Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3650 | KDB | |
PAff | 670.40 | kJ/mol | NIST |
BasG | 639.70 | kJ/mol | NIST |
EA | 0.44 | eV | NIST |
ΔfG° | -1317.72 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -1411.99 | kJ/mol | Joback Calculated Property |
ΔfusH° | 8.78 | kJ/mol | Joback Calculated Property |
ΔvapH° | 21.52 | kJ/mol | Joback Calculated Property |
IE | [11.44; 12.09] | eV | |
IE | 11.57 ± 0.13 | eV | NIST |
IE | 11.44 | eV | NIST |
IE | 11.68 | eV | NIST |
IE | 12.09 ± 0.02 | eV | NIST |
log10WS | -1.68 | Crippen Calculated Property | |
logPoct/wat | 1.680 | Crippen Calculated Property | |
McVol | 65.320 | ml/mol | McGowan Calculated Property |
Pc | [2832.00; 2840.00] | kPa | |
Pc | 2840.00 | kPa | KDB |
Pc | 2832.00 ± 3.44 | kPa | NIST |
ρc | 504.71 ± 5.05 | kg/m3 | NIST |
S°liquid | 286.60 | J/mol×K | NIST |
Tboil | [245.20; 247.20] | K | |
Tboil | 245.70 | K | KDB |
Tboil | 247.20 | K | NIST |
Tboil | 245.70 | K | NIST |
Tboil | 245.20 | K | NIST |
Tc | [357.14; 357.14] | K | |
Tc | 357.14 | K | KDB |
Tc | 357.14 ± 0.20 | K | NIST |
Tfus | 148.00 | K | KDB |
Ttriple | 147.70 ± 0.02 | K | NIST |
Vc | 0.329 | m3/kmol | KDB |
Zc | 0.3146580 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [127.89; 162.11] | J/mol×K | [311.07; 454.82] | |
T(K) Ideal gas heat capacity (J/mol×K) 130 140 150 160 350 400 450 | ||||
Cp,gas | 127.89 | J/mol×K | 311.07 | Joback Calculated Property |
Cp,gas | 134.60 | J/mol×K | 335.03 | Joback Calculated Property |
Cp,gas | 140.89 | J/mol×K | 358.99 | Joback Calculated Property |
Cp,gas | 146.77 | J/mol×K | 382.94 | Joback Calculated Property |
Cp,gas | 152.25 | J/mol×K | 406.90 | Joback Calculated Property |
Cp,gas | 157.36 | J/mol×K | 430.86 | Joback Calculated Property |
Cp,gas | 162.11 | J/mol×K | 454.82 | Joback Calculated Property |
Cp,liquid | 181.29 | J/mol×K | 245.00 | NIST |
ΔfusH | [8.38; 8.38] | kJ/mol | [147.70; 147.70] | |
ΔfusH | 8.38 | kJ/mol | 147.70 | NIST |
ΔfusH | 8.38 | kJ/mol | 147.70 | NIST |
ΔvapH | 21.61 | kJ/mol | 245.87 | NIST |
ΔfusS | 56.75 | J/mol×K | 147.70 | NIST |
ΔvapS | 87.91 | J/mol×K | 245.87 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 2837.03] | kPa | [180.83; 357.14] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42172e+01 | |||
Coefficient B | -2.00849e+03 | |||
Coefficient C | -3.66370e+01 | |||
Temperature range, min. | 180.83 | |||
Temperature range, max. | 357.14 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 250 300 350 | ||||
Pvap | 1.33 | kPa | 180.83 | Calculated Property |
Pvap | 7.06 | kPa | 200.42 | Calculated Property |
Pvap | 26.16 | kPa | 220.01 | Calculated Property |
Pvap | 75.29 | kPa | 239.60 | Calculated Property |
Pvap | 179.90 | kPa | 259.19 | Calculated Property |
Pvap | 373.36 | kPa | 278.78 | Calculated Property |
Pvap | 694.63 | kPa | 298.37 | Calculated Property |
Pvap | 1185.30 | kPa | 317.96 | Calculated Property |
Pvap | 1886.62 | kPa | 337.55 | Calculated Property |
Pvap | 2837.03 | kPa | 357.14 | Calculated Property |
Find more compounds similar to 2-Propanone, 1,1,1,3,3,3-hexafluoro-.
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