Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -231.46 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -399.14 | kJ/mol | Joback Calculated Property |
ΔfusH° | 25.34 | kJ/mol | Influen... |
ΔvapH° | 60.71 | kJ/mol | Joback Calculated Property |
log10WS | -1.77 | Aq. Sol... | |
logPoct/wat | 1.603 | Crippen Calculated Property | |
McVol | 127.220 | ml/mol | McGowan Calculated Property |
Pc | 4109.14 | kPa | Joback Calculated Property |
Inp | [1433.00; 1453.00] |
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|
Inp | Outlier 1433.00 | NIST | |
Inp | 1452.00 | NIST | |
Inp | 1446.00 | NIST | |
Inp | 1453.00 | NIST | |
Inp | 1448.00 | NIST | |
Inp | 1448.00 | NIST | |
Inp | 1448.00 | NIST | |
I | [2414.00; 2514.00] |
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|
I | 2514.00 | NIST | |
I | 2414.00 | NIST | |
I | 2514.00 | NIST | |
Tboil | 588.68 | K | Joback Calculated Property |
Tc | 812.18 | K | Joback Calculated Property |
Tfus | [350.40; 352.98] | K |
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Tfus | 350.40 | K | Aq. Sol... |
Tfus | 352.98 | K | Solid-l... |
Tfus | 351.00 | K | Determi... |
Vc | 0.432 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [304.26; 359.35] | J/mol×K | [588.68; 812.18] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 300 310 320 330 340 350 360 600 700 800 | ||||
Cp,gas | 304.26 | J/mol×K | 588.68 | Joback Calculated Property |
Cp,gas | 314.95 | J/mol×K | 625.93 | Joback Calculated Property |
Cp,gas | 324.97 | J/mol×K | 663.18 | Joback Calculated Property |
Cp,gas | 334.37 | J/mol×K | 700.43 | Joback Calculated Property |
Cp,gas | 343.20 | J/mol×K | 737.68 | Joback Calculated Property |
Cp,gas | 351.51 | J/mol×K | 774.93 | Joback Calculated Property |
Cp,gas | 359.35 | J/mol×K | 812.18 | Joback Calculated Property |
η | [0.0000432; 0.0008942] | Pa×s | [406.08; 588.68] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-4 4.00e-4 6.00e-4 8.00e-4 450 500 550 | ||||
η | 0.0008942 | Pa×s | 406.08 | Joback Calculated Property |
η | 0.0004525 | Pa×s | 436.51 | Joback Calculated Property |
η | 0.0002502 | Pa×s | 466.95 | Joback Calculated Property |
η | 0.0001488 | Pa×s | 497.38 | Joback Calculated Property |
η | 0.0000939 | Pa×s | 527.81 | Joback Calculated Property |
η | 0.0000623 | Pa×s | 558.25 | Joback Calculated Property |
η | 0.0000432 | Pa×s | 588.68 | Joback Calculated Property |
ΔfusH | 23.10 | kJ/mol | 349.80 | NIST |
ΔsubH | 101.50 | kJ/mol | 317.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.57e-03; 3234.93] | kPa | [350.65; 748.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.75341e+02 | |||
Coefficient B | -1.86800e+04 | |||
Coefficient C | -2.20762e+01 | |||
Coefficient D | 6.79415e-06 | |||
Temperature range, min. | 350.65 | |||
Temperature range, max. | 748.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 400 500 600 700 | ||||
Pvap | 1.57e-03 | kPa | 350.65 | Calculated Property |
Pvap | 0.06 | kPa | 394.80 | Calculated Property |
Pvap | 0.80 | kPa | 438.95 | Calculated Property |
Pvap | 6.19 | kPa | 483.10 | Calculated Property |
Pvap | 31.00 | kPa | 527.25 | Calculated Property |
Pvap | 112.81 | kPa | 571.40 | Calculated Property |
Pvap | 324.90 | kPa | 615.55 | Calculated Property |
Pvap | 786.65 | kPa | 659.70 | Calculated Property |
Pvap | 1673.79 | kPa | 703.85 | Calculated Property |
Pvap | 3234.93 | kPa | 748.00 | Calculated Property |
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