| Property | Value | Unit | Source |
|---|---|---|---|
| ΔcH°liquid | -4127.20 ± 0.63 | kJ/mol | NIST |
| ΔfH°gas | -121.00 ± 0.75 | kJ/mol | NIST |
| ΔfH°liquid | -156.90 ± 0.75 | kJ/mol | NIST |
| ΔfusH° | 5.42 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [34.20; 35.90] | kJ/mol |
|
| ΔvapH° | 35.90 | kJ/mol | NIST |
| ΔvapH° | Outlier 34.20 | kJ/mol | NIST |
| ΔvapH° | 35.90 | kJ/mol | NIST |
| ΔvapH° | 35.80 | kJ/mol | NIST |
| ΔvapH° | 35.90 | kJ/mol | NIST |
| ΔvapH° | 35.80 | kJ/mol | NIST |
| ΔvapH° | 35.90 | kJ/mol | NIST |
| IE | 8.38 ± 0.05 | eV | NIST |
| logPoct/wat | 2.148 | Crippen Calculated Property | |
| McVol | 97.660 | ml/mol | McGowan Calculated Property |
| Inp | [710.00; 725.00] |
|
|
| Inp | 724.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | Outlier 710.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 724.00 | NIST | |
| S°liquid | 276.14 | J/mol×K | NIST |
| Tboil | [372.05; 375.00] | K |
|
| Tboil | 374.70 | K | NIST |
| Tboil | 372.10 | K | NIST |
| Tboil | 372.05 ± 0.20 | K | NIST |
| Tboil | 372.10 ± 0.30 | K | NIST |
| Tboil | 372.20 ± 0.50 | K | NIST |
| Tboil | 375.00 ± 4.00 | K | NIST |
| Tc | 569.80 | K | NIST |
| Tfus | [190.85; 190.90] | K |
|
| Tfus | 190.85 ± 0.20 | K | NIST |
| Tfus | 190.90 ± 0.30 | K | NIST |
| Ttriple | [184.86; 190.84] | K |
|
| Ttriple | 190.84 ± 0.02 | K | NIST |
| Ttriple | 184.86 ± 0.06 | K | NIST |
| Ttriple | 190.84 ± 0.02 | K | NIST |
| Ttriple | 184.86 ± 0.06 | K | NIST |
Cheméo can also estimate 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 | [171.13; 231.97] | J/mol×K | [379.35; 582.94] | |
| Cp,gas | 171.13 | J/mol×K | 379.35 | Joback Calculated Property |
| Cp,gas | 182.72 | J/mol×K | 413.28 | Joback Calculated Property |
| Cp,gas | 193.70 | J/mol×K | 447.21 | Joback Calculated Property |
| Cp,gas | 204.10 | J/mol×K | 481.15 | Joback Calculated Property |
| Cp,gas | 213.93 | J/mol×K | 515.08 | Joback Calculated Property |
| Cp,gas | 223.21 | J/mol×K | 549.01 | Joback Calculated Property |
| Cp,gas | 231.97 | J/mol×K | 582.94 | Joback Calculated Property |
| Cp,liquid | 199.95 | J/mol×K | 298.15 | NIST |
| ΔfusH | [8.41; 8.41] | kJ/mol | [190.80; 190.84] | |
| ΔfusH | 8.41 | kJ/mol | 190.80 | NIST |
| ΔfusH | 8.41 | kJ/mol | 190.80 | NIST |
| ΔfusH | 8.41 | kJ/mol | 190.84 | NIST |
| ΔfusH | 8.41 | kJ/mol | 190.84 | NIST |
| ΔvapH | [31.47; 36.50] | kJ/mol | [336.50; 372.10] | |
| ΔvapH | 36.50 | kJ/mol | 336.50 | NIST |
| ΔvapH | 35.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 31.47 | kJ/mol | 372.10 | NIST |
| ΔfusS | [44.09; 44.09] | J/mol×K | [190.84; 190.84] | |
| ΔfusS | 44.09 | J/mol×K | 190.84 | NIST |
| ΔfusS | 44.09 | J/mol×K | 190.84 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [269.89; 399.18] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.38760e+01 | |||
| Coefficient B | -2.99505e+03 | |||
| Coefficient C | -4.94790e+01 | |||
| Temperature range, min. | 269.89 | |||
| Temperature range, max. | 399.18 | |||
| Pvap | 1.33 | kPa | 269.89 | Calculated Property |
| Pvap | 3.06 | kPa | 284.26 | Calculated Property |
| Pvap | 6.39 | kPa | 298.62 | Calculated Property |
| Pvap | 12.30 | kPa | 312.99 | Calculated Property |
| Pvap | 22.14 | kPa | 327.35 | Calculated Property |
| Pvap | 37.61 | kPa | 341.72 | Calculated Property |
| Pvap | 60.80 | kPa | 356.08 | Calculated Property |
| Pvap | 94.14 | kPa | 370.45 | Calculated Property |
| Pvap | 140.40 | kPa | 384.81 | Calculated Property |
| Pvap | 202.64 | kPa | 399.18 | Calculated Property |
| Pvap | [9.28; 269.57] | kPa | [306.15; 410.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.81918e+01 | |||
| Coefficient B | -6.79559e+03 | |||
| Coefficient C | -9.50787e+00 | |||
| Coefficient D | 7.00157e-06 | |||
| Temperature range, min. | 306.15 | |||
| Temperature range, max. | 410.15 | |||
| Pvap | 9.28 | kPa | 306.15 | Calculated Property |
| Pvap | 15.38 | kPa | 317.71 | Calculated Property |
| Pvap | 24.44 | kPa | 329.26 | Calculated Property |
| Pvap | 37.42 | kPa | 340.82 | Calculated Property |
| Pvap | 55.44 | kPa | 352.37 | Calculated Property |
| Pvap | 79.74 | kPa | 363.93 | Calculated Property |
| Pvap | 111.73 | kPa | 375.48 | Calculated Property |
| Pvap | 152.92 | kPa | 387.04 | Calculated Property |
| Pvap | 204.95 | kPa | 398.59 | Calculated Property |
| Pvap | 269.57 | kPa | 410.15 | Calculated Property |
Find more compounds similar to Propane, 2-methyl-2-(methylthio)-.
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