| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 816.40 | kJ/mol | NIST |
| BasG | 785.10 | kJ/mol | NIST |
| ΔcH°liquid | -3465.00 ± 0.71 | kJ/mol | NIST |
| ΔfH°gas | -108.70 ± 0.88 | kJ/mol | NIST |
| ΔfH°liquid | -140.50 ± 0.88 | kJ/mol | NIST |
| ΔfusH° | 2.74 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [30.80; 31.80] | kJ/mol |
|
| ΔvapH° | 30.93 | kJ/mol | NIST |
| ΔvapH° | 30.80 | kJ/mol | NIST |
| ΔvapH° | 30.90 ± 0.08 | kJ/mol | NIST |
| ΔvapH° | 31.80 | kJ/mol | NIST |
| IE | 9.03 | eV | NIST |
| logPoct/wat | 1.715 | Crippen Calculated Property | |
| McVol | 83.570 | ml/mol | McGowan Calculated Property |
| Pc | 4333.96 | kPa | Joback Calculated Property |
| Inp | [574.00; 617.00] |
|
|
| Inp | 584.00 | NIST | |
| Inp | 605.50 | NIST | |
| Inp | Outlier 617.00 | NIST | |
| Inp | 599.20 | NIST | |
| Inp | 602.50 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 586.00 | NIST | |
| Inp | Outlier 574.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 599.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 584.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 602.00 | NIST | |
| I | [779.00; 779.00] |
|
|
| I | 779.00 | NIST | |
| I | 779.00 | NIST | |
| S°liquid | 246.44 | J/mol×K | NIST |
| Tboil | [334.50; 339.00] | K |
|
| Tboil | 334.75 | K | KDB |
| Tboil | 337.40 | K | NIST |
| Tboil | 337.00 | K | NIST |
| Tboil | 337.40 | K | NIST |
| Tboil | 339.00 ± 2.00 | K | NIST |
| Tboil | 336.00 ± 3.00 | K | NIST |
| Tboil | 334.50 ± 0.35 | K | NIST |
| Tboil | 337.90 ± 0.60 | K | NIST |
| Tboil | 337.00 ± 2.00 | K | NIST |
| Tc | 530.10 | K | NIST |
| Tfus | [273.97; 274.41] | K |
|
| Tfus | 274.41 | K | KDB |
| Tfus | 273.97 ± 0.20 | K | NIST |
| Ttriple | 274.42 ± 0.02 | K | NIST |
| Vc | 0.297 | m3/kmol | Relay (1.0) Calculated Property |
Cheméo can also estimate 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 | [135.13; 187.65] | J/mol×K | [350.55; 555.05] | |
| Cp,gas | 135.13 | J/mol×K | 350.55 | Joback Calculated Property |
| Cp,gas | 145.28 | J/mol×K | 384.63 | Joback Calculated Property |
| Cp,gas | 154.84 | J/mol×K | 418.72 | Joback Calculated Property |
| Cp,gas | 163.83 | J/mol×K | 452.80 | Joback Calculated Property |
| Cp,gas | 172.28 | J/mol×K | 486.88 | Joback Calculated Property |
| Cp,gas | 180.21 | J/mol×K | 520.97 | Joback Calculated Property |
| Cp,gas | 187.65 | J/mol×K | 555.05 | Joback Calculated Property |
| Cp,liquid | 175.06 | J/mol×K | 298.15 | NIST |
| ΔfusH | [0.65; 4.07] | kJ/mol | [151.60; 274.40] | |
| ΔfusH | 4.07 | kJ/mol | 151.60 | NIST |
| ΔfusH | 0.65 | kJ/mol | 157.00 | NIST |
| ΔfusH | 0.97 | kJ/mol | 199.40 | NIST |
| ΔfusH | 2.48 | kJ/mol | 274.40 | NIST |
| ΔfusH | 2.48 | kJ/mol | 274.40 | NIST |
| ΔvapH | [28.45; 30.90] | kJ/mol | [284.00; 337.40] | |
| ΔvapH | 30.10 | kJ/mol | 284.00 | NIST |
| ΔvapH | 30.90 | kJ/mol | 333.00 | NIST |
| ΔvapH | 28.45 | kJ/mol | 337.40 | NIST |
| n0 | [1.42000; 1.42000] | [293.10; 298.15] | ||
| n0 | 1.42000 | 293.10 | Isothermal Binary Vapor-Liquid Equilibrium for 2-Methylpropane and n-Butane with 1,2-Ethanedithiol and 2-Methyl-2-propanethiol | |
| n0 | 1.42000 | 298.15 | Vapor Liquid Equilibrium for Methoxymethane + Thiophene, + Diethylsulfide, + 2-Methyl-2-propanethiol and 1-Hexene, + 1-Propanethiol | |
| ΔfusS | [4.13; 26.83] | J/mol×K | [151.60; 274.40] | |
| ΔfusS | 26.83 | J/mol×K | 151.60 | NIST |
| ΔfusS | 4.13 | J/mol×K | 157.00 | NIST |
| ΔfusS | 4.87 | J/mol×K | 199.40 | NIST |
| ΔfusS | 9.04 | J/mol×K | 274.40 | NIST |
Find more compounds similar to 2-Propanethiol, 2-methyl-.
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