| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°solid | [-6033.40; -6024.50] | kJ/mol |
|
| ΔcH°solid | -6029.00 ± 4.00 | kJ/mol | NIST |
| ΔcH°solid | -6033.10 ± 2.80 | kJ/mol | NIST |
| ΔcH°solid | -6033.40 ± 3.30 | kJ/mol | NIST |
| ΔcH°solid | -6024.50 ± 0.71 | kJ/mol | NIST |
| ΔfH°gas | [-138.70; -129.00] | kJ/mol |
|
| ΔfH°gas | -134.40 ± 2.30 | kJ/mol | NIST |
| ΔfH°gas | -138.70 | kJ/mol | NIST |
| ΔfH°gas | -133.60 ± 2.50 | kJ/mol | NIST |
| ΔfH°gas | -129.00 ± 4.00 | kJ/mol | NIST |
| ΔfH°gas | -137.90 ± 0.79 | kJ/mol | NIST |
| ΔfH°solid | [-197.20; -188.40] | kJ/mol |
|
| ΔfH°solid | -192.50 ± 0.40 | kJ/mol | NIST |
| ΔfH°solid | -193.80 | kJ/mol | NIST |
| ΔfH°solid | -188.70 ± 2.80 | kJ/mol | NIST |
| ΔfH°solid | -188.40 ± 3.30 | kJ/mol | NIST |
| ΔfH°solid | -197.20 ± 0.79 | kJ/mol | NIST |
| ΔfusH° | 3.09 | kJ/mol | Redetermination of the thermodynamic properties of the solid solid transition of adamantane by adiabatic calorimetry to investigate the suitability as a reference material for low-temperature DSC-calibration |
| ΔsubH° | [52.60; 62.30] | kJ/mol |
|
| ΔsubH° | 59.10 | kJ/mol | NIST |
| ΔsubH° | Outlier 52.60 | kJ/mol | NIST |
| ΔsubH° | 58.50 ± 0.70 | kJ/mol | NIST |
| ΔsubH° | 58.45 | kJ/mol | NIST |
| ΔsubH° | 59.66 | kJ/mol | NIST |
| ΔsubH° | 58.10 | kJ/mol | NIST |
| ΔsubH° | 58.60 | kJ/mol | NIST |
| ΔsubH° | 60.00 ± 1.00 | kJ/mol | NIST |
| ΔsubH° | 55.10 | kJ/mol | NIST |
| ΔsubH° | 60.50 ± 1.30 | kJ/mol | NIST |
| ΔsubH° | 59.40 | kJ/mol | NIST |
| ΔsubH° | 54.80 | kJ/mol | NIST |
| ΔsubH° | 59.30 ± 0.20 | kJ/mol | NIST |
| ΔsubH° | 59.30 | kJ/mol | NIST |
| ΔsubH° | 59.50 | kJ/mol | NIST |
| ΔsubH° | 59.30 ± 0.16 | kJ/mol | NIST |
| ΔsubH° | 59.60 | kJ/mol | NIST |
| ΔsubH° | 62.30 | kJ/mol | NIST |
| ΔvapH° | [48.20; 51.70] | kJ/mol |
|
| ΔvapH° | 48.20 | kJ/mol | NIST |
| ΔvapH° | 51.70 | kJ/mol | NIST |
| IE | [9.10; 9.75] | eV |
|
| IE | 9.25 ± 0.04 | eV | NIST |
| IE | 9.20 | eV | NIST |
| IE | 9.25 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | 9.10 ± 0.05 | eV | NIST |
| IE | 9.30 ± 0.10 | eV | NIST |
| IE | 9.31 ± 0.01 | eV | NIST |
| IE | 9.30 ± 0.01 | eV | NIST |
| IE | 9.22 | eV | NIST |
| IE | 9.25 | eV | NIST |
| IE | 9.75 | eV | NIST |
| IE | 9.28 | eV | NIST |
| IE | 9.75 ± 0.02 | eV | NIST |
| IE | 9.75 | eV | NIST |
| IE | 9.55 | eV | NIST |
| logPoct/wat | 2.833 | Crippen Calculated Property | |
| McVol | 119.180 | ml/mol | McGowan Calculated Property |
| Inp | [1076.00; 1153.00] |
|
|
| Inp | 1121.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1136.90 | NIST | |
| Inp | 1149.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1149.00 | NIST | |
| Inp | 1135.30 | NIST | |
| Inp | 1095.20 | NIST | |
| Inp | 1113.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1116.00 | NIST | |
| Inp | 1117.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1128.00 | NIST | |
| Inp | 1131.00 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1114.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1132.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | Outlier 1153.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | Outlier 1076.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1118.00 | NIST | |
| Inp | 1144.00 | NIST | |
| Inp | 1123.00 | NIST | |
| I | [1320.00; 1400.00] |
|
|
| I | 1400.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1320.00 | NIST | |
| I | 1339.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1400.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1400.00 | NIST | |
| S°solid,1 bar | [195.83; 195.83] | J/mol×K |
|
| S°solid,1 bar | 195.83 | J/mol×K | NIST |
| S°solid,1 bar | 195.83 | J/mol×K | NIST |
| Tboil | 471.37 | K | Relay (1.0) Calculated Property |
| Tfus | [542.15; 552.00] | K |
|
| Tfus | 552.00 ± 3.00 | K | NIST |
| Tfus | 542.15 ± 1.00 | K | NIST |
Cheméo can also estimate Critical Temperature, Critical Pressure, Critical Volume, Standard Gibbs free energy of formation, Acentric Factor, Log10 of Water solubility in mol/l 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 | [272.66; 379.04] | J/mol×K | [448.22; 661.92] | |
| Cp,gas | 272.66 | J/mol×K | 448.22 | Joback Calculated Property |
| Cp,gas | 293.72 | J/mol×K | 483.84 | Joback Calculated Property |
| Cp,gas | 313.32 | J/mol×K | 519.45 | Joback Calculated Property |
| Cp,gas | 331.56 | J/mol×K | 555.07 | Joback Calculated Property |
| Cp,gas | 348.53 | J/mol×K | 590.68 | Joback Calculated Property |
| Cp,gas | 364.33 | J/mol×K | 626.30 | Joback Calculated Property |
| Cp,gas | 379.04 | J/mol×K | 661.92 | Joback Calculated Property |
| Cp,solid | [189.74; 189.74] | J/mol×K | [298.15; 298.15] | |
| Cp,solid | 189.74 | J/mol×K | 298.15 | NIST |
| Cp,solid | 189.74 | J/mol×K | 298.15 | NIST |
| η | [0.0006121; 0.0011056] | Pa×s | [248.52; 448.22] | |
| η | 0.0006121 | Pa×s | 248.52 | Joback Calculated Property |
| η | 0.0007159 | Pa×s | 281.80 | Joback Calculated Property |
| η | 0.0008101 | Pa×s | 315.09 | Joback Calculated Property |
| η | 0.0008954 | Pa×s | 348.37 | Joback Calculated Property |
| η | 0.0009724 | Pa×s | 381.65 | Joback Calculated Property |
| η | 0.0010422 | Pa×s | 414.94 | Joback Calculated Property |
| η | 0.0011056 | Pa×s | 448.22 | Joback Calculated Property |
| ΔfusH | [10.90; 13.80] | kJ/mol | [541.00; 543.20] | |
| ΔfusH | 10.90 | kJ/mol | 541.00 | NIST |
| ΔfusH | 10.90 | kJ/mol | 541.20 | NIST |
| ΔfusH | 13.80 | kJ/mol | 543.20 | NIST |
| ΔsubH | [53.60; 59.70] | kJ/mol | [308.00; 413.00] | |
| ΔsubH | 58.30 | kJ/mol | 308.00 | NIST |
| ΔsubH | 59.70 | kJ/mol | 323.00 | NIST |
| ΔsubH | 59.70 ± 0.80 | kJ/mol | 323.00 | NIST |
| ΔsubH | 59.30 ± 0.20 | kJ/mol | 323.00 | NIST |
| ΔsubH | 58.60 ± 0.60 | kJ/mol | 333.00 | NIST |
| ΔsubH | 53.60 | kJ/mol | 339.00 | NIST |
| ΔsubH | 55.30 | kJ/mol | 350.50 | NIST |
| ΔsubH | 59.50 | kJ/mol | 360.50 | NIST |
| ΔsubH | 54.30 | kJ/mol | 413.00 | NIST |
| ΔvapH | 48.50 | kJ/mol | 298.15 | The vaporization enthalpy and vapor pressures of liquid adamantane, diamantane and alpha- and beta-cedrene by correlation gas chromatography |
| ρl | [880.32; 935.74] | kg/m3 | [293.15; 363.15] | |
| ρl | 935.74 | kg/m3 | 293.15 | Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes |
| ρl | 931.86 | kg/m3 | 298.15 | Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes |
| ρl | 927.95 | kg/m3 | 303.15 | Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes |
| ρl | 920.13 | kg/m3 | 313.15 | Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes |
| ρl | 912.14 | kg/m3 | 323.15 | Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes |
| ρl | 904.25 | kg/m3 | 333.15 | Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes |
| ρl | 896.32 | kg/m3 | 343.15 | Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes |
| ρl | 888.34 | kg/m3 | 353.15 | Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes |
| ρl | 880.32 | kg/m3 | 363.15 | Density, Viscosity, Surface Tension, and Refractive Index for Binary Mixtures of 1,3-Dimethyladamantane with Four C10 Alkanes |
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