Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -465.70 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -557.29 | kJ/mol | Joback Calculated Property |
ΔfusH° | 9.06 | kJ/mol | Joback Calculated Property |
ΔvapH° | 33.36 | kJ/mol | Joback Calculated Property |
log10WS | -3.18 | Crippen Calculated Property | |
logPoct/wat | 3.188 | Crippen Calculated Property | |
McVol | 91.540 | ml/mol | McGowan Calculated Property |
Pc | 3857.88 | kPa | Joback Calculated Property |
Inp | [702.00; 785.00] |
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Inp | 702.00 | NIST | |
Inp | 702.00 | NIST | |
Inp | 785.00 | NIST | |
Inp | 785.00 | NIST | |
Tboil | [364.60; 364.70] | K |
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Tboil | 364.60 | K | NIST |
Tboil | 364.70 | K | NIST |
Tc | 592.71 | K | Joback Calculated Property |
Tfus | 314.20 ± 0.20 | K | NIST |
Vc | 0.357 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [138.37; 161.61] | J/mol×K | [386.96; 592.71] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 140 145 150 155 160 400 450 500 550 | ||||
Cp,gas | 138.37 | J/mol×K | 386.96 | Joback Calculated Property |
Cp,gas | 143.76 | J/mol×K | 421.25 | Joback Calculated Property |
Cp,gas | 148.47 | J/mol×K | 455.54 | Joback Calculated Property |
Cp,gas | 152.57 | J/mol×K | 489.84 | Joback Calculated Property |
Cp,gas | 156.09 | J/mol×K | 524.13 | Joback Calculated Property |
Cp,gas | 159.09 | J/mol×K | 558.42 | Joback Calculated Property |
Cp,gas | 161.61 | J/mol×K | 592.71 | Joback Calculated Property |
ΔfusH | 3.99 | kJ/mol | 314.20 | NIST |
ΔfusS | 12.70 | J/mol×K | 314.20 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [270.27; 389.05] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.34757e+01 | |||
Coefficient B | -2.54565e+03 | |||
Coefficient C | -7.72440e+01 | |||
Temperature range, min. | 270.27 | |||
Temperature range, max. | 389.05 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 270.27 | Calculated Property |
Pvap | 3.10 | kPa | 283.47 | Calculated Property |
Pvap | 6.51 | kPa | 296.67 | Calculated Property |
Pvap | 12.58 | kPa | 309.86 | Calculated Property |
Pvap | 22.64 | kPa | 323.06 | Calculated Property |
Pvap | 38.38 | kPa | 336.26 | Calculated Property |
Pvap | 61.80 | kPa | 349.46 | Calculated Property |
Pvap | 95.24 | kPa | 362.65 | Calculated Property |
Pvap | 141.26 | kPa | 375.85 | Calculated Property |
Pvap | 202.64 | kPa | 389.05 | Calculated Property |
Pvap | [1.34; 48.88] | kPa | [262.15; 343.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.41240e+01 | |||
Coefficient B | -6.96532e+03 | |||
Coefficient C | -1.22355e+01 | |||
Coefficient D | 1.27074e-05 | |||
Temperature range, min. | 262.15 | |||
Temperature range, max. | 343.15 | |||
T(K) Vapor pressure (kPa) 0 10 20 30 40 50 280 300 320 340 | ||||
Pvap | 1.34 | kPa | 262.15 | Calculated Property |
Pvap | 2.27 | kPa | 271.15 | Calculated Property |
Pvap | 3.70 | kPa | 280.15 | Calculated Property |
Pvap | 5.81 | kPa | 289.15 | Calculated Property |
Pvap | 8.84 | kPa | 298.15 | Calculated Property |
Pvap | 13.05 | kPa | 307.15 | Calculated Property |
Pvap | 18.77 | kPa | 316.15 | Calculated Property |
Pvap | 26.37 | kPa | 325.15 | Calculated Property |
Pvap | 36.25 | kPa | 334.15 | Calculated Property |
Pvap | 48.88 | kPa | 343.15 | Calculated Property |
Find more compounds similar to Ethane, 1,1,1,2-tetrachloro-2,2-difluoro-.
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