Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -1978.62 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -2052.31 | kJ/mol | Joback Calculated Property |
ΔfusH° | 6.23 | kJ/mol | Joback Calculated Property |
ΔvapH° | [25.60; 26.30] | kJ/mol |
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ΔvapH° | 25.60 | kJ/mol | NIST |
ΔvapH° | 26.30 | kJ/mol | NIST |
IE | 11.70 | eV | NIST |
log10WS | -3.38 | Crippen Calculated Property | |
logPoct/wat | 3.176 | Crippen Calculated Property | |
McVol | 88.150 | ml/mol | McGowan Calculated Property |
Pc | 2844.44 | kPa | Joback Calculated Property |
Tboil | 293.70 ± 1.00 | K | NIST |
Tc | 438.50 | K | Joback Calculated Property |
Tfus | [283.45; 343.00] | K |
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Tfus | 283.45 | K | KDB |
Tfus | 343.00 ± 5.00 | K | NIST |
Ttriple | 283.55 ± 0.30 | K | NIST |
Vc | 0.422 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [172.94; 240.58] | J/mol×K | [304.30; 438.50] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 170 180 190 200 210 220 230 240 350 400 | ||||
Cp,gas | 172.94 | J/mol×K | 304.30 | Joback Calculated Property |
Cp,gas | 187.60 | J/mol×K | 326.67 | Joback Calculated Property |
Cp,gas | 200.77 | J/mol×K | 349.03 | Joback Calculated Property |
Cp,gas | 212.55 | J/mol×K | 371.40 | Joback Calculated Property |
Cp,gas | 223.05 | J/mol×K | 393.77 | Joback Calculated Property |
Cp,gas | 232.35 | J/mol×K | 416.13 | Joback Calculated Property |
Cp,gas | 240.58 | J/mol×K | 438.50 | Joback Calculated Property |
ΔfusH | [2.99; 5.00] | kJ/mol | [118.20; 238.50] | ![]() |
ΔfusH | 5.00 | kJ/mol | 118.20 | NIST |
ΔfusH | 2.99 | kJ/mol | 238.50 | NIST |
ΔfusH | 3.00 | kJ/mol | 238.50 | NIST |
ΔsubH | [32.10; 38.20] | kJ/mol | [115.00; 255.00] | ![]() |
ΔsubH | 38.20 | kJ/mol | 115.00 | NIST |
ΔsubH | 32.10 | kJ/mol | 255.00 | NIST |
ΔvapH | 27.00 | kJ/mol | 291.00 | NIST |
ΔfusS | [12.60; 41.90] | J/mol×K | [118.20; 238.50] | ![]() |
ΔfusS | 41.90 | J/mol×K | 118.20 | NIST |
ΔfusS | 12.60 | J/mol×K | 238.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [82.18; 305.57] | kPa | [290.15; 329.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 5.79210e+01 | |||
Coefficient B | -4.87335e+03 | |||
Coefficient C | -6.56816e+00 | |||
Coefficient D | 6.27180e-06 | |||
Temperature range, min. | 290.15 | |||
Temperature range, max. | 329.15 | |||
T(K) Vapor pressure (kPa) 100 150 200 250 300 300 320 | ||||
Pvap | 82.18 | kPa | 290.15 | Calculated Property |
Pvap | 96.99 | kPa | 294.48 | Calculated Property |
Pvap | 113.84 | kPa | 298.82 | Calculated Property |
Pvap | 132.91 | kPa | 303.15 | Calculated Property |
Pvap | 154.41 | kPa | 307.48 | Calculated Property |
Pvap | 178.54 | kPa | 311.82 | Calculated Property |
Pvap | 205.50 | kPa | 316.15 | Calculated Property |
Pvap | 235.51 | kPa | 320.48 | Calculated Property |
Pvap | 268.79 | kPa | 324.82 | Calculated Property |
Pvap | 305.57 | kPa | 329.15 | Calculated Property |
Find more compounds similar to Cyclopentane, decafluoro-.
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