| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfH°gas | -49.04 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 23.51 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [120.20; 122.00] | kJ/mol |
|
| ΔsubH° | 122.00 ± 3.00 | kJ/mol | NIST |
| ΔsubH° | 120.20 ± 3.00 | kJ/mol | NIST |
| ΔvapH° | 80.18 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 7.98 ± 0.05 | eV | NIST |
| log10WS | [-1.46; -1.46] |
|
|
| log10WS | -1.46 | Aq. Solubility Prediction | |
| log10WS | -1.46 | Estimated Solubility | |
| logPoct/wat | 0.490 | Crippen Calculated Property | |
| McVol | 113.320 | ml/mol | McGowan Calculated Property |
| Tboil | 508.96 | K | Relay (1.0) Calculated Property |
| Tfus | [350.60; 350.65] | K |
|
| Tfus | 350.65 | K | Aq. Solubility Prediction |
| Tfus | 350.60 ± 0.10 | K | NIST |
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 | [235.39; 289.86] | J/mol×K | [484.18; 686.47] | |
| Cp,gas | 235.39 | J/mol×K | 484.18 | Joback Calculated Property |
| Cp,gas | 245.94 | J/mol×K | 517.90 | Joback Calculated Property |
| Cp,gas | 255.85 | J/mol×K | 551.61 | Joback Calculated Property |
| Cp,gas | 265.16 | J/mol×K | 585.33 | Joback Calculated Property |
| Cp,gas | 273.91 | J/mol×K | 619.04 | Joback Calculated Property |
| Cp,gas | 282.13 | J/mol×K | 652.76 | Joback Calculated Property |
| Cp,gas | 289.86 | J/mol×K | 686.47 | Joback Calculated Property |
| ΔfusH | 17.14 | kJ/mol | 350.50 | NIST |
| ΔvapH | 101.00 ± 3.00 | kJ/mol | 367.50 | NIST |
| ρs | 1120.00 | kg/m3 | 293.00 | Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems |
Find more compounds similar to Thiourea, N,N'-diethyl-.
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