Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3570 | KDB | |
ΔcH°liquid | -2652.70 ± 1.50 | kJ/mol | NIST |
ΔfG° | 15.91 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -141.93 | kJ/mol | Joback Calculated Property |
ΔfH°liquid | -207.60 ± 1.50 | kJ/mol | NIST |
ΔfusH° | 13.95 | kJ/mol | Joback Calculated Property |
ΔvapH° | 43.85 ± 0.42 | kJ/mol | NIST |
IE | 10.71 ± 0.01 | eV | NIST |
log10WS | -1.69 | Crippen Calculated Property | |
logPoct/wat | 1.062 | Crippen Calculated Property | |
McVol | 84.640 | ml/mol | McGowan Calculated Property |
Pc | 3600.00 | kPa | KDB |
Inp | [774.00; 776.00] | ||
Inp | 776.00 | NIST | |
Inp | 776.00 | NIST | |
Inp | 774.00 | NIST | |
Inp | 776.00 | NIST | |
Tboil | [412.80; 412.90] | K | |
Tboil | 412.90 | K | KDB |
Tboil | 412.80 ± 0.70 | K | NIST |
Tc | 615.00 | K | KDB |
Tfus | [141.00; 412.65] | K | |
Tfus | 141.00 | K | KDB |
Tfus | 412.65 ± 0.07 | K | NIST |
Vc | 0.336 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [170.34; 220.79] | J/mol×K | [442.32; 654.36] | |
T(K) Ideal gas heat capacity (J/mol×K) 170 180 190 200 210 220 500 600 | ||||
Cp,gas | 170.34 | J/mol×K | 442.32 | Joback Calculated Property |
Cp,gas | 179.92 | J/mol×K | 477.66 | Joback Calculated Property |
Cp,gas | 189.01 | J/mol×K | 513.00 | Joback Calculated Property |
Cp,gas | 197.63 | J/mol×K | 548.34 | Joback Calculated Property |
Cp,gas | 205.79 | J/mol×K | 583.68 | Joback Calculated Property |
Cp,gas | 213.51 | J/mol×K | 619.02 | Joback Calculated Property |
Cp,gas | 220.79 | J/mol×K | 654.36 | Joback Calculated Property |
ΔvapH | [36.82; 40.30] | kJ/mol | [379.00; 412.90] | |
ΔvapH | 40.30 | kJ/mol | 379.00 | NIST |
ΔvapH | 36.82 | kJ/mol | 412.90 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [297.61; 440.60] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.51998e+01 | |||
Coefficient B | -4.19718e+03 | |||
Coefficient C | -1.61470e+01 | |||
Temperature range, min. | 297.61 | |||
Temperature range, max. | 440.60 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 297.61 | Calculated Property |
Pvap | 2.96 | kPa | 313.50 | Calculated Property |
Pvap | 6.05 | kPa | 329.39 | Calculated Property |
Pvap | 11.56 | kPa | 345.27 | Calculated Property |
Pvap | 20.79 | kPa | 361.16 | Calculated Property |
Pvap | 35.52 | kPa | 377.05 | Calculated Property |
Pvap | 58.00 | kPa | 392.94 | Calculated Property |
Pvap | 91.03 | kPa | 408.82 | Calculated Property |
Pvap | 137.94 | kPa | 424.71 | Calculated Property |
Pvap | 202.63 | kPa | 440.60 | Calculated Property |
Pvap | [11.96; 3138.32] | kPa | [348.15; 615.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 3.88020e+01 | |||
Coefficient B | -5.62246e+03 | |||
Coefficient C | -3.49067e+00 | |||
Coefficient D | 2.13481e-06 | |||
Temperature range, min. | 348.15 | |||
Temperature range, max. | 615.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 400 500 600 | ||||
Pvap | 11.96 | kPa | 348.15 | Calculated Property |
Pvap | 33.44 | kPa | 377.80 | Calculated Property |
Pvap | 79.73 | kPa | 407.45 | Calculated Property |
Pvap | 167.82 | kPa | 437.10 | Calculated Property |
Pvap | 319.94 | kPa | 466.75 | Calculated Property |
Pvap | 563.20 | kPa | 496.40 | Calculated Property |
Pvap | 929.12 | kPa | 526.05 | Calculated Property |
Pvap | 1453.29 | kPa | 555.70 | Calculated Property |
Pvap | 2175.17 | kPa | 585.35 | Calculated Property |
Pvap | 3138.32 | kPa | 615.00 | Calculated Property |
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