| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 1.2567 | ChemSep v8.3 pure component data Compiled value | |
| μ | 0.68 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -503.50 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -829.70 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 19.05 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 85.34 | kJ/mol | Relay (1.0) Calculated Property |
| logPoct/wat | 0.170 | Crippen Calculated Property | |
| McVol | 161.150 | ml/mol | McGowan Calculated Property |
| Pc | 2540.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 2.05e-08 | kPa | ChemSep v8.3 pure component data Compiled value |
| Tboil | 554.01 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 677.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 228.15 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 228.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 6.50 | ChemSep v8.3 pure component data Compiled value | |
| URi | 7.62 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.596 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2689410 | ChemSep v8.3 pure component data Compiled value |
Cheméo can also estimate Ionization energy, 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,liquid | 440.60 | J/mol×K | 298.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [218.73; 630.84] | J/mol×K | [255.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.17986e+02 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 6.57332e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 218.73 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 318.75 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 397.45 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 457.34 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 503.57 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 540.05 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 569.45 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 593.60 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 613.76 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 630.84 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [14.8007161; 0.0001903] | Pa×s | [228.15; 473.90] |
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 | -1.90222e+01 | |||
| Coefficient B | 4.95470e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 228.15 | |||
| Temperature range, max. | 473.90 | |||
| η | 14.8007161 | Pa×s | 228.15 | Calculated Property |
| η | 1.4526198 | Pa×s | 255.46 | Calculated Property |
| η | 0.2232167 | Pa×s | 282.76 | Calculated Property |
| η | 0.0477054 | Pa×s | 310.07 | Calculated Property |
| η | 0.0130885 | Pa×s | 337.37 | Calculated Property |
| η | 0.0043583 | Pa×s | 364.68 | Calculated Property |
| η | 0.0016916 | Pa×s | 391.98 | Calculated Property |
| η | 0.0007427 | Pa×s | 419.29 | Calculated Property |
| η | 0.0003606 | Pa×s | 446.59 | Calculated Property |
| η | 0.0001903 | Pa×s | 473.90 | Calculated Property |
Find more compounds similar to 2-Propanol, 1,1'-[(1-methyl-1,2-ethanediyl)bis(oxy)]bis-.
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