| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -6226.52 | kJ/mol | NIST |
| ΔfH°gas | -140.33 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 9.53 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 50.16 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [9.14; 9.35] | eV |
|
| IE | 9.14 | eV | NIST |
| IE | 9.35 | eV | NIST |
| log10WS | -5.19 | Estimated Solubility | |
| logPoct/wat | 3.367 | Crippen Calculated Property | |
| McVol | 130.040 | ml/mol | McGowan Calculated Property |
| Pc | 2080.00 ± 151.99 | kPa | NIST |
| Inp | [173.01; 1089.00] |
|
|
| Inp | 1042.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | Outlier 173.01 | NIST | |
| Inp | Outlier 173.31 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | Outlier 173.01 | NIST | |
| S°liquid | 265.01 | J/mol×K | NIST |
| Tboil | [445.00; 465.00] | K |
|
| Tboil | 464.25 | K | Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K |
| Tboil | 463.20 | K | NIST |
| Tboil | 465.00 ± 5.00 | K | NIST |
| Tboil | 465.00 ± 2.00 | K | NIST |
| Tboil | Outlier 445.00 ± 10.00 | K | NIST |
| Tboil | 461.00 ± 6.00 | K | NIST |
| Tc | 645.00 ± 2.00 | K | NIST |
| Tfus | 149.00 ± 2.50 | K | NIST |
Cheméo can also estimate 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 | [151.17; 501.83] | 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 | -1.27170e+02 | |||
| Coefficient B | 1.21720e+00 | |||
| Coefficient C | -7.75000e-04 | |||
| Coefficient D | 1.86800e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 151.17 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 214.72 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 270.75 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 319.84 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 362.59 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 399.58 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 431.41 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 458.67 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 481.95 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 501.83 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0524483; 0.0004195] | Pa×s | [149.00; 451.50] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.01549e+01 | |||
| Coefficient B | 1.07384e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 149.00 | |||
| Temperature range, max. | 451.50 | |||
| η | 0.0524483 | Pa×s | 149.00 | Calculated Property |
| η | 0.0139199 | Pa×s | 182.61 | Calculated Property |
| η | 0.0055802 | Pa×s | 216.22 | Calculated Property |
| η | 0.0028607 | Pa×s | 249.83 | Calculated Property |
| η | 0.0017184 | Pa×s | 283.44 | Calculated Property |
| η | 0.0011500 | Pa×s | 317.06 | Calculated Property |
| η | 0.0008312 | Pa×s | 350.67 | Calculated Property |
| η | 0.0006359 | Pa×s | 384.28 | Calculated Property |
| η | 0.0005079 | Pa×s | 417.89 | Calculated Property |
| η | 0.0004195 | Pa×s | 451.50 | Calculated Property |
Find more compounds similar to Naphthalene, decahydro-.
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