Property | Value | Unit | Source |
---|---|---|---|
PAff | 851.80 | kJ/mol | NIST |
BasG | 820.00 | kJ/mol | NIST |
EA | 0.37 ± 0.02 | eV | NIST |
ΔfG° | 19.74 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -68.97 | kJ/mol | Joback Calculated Property |
ΔfusH° | 12.42 | kJ/mol | Joback Calculated Property |
ΔvapH° | 43.06 | kJ/mol | Joback Calculated Property |
IE | [9.33; 9.34] | eV |
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IE | 9.33 ± 0.05 | eV | NIST |
IE | 9.34 | eV | NIST |
log10WS | -2.19 | Crippen Calculated Property | |
logPoct/wat | 1.808 | Crippen Calculated Property | |
McVol | 101.390 | ml/mol | McGowan Calculated Property |
Pc | 3925.85 | kPa | Joback Calculated Property |
Inp | [174.20; 1096.00] |
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|
Inp | 1073.90 | NIST | |
Inp | 1083.60 | NIST | |
Inp | 1074.60 | NIST | |
Inp | 1096.00 | NIST | |
Inp | 1089.00 | NIST | |
Inp | 1093.00 | NIST | |
Inp | 1079.00 | NIST | |
Inp | 1079.00 | NIST | |
Inp | 1079.00 | NIST | |
Inp | 1079.00 | NIST | |
Inp | 1076.10 | NIST | |
Inp | 1079.00 | NIST | |
Inp | 1072.00 | NIST | |
Inp | 1042.00 | NIST | |
Inp | 1080.00 | NIST | |
Inp | 1079.00 | NIST | |
Inp | 1047.00 | NIST | |
Inp | 1046.00 | NIST | |
Inp | 1074.00 | NIST | |
Inp | 1079.00 | NIST | |
Inp | 1080.00 | NIST | |
Inp | 1075.00 | NIST | |
Inp | 1075.00 | NIST | |
Inp | 1067.00 | NIST | |
Inp | 1081.00 | NIST | |
Inp | 1079.00 | NIST | |
Inp | 1067.00 | NIST | |
Inp | Outlier 174.20 | NIST | |
Inp | 1072.00 | NIST | |
Inp | 1046.00 | NIST | |
Inp | 1073.90 | NIST | |
Inp | 1079.00 | NIST | |
I | [1605.00; 1657.00] |
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|
I | 1654.00 | NIST | |
I | 1642.00 | NIST | |
I | Outlier 1605.00 | NIST | |
I | 1643.00 | NIST | |
I | 1657.00 | NIST | |
I | 1653.00 | NIST | |
I | 1653.00 | NIST | |
I | 1655.00 | NIST | |
I | 1656.00 | NIST | |
I | 1630.00 | NIST | |
I | 1638.00 | NIST | |
I | 1639.00 | NIST | |
I | 1652.00 | NIST | |
I | 1654.00 | NIST | |
I | Outlier 1605.00 | NIST | |
I | 1655.00 | NIST | |
Tboil | 477.70 | K | NIST |
Tc | 712.00 | K | Vapor-l... |
Tfus | 260.86 | K | Joback Calculated Property |
Vc | 0.393 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [194.28; 250.87] | J/mol×K | [462.76; 679.96] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 190 200 210 220 230 240 250 500 550 600 650 | ||||
Cp,gas | 194.28 | J/mol×K | 462.76 | Joback Calculated Property |
Cp,gas | 205.24 | J/mol×K | 498.96 | Joback Calculated Property |
Cp,gas | 215.55 | J/mol×K | 535.16 | Joback Calculated Property |
Cp,gas | 225.25 | J/mol×K | 571.36 | Joback Calculated Property |
Cp,gas | 234.35 | J/mol×K | 607.56 | Joback Calculated Property |
Cp,gas | 242.88 | J/mol×K | 643.76 | Joback Calculated Property |
Cp,gas | 250.87 | J/mol×K | 679.96 | Joback Calculated Property |
η | [0.0002879; 0.0022848] | Pa×s | [260.86; 462.76] | ![]() |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 300 350 400 450 | ||||
η | 0.0022848 | Pa×s | 260.86 | Joback Calculated Property |
η | 0.0013282 | Pa×s | 294.51 | Joback Calculated Property |
η | 0.0008630 | Pa×s | 328.16 | Joback Calculated Property |
η | 0.0006075 | Pa×s | 361.81 | Joback Calculated Property |
η | 0.0004540 | Pa×s | 395.46 | Joback Calculated Property |
η | 0.0003551 | Pa×s | 429.11 | Joback Calculated Property |
η | 0.0002879 | Pa×s | 462.76 | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [355.66; 507.57] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.47996e+01 | |||
Coefficient B | -4.16349e+03 | |||
Coefficient C | -6.87640e+01 | |||
Temperature range, min. | 355.66 | |||
Temperature range, max. | 507.57 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 355.66 | Calculated Property |
Pvap | 2.99 | kPa | 372.54 | Calculated Property |
Pvap | 6.14 | kPa | 389.42 | Calculated Property |
Pvap | 11.76 | kPa | 406.30 | Calculated Property |
Pvap | 21.16 | kPa | 423.18 | Calculated Property |
Pvap | 36.09 | kPa | 440.05 | Calculated Property |
Pvap | 58.77 | kPa | 456.93 | Calculated Property |
Pvap | 91.89 | kPa | 473.81 | Calculated Property |
Pvap | 138.63 | kPa | 490.69 | Calculated Property |
Pvap | 202.63 | kPa | 507.57 | Calculated Property |
Pvap | [0.02; 3618.98] | kPa | [289.85; 698.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.69627e+01 | |||
Coefficient B | -9.73128e+03 | |||
Coefficient C | -1.01911e+01 | |||
Coefficient D | 3.91264e-06 | |||
Temperature range, min. | 289.85 | |||
Temperature range, max. | 698.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 400 600 | ||||
Pvap | 0.02 | kPa | 289.85 | Calculated Property |
Pvap | 0.41 | kPa | 335.20 | Calculated Property |
Pvap | 4.08 | kPa | 380.55 | Calculated Property |
Pvap | 22.76 | kPa | 425.90 | Calculated Property |
Pvap | 85.77 | kPa | 471.25 | Calculated Property |
Pvap | 245.52 | kPa | 516.60 | Calculated Property |
Pvap | 576.76 | kPa | 561.95 | Calculated Property |
Pvap | 1172.75 | kPa | 607.30 | Calculated Property |
Pvap | 2143.42 | kPa | 652.65 | Calculated Property |
Pvap | 3618.98 | kPa | 698.00 | Calculated Property |
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