Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2380 | KDB | |
PAff | 699.40 | kJ/mol | NIST |
BasG | 666.90 | kJ/mol | NIST |
ΔcH°gas | -976.50 ± 8.40 | kJ/mol | NIST |
ΔfG° | -546.80 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -474.00 ± 8.40 | kJ/mol | NIST |
ΔfusH° | 9.07 | kJ/mol | Joback Calculated Property |
ΔvapH° | 17.63 | kJ/mol | Joback Calculated Property |
IE | [10.14; 10.62] | eV |
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IE | 10.14 | eV | NIST |
IE | 10.14 ± 0.02 | eV | NIST |
IE | 10.14 | eV | NIST |
IE | 10.14 | eV | NIST |
IE | 10.62 ± 0.02 | eV | NIST |
IE | 10.54 ± 0.02 | eV | NIST |
IE | 10.53 | eV | NIST |
log10WS | -1.56 | Crippen Calculated Property | |
logPoct/wat | 1.694 | Crippen Calculated Property | |
McVol | 40.050 | ml/mol | McGowan Calculated Property |
Pc | 4520.00 | kPa | KDB |
Inp | [254.00; 254.00] |
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|
Inp | 254.00 | NIST | |
Inp | 254.00 | NIST | |
Tboil | [221.00; 222.00] | K |
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Tboil | 221.00 | K | KDB |
Tboil | 222.00 | K | NIST |
Tc | 347.20 | K | KDB |
Tfus | 95.00 | K | KDB |
Vc | 0.182 | m3/kmol | KDB |
Zc | 0.2857490 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [54.74; 73.55] | J/mol×K | [247.01; 388.06] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 55 60 65 70 75 250 300 350 | ||||
Cp,gas | 54.74 | J/mol×K | 247.01 | Joback Calculated Property |
Cp,gas | 58.29 | J/mol×K | 270.52 | Joback Calculated Property |
Cp,gas | 61.66 | J/mol×K | 294.03 | Joback Calculated Property |
Cp,gas | 64.87 | J/mol×K | 317.54 | Joback Calculated Property |
Cp,gas | 67.92 | J/mol×K | 341.05 | Joback Calculated Property |
Cp,gas | 70.81 | J/mol×K | 364.55 | Joback Calculated Property |
Cp,gas | 73.55 | J/mol×K | 388.06 | Joback Calculated Property |
Pvap | [1230.30; 4543.40] | kPa | [277.67; 331.73] | ![]() |
T(K) Vapor pressure (kPa) 1000 1500 2000 2500 3000 3500 4000 4500 280 300 320 | ||||
Pvap | 1230.30 | kPa | 277.67 | Measure... |
Pvap | 1231.00 | kPa | 277.67 | Measure... |
Pvap | 1312.50 | kPa | 279.97 | Measure... |
Pvap | 1313.70 | kPa | 279.98 | Measure... |
Pvap | 1476.60 | kPa | 284.12 | Measure... |
Pvap | 1476.80 | kPa | 284.12 | Measure... |
Pvap | 1477.70 | kPa | 284.15 | Measure... |
Pvap | 1516.10 | kPa | 285.10 | Measure... |
Pvap | 1517.00 | kPa | 285.12 | Measure... |
Pvap | 1727.20 | kPa | 289.99 | Measure... |
Pvap | 1727.40 | kPa | 289.99 | Measure... |
Pvap | 1963.00 | kPa | 294.97 | Measure... |
Pvap | 1963.10 | kPa | 294.97 | Measure... |
Pvap | 2222.10 | kPa | 300.00 | Measure... |
Pvap | 2388.20 | kPa | 303.00 | Measure... |
Pvap | 2504.70 | kPa | 305.00 | Measure... |
Pvap | 2687.80 | kPa | 308.00 | Measure... |
Pvap | 2815.30 | kPa | 310.00 | Measure... |
Pvap | 3015.40 | kPa | 313.00 | Measure... |
Pvap | 3155.00 | kPa | 315.00 | Measure... |
Pvap | 3373.30 | kPa | 318.00 | Measure... |
Pvap | 3525.70 | kPa | 320.00 | Measure... |
Pvap | 3764.50 | kPa | 323.00 | Measure... |
Pvap | 3931.30 | kPa | 325.00 | Measure... |
Pvap | 4194.20 | kPa | 328.00 | Measure... |
Pvap | 4377.70 | kPa | 330.00 | Measure... |
Pvap | 4543.40 | kPa | 331.73 | Measure... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [143.04; 239.70] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.78527e+01 | |||
Coefficient B | -4.23849e+03 | |||
Coefficient C | 9.82630e+01 | |||
Temperature range, min. | 143.04 | |||
Temperature range, max. | 239.70 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 150 200 | ||||
Pvap | 1.33 | kPa | 143.04 | Calculated Property |
Pvap | 2.82 | kPa | 153.78 | Calculated Property |
Pvap | 5.60 | kPa | 164.52 | Calculated Property |
Pvap | 10.56 | kPa | 175.26 | Calculated Property |
Pvap | 18.96 | kPa | 186.00 | Calculated Property |
Pvap | 32.63 | kPa | 196.74 | Calculated Property |
Pvap | 54.04 | kPa | 207.48 | Calculated Property |
Pvap | 86.51 | kPa | 218.22 | Calculated Property |
Pvap | 134.27 | kPa | 228.96 | Calculated Property |
Pvap | 202.64 | kPa | 239.70 | Calculated Property |
Pvap | [14.15; 215.01] | kPa | [180.15; 244.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.65399e+01 | |||
Coefficient B | -3.90796e+03 | |||
Coefficient C | -1.21425e+01 | |||
Coefficient D | 2.67399e-05 | |||
Temperature range, min. | 180.15 | |||
Temperature range, max. | 244.15 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 180 200 220 240 | ||||
Pvap | 14.15 | kPa | 180.15 | Calculated Property |
Pvap | 21.60 | kPa | 187.26 | Calculated Property |
Pvap | 31.70 | kPa | 194.37 | Calculated Property |
Pvap | 44.92 | kPa | 201.48 | Calculated Property |
Pvap | 61.75 | kPa | 208.59 | Calculated Property |
Pvap | 82.62 | kPa | 215.71 | Calculated Property |
Pvap | 107.99 | kPa | 222.82 | Calculated Property |
Pvap | 138.25 | kPa | 229.93 | Calculated Property |
Pvap | 173.80 | kPa | 237.04 | Calculated Property |
Pvap | 215.01 | kPa | 244.15 | Calculated Property |
Find more compounds similar to Ethene, trifluoro-.
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