| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | -6528.50 ± 1.50 | kJ/mol | NIST |
| ΔfH°gas | -118.70 ± 3.30 | kJ/mol | NIST |
| ΔfH°solid | -225.00 ± 1.60 | kJ/mol | NIST |
| ΔfusH° | 26.30 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 106.00 ± 2.00 | kJ/mol | NIST |
| IE | [9.16; 9.70] | eV |
|
| IE | 9.16 | eV | NIST |
| IE | 9.20 | eV | NIST |
| IE | 9.16 ± 0.03 | eV | NIST |
| IE | 9.70 | eV | NIST |
| IE | 9.46 | eV | NIST |
| IE | 9.37 | eV | NIST |
| log10WS | -3.64 | Aq. Solubility Prediction | |
| logPoct/wat | 2.519 | Crippen Calculated Property | |
| McVol | 160.510 | ml/mol | McGowan Calculated Property |
| Tboil | 619.77 | K | Relay (1.0) Calculated Property |
| Tfus | [394.00; 433.50] | K |
|
| Tfus | 398.20 | K | Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements |
| Tfus | 401.40 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 401.40 | K | Aq. Solubility Prediction |
| Tfus | 397.00 ± 2.00 | K | NIST |
| Tfus | Outlier 433.50 ± 1.50 | K | NIST |
| Tfus | 400.00 ± 3.00 | K | NIST |
| Tfus | 397.00 ± 3.00 | K | NIST |
| Tfus | 398.00 ± 2.00 | K | NIST |
| Tfus | 394.00 ± 2.00 | K | NIST |
| Tfus | 401.00 ± 2.00 | K | NIST |
| Tfus | 399.00 ± 3.00 | K | NIST |
| Tfus | 396.00 ± 4.00 | K | NIST |
| Tfus | 397.00 ± 3.00 | K | NIST |
| Tfus | 397.00 ± 3.00 | K | NIST |
| Tfus | 399.00 ± 3.00 | K | NIST |
| Tfus | 399.00 ± 3.00 | K | NIST |
| Tfus | 401.40 ± 1.00 | K | NIST |
| Tfus | 400.35 ± 0.60 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Enthalpy of vaporization at standard conditions, 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,solid | 244.30 | J/mol×K | 298.50 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [191.55; 470.60] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -4.25900e+01 | |||
| Coefficient B | 1.01959e+00 | |||
| Coefficient C | -6.25800e-04 | |||
| Coefficient D | 1.19400e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 191.55 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 245.08 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 292.10 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 332.99 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 368.11 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 397.86 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 422.61 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 442.73 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 458.60 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 470.60 | J/mol×K | 1000.00 | Calculated Property |
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