Property | Value | Unit | Source |
---|---|---|---|
PAff | 686.60 | kJ/mol | NIST |
BasG | 656.20 | kJ/mol | NIST |
ΔfG° | -1328.06 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -1456.92 | kJ/mol | Joback Calculated Property |
ΔfusH° | 7.74 | kJ/mol | Joback Calculated Property |
ΔvapH° | [41.58; 41.60] | kJ/mol | |
ΔvapH° | 41.58 | kJ/mol | NIST |
ΔvapH° | 41.60 | kJ/mol | NIST |
IE | [11.94; 12.23] | eV | |
IE | 11.94 | eV | NIST |
IE | 12.23 | eV | NIST |
log10WS | -1.78 | Crippen Calculated Property | |
logPoct/wat | 1.472 | Crippen Calculated Property | |
McVol | 69.620 | ml/mol | McGowan Calculated Property |
Pc | 3727.11 | kPa | Joback Calculated Property |
Tboil | [331.00; 332.20] | K | |
Tboil | 331.00 | K | NIST |
Tboil | 332.20 | K | NIST |
Tc | 485.00 | K | Joback Calculated Property |
Tfus | 177.77 | K | Joback Calculated Property |
Vc | 0.302 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [152.66; 186.58] | J/mol×K | [348.94; 485.00] | |
T(K) Ideal gas heat capacity (J/mol×K) 150 155 160 165 170 175 180 185 350 400 450 | ||||
Cp,gas | 152.66 | J/mol×K | 348.94 | Joback Calculated Property |
Cp,gas | 159.24 | J/mol×K | 371.62 | Joback Calculated Property |
Cp,gas | 165.43 | J/mol×K | 394.29 | Joback Calculated Property |
Cp,gas | 171.24 | J/mol×K | 416.97 | Joback Calculated Property |
Cp,gas | 176.70 | J/mol×K | 439.65 | Joback Calculated Property |
Cp,gas | 181.81 | J/mol×K | 462.32 | Joback Calculated Property |
Cp,gas | 186.58 | J/mol×K | 485.00 | Joback Calculated Property |
ΔvapH | [40.20; 47.30] | kJ/mol | [284.50; 312.00] | |
ΔvapH | 47.30 | kJ/mol | 284.50 | NIST |
ΔvapH | 40.20 | kJ/mol | 312.00 | NIST |
ρl | 1604.84 | kg/m3 | 298.15 | Liquid ... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.62] | kPa | [255.86; 349.50] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.72410e+01 | |||
Coefficient B | -3.76991e+03 | |||
Coefficient C | -3.34880e+01 | |||
Temperature range, min. | 255.86 | |||
Temperature range, max. | 349.50 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 255.86 | Calculated Property |
Pvap | 2.85 | kPa | 266.26 | Calculated Property |
Pvap | 5.69 | kPa | 276.67 | Calculated Property |
Pvap | 10.75 | kPa | 287.07 | Calculated Property |
Pvap | 19.31 | kPa | 297.48 | Calculated Property |
Pvap | 33.18 | kPa | 307.88 | Calculated Property |
Pvap | 54.81 | kPa | 318.29 | Calculated Property |
Pvap | 87.39 | kPa | 328.69 | Calculated Property |
Pvap | 134.99 | kPa | 339.10 | Calculated Property |
Pvap | 202.62 | kPa | 349.50 | Calculated Property |
Find more compounds similar to 2-Propanol, 1,1,1,3,3,3-hexafluoro-.
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