 | J/mol×K | 1146.44 | Joback Calculated Property |
| Cp,solid | [243.30; 311.70] | J/mol×K | [293.00; 298.00] | |
| Cp,solid | 311.70 | J/mol×K | 293.00 | NIST |
| Cp,solid | 243.30 | J/mol×K | 298.00 | NIST |
| ΔfusH | [23.40; 23.43] | kJ/mol | [352.20; 352.20] | |
| ΔfusH | 23.43 | kJ/mol | 352.20 | NIST |
| ΔfusH | 23.40 | kJ/mol | 352.20 | NIST |
| ΔfusH | 23.43 | kJ/mol | 352.20 | NIST |
| ΔsubH | [99.00; 118.40] | kJ/mol | [313.50; 338.00] | |
| ΔsubH | 99.00 ± 2.00 | kJ/mol | 313.50 | NIST |
| ΔsubH | 112.40 | kJ/mol | 323.00 | NIST |
| ΔsubH | 103.30 ± 2.50 | kJ/mol | 338.00 | NIST |
| ΔsubH | 118.40 ± 4.20 | kJ/mol | 338.00 | NIST |
| ΔvapH | [93.70; 113.70] | kJ/mol | [343.15; 438.00] | |
| ΔvapH | 113.70 | kJ/mol | 343.15 | Comment on Studies on Thermodynamic Properties of FOX-7 and Its Five Closed-Loop Derivatives |
| ΔvapH | 93.70 | kJ/mol | 438.00 | NIST |
| Psub | [1.30e-05; 2.71e-04] | kPa | [313.15; 338.15] | |
| Psub | 1.30e-05 | kPa | 313.15 | Triacetone triperoxide thermogravimetric study of vapor pressure and enthalpy of sublimation in 303 338 K temperature range |
| Psub | 2.20e-05 | kPa | 318.15 | Triacetone triperoxide thermogravimetric study of vapor pressure and enthalpy of sublimation in 303 338 K temperature range |
| Psub | 4.00e-05 | kPa | 323.15 | Triacetone triperoxide thermogravimetric study of vapor pressure and enthalpy of sublimation in 303 338 K temperature range |
| Psub | 7.30e-05 | kPa | 328.15 | Triacetone triperoxide thermogravimetric study of vapor pressure and enthalpy of sublimation in 303 338 K temperature range |
| Psub | 1.37e-04 | kPa | 333.15 | Triacetone triperoxide thermogravimetric study of vapor pressure and enthalpy of sublimation in 303 338 K temperature range |
| Psub | 2.71e-04 | kPa | 338.15 | Triacetone triperoxide thermogravimetric study of vapor pressure and enthalpy of sublimation in 303 338 K temperature range |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [464.70; 688.99] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.29612e+01 | |||
| Coefficient B | -4.32833e+03 | |||
| Coefficient C | -1.23172e+02 | |||
| Temperature range, min. | 464.70 | |||
| Temperature range, max. | 688.99 | |||
| Pvap | 1.33 | kPa | 464.70 | Calculated Property |
| Pvap | 3.16 | kPa | 489.62 | Calculated Property |
| Pvap | 6.70 | kPa | 514.54 | Calculated Property |
| Pvap | 12.99 | kPa | 539.46 | Calculated Property |
| Pvap | 23.36 | kPa | 564.38 | Calculated Property |
| Pvap | 39.47 | kPa | 589.31 | Calculated Property |
| Pvap | 63.23 | kPa | 614.23 | Calculated Property |
| Pvap | 96.79 | kPa | 639.15 | Calculated Property |
| Pvap | 142.46 | kPa | 664.07 | Calculated Property |
| Pvap | 202.65 | kPa | 688.99 | Calculated Property |
| Pvap | [1.52e-04; 9.03] | kPa | [337.15; 523.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 5.87826e+02 | |||
| Coefficient B | -3.70745e+04 | |||
| Coefficient C | -8.47236e+01 | |||
| Coefficient D | 5.70032e-05 | |||
| Temperature range, min. | 337.15 | |||
| Temperature range, max. | 523.15 | |||
| Pvap | 1.52e-04 | kPa | 337.15 | Calculated Property |
| Pvap | 1.27e-03 | kPa | 357.82 | Calculated Property |
| Pvap | 7.47e-03 | kPa | 378.48 | Calculated Property |
| Pvap | 0.03 | kPa | 399.15 | Calculated Property |
| Pvap | 0.12 | kPa | 419.82 | Calculated Property |
| Pvap | 0.34 | kPa | 440.48 | Calculated Property |
| Pvap | 0.89 | kPa | 461.15 | Calculated Property |
| Pvap | 2.07 | kPa | 481.82 | Calculated Property |
| Pvap | 4.45 | kPa | 502.48 | Calculated Property |
| Pvap | 9.03 | kPa | 523.15 | Calculated Property |
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