Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 266.00 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 149.00 ± 2.00 | kJ/mol | NIST |
ΔfH°liquid | 84.90 ± 0.40 | kJ/mol | NIST |
ΔfusH° | 18.03 | kJ/mol | Fusion ... |
ΔvapH° | [64.00; 64.10] | kJ/mol |
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ΔvapH° | 64.00 ± 1.00 | kJ/mol | NIST |
ΔvapH° | 64.10 | kJ/mol | NIST |
log10WS | -2.07 | Crippen Calculated Property | |
logPoct/wat | 1.594 | Crippen Calculated Property | |
McVol | 98.160 | ml/mol | McGowan Calculated Property |
NFPA Fire | 2 | KDB | |
NFPA Health | 4 | KDB | |
Pc | 2940.89 | kPa | Joback Calculated Property |
Inp | 1090.00 | NIST | |
Tboil | 568.20 | K | NIST |
Tc | 748.95 | K | Joback Calculated Property |
Tfus | 287.36 | K | Joback Calculated Property |
Vc | 0.423 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [208.40; 248.56] | J/mol×K | [540.84; 748.95] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 210 220 230 240 250 600 700 | ||||
Cp,gas | 208.40 | J/mol×K | 540.84 | Joback Calculated Property |
Cp,gas | 216.00 | J/mol×K | 575.53 | Joback Calculated Property |
Cp,gas | 223.23 | J/mol×K | 610.21 | Joback Calculated Property |
Cp,gas | 230.08 | J/mol×K | 644.90 | Joback Calculated Property |
Cp,gas | 236.58 | J/mol×K | 679.58 | Joback Calculated Property |
Cp,gas | 242.74 | J/mol×K | 714.27 | Joback Calculated Property |
Cp,gas | 248.56 | J/mol×K | 748.95 | Joback Calculated Property |
ΔfusH | 18.00 | kJ/mol | 275.00 | NIST |
ΔvapH | 58.70 | kJ/mol | 435.50 | NIST |
ρl | 975.26 | kg/m3 | 298.15 | Compres... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [423.82; 601.89] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.62876e+01 | |||
Coefficient B | -6.22480e+03 | |||
Coefficient C | -3.47660e+01 | |||
Temperature range, min. | 423.82 | |||
Temperature range, max. | 601.89 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
Pvap | 1.33 | kPa | 423.82 | Calculated Property |
Pvap | 2.89 | kPa | 443.61 | Calculated Property |
Pvap | 5.84 | kPa | 463.39 | Calculated Property |
Pvap | 11.09 | kPa | 483.18 | Calculated Property |
Pvap | 19.93 | kPa | 502.96 | Calculated Property |
Pvap | 34.17 | kPa | 522.75 | Calculated Property |
Pvap | 56.18 | kPa | 542.53 | Calculated Property |
Pvap | 88.97 | kPa | 562.32 | Calculated Property |
Pvap | 136.29 | kPa | 582.10 | Calculated Property |
Pvap | 202.66 | kPa | 601.89 | Calculated Property |
Pvap | [4.75e-06; 3197.13] | kPa | [275.64; 781.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.46196e+02 | |||
Coefficient B | -1.98500e+04 | |||
Coefficient C | -3.33952e+01 | |||
Coefficient D | 1.59380e-05 | |||
Temperature range, min. | 275.64 | |||
Temperature range, max. | 781.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 400 600 | ||||
Pvap | 4.75e-06 | kPa | 275.64 | Calculated Property |
Pvap | 3.28e-03 | kPa | 331.79 | Calculated Property |
Pvap | 0.19 | kPa | 387.94 | Calculated Property |
Pvap | 2.90 | kPa | 444.09 | Calculated Property |
Pvap | 19.09 | kPa | 500.24 | Calculated Property |
Pvap | 77.23 | kPa | 556.40 | Calculated Property |
Pvap | 233.32 | kPa | 612.55 | Calculated Property |
Pvap | 596.56 | kPa | 668.70 | Calculated Property |
Pvap | 1401.32 | kPa | 724.85 | Calculated Property |
Pvap | 3197.13 | kPa | 781.00 | Calculated Property |
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