Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -88.04 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -158.05 | kJ/mol | Joback Calculated Property |
ΔfusH° | 17.41 | kJ/mol | Joback Calculated Property |
ΔvapH° | 60.01 | kJ/mol | Joback Calculated Property |
log10WS | 0.18 | Crippen Calculated Property | |
logPoct/wat | -1.026 | Crippen Calculated Property | |
McVol | 70.360 | ml/mol | McGowan Calculated Property |
Pc | 6318.86 | kPa | Joback Calculated Property |
Tboil | [511.00; 511.20] | K |
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Tboil | 511.00 | K | NIST |
Tboil | 511.20 | K | NIST |
Tc | 662.26 | K | Joback Calculated Property |
Tfus | 362.58 | K | Joback Calculated Property |
Vc | 0.260 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [139.52; 166.30] | J/mol×K | [484.28; 662.26] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 140 145 150 155 160 165 500 550 600 650 | ||||
Cp,gas | 139.52 | J/mol×K | 484.28 | Joback Calculated Property |
Cp,gas | 144.44 | J/mol×K | 513.94 | Joback Calculated Property |
Cp,gas | 149.17 | J/mol×K | 543.61 | Joback Calculated Property |
Cp,gas | 153.72 | J/mol×K | 573.27 | Joback Calculated Property |
Cp,gas | 158.09 | J/mol×K | 602.94 | Joback Calculated Property |
Cp,gas | 162.28 | J/mol×K | 632.60 | Joback Calculated Property |
Cp,gas | 166.30 | J/mol×K | 662.26 | Joback Calculated Property |
ΔvapH | [69.00; 81.50] | kJ/mol | [298.15; 469.00] | ![]() |
ΔvapH | 81.50 | kJ/mol | 298.15 | Vaporiz... |
ΔvapH | 69.00 | kJ/mol | 469.00 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [418.00; 418.20] | K | [2.00; 2.00] |
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Tboilr | 418.00 | K | 2.00 | NIST |
Tboilr | 418.20 | K | 2.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 203.79] | kPa | [409.99; 533.96] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.76213e+01 | |||
Coefficient B | -5.25702e+03 | |||
Coefficient C | -1.06705e+02 | |||
Temperature range, min. | 409.99 | |||
Temperature range, max. | 533.96 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 | ||||
Pvap | 1.33 | kPa | 409.99 | Calculated Property |
Pvap | 2.83 | kPa | 423.76 | Calculated Property |
Pvap | 5.65 | kPa | 437.54 | Calculated Property |
Pvap | 10.66 | kPa | 451.31 | Calculated Property |
Pvap | 19.15 | kPa | 465.09 | Calculated Property |
Pvap | 32.97 | kPa | 478.86 | Calculated Property |
Pvap | 54.58 | kPa | 492.64 | Calculated Property |
Pvap | 87.27 | kPa | 506.41 | Calculated Property |
Pvap | 135.26 | kPa | 520.19 | Calculated Property |
Pvap | 203.79 | kPa | 533.96 | Calculated Property |
Pvap | [3.14e-03; 5819.51] | kPa | [331.00; 695.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.73365e+02 | |||
Coefficient B | -1.75313e+04 | |||
Coefficient C | -2.18926e+01 | |||
Coefficient D | 7.85071e-06 | |||
Temperature range, min. | 331.00 | |||
Temperature range, max. | 695.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 400 500 600 700 | ||||
Pvap | 3.14e-03 | kPa | 331.00 | Calculated Property |
Pvap | 0.10 | kPa | 371.44 | Calculated Property |
Pvap | 1.38 | kPa | 411.89 | Calculated Property |
Pvap | 10.52 | kPa | 452.33 | Calculated Property |
Pvap | 52.43 | kPa | 492.78 | Calculated Property |
Pvap | 191.87 | kPa | 533.22 | Calculated Property |
Pvap | 558.74 | kPa | 573.67 | Calculated Property |
Pvap | 1371.94 | kPa | 614.11 | Calculated Property |
Pvap | 2964.35 | kPa | 654.56 | Calculated Property |
Pvap | 5819.51 | kPa | 695.00 | Calculated Property |
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