Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 157.73 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -182.92 | kJ/mol | Joback Calculated Property |
ΔfusH° | 29.68 | kJ/mol | Joback Calculated Property |
ΔvapH° | 56.13 | kJ/mol | Joback Calculated Property |
log10WS | -5.49 | Crippen Calculated Property | |
logPoct/wat | 4.499 | Crippen Calculated Property | |
McVol | 212.540 | ml/mol | McGowan Calculated Property |
Pc | 1621.98 | kPa | Joback Calculated Property |
Inp | 1538.00 | NIST | |
Tboil | 612.08 | K | Joback Calculated Property |
Tc | 805.10 | K | Joback Calculated Property |
Tfus | 346.58 | K | Joback Calculated Property |
Vc | 0.824 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [546.12; 643.08] | J/mol×K | [612.08; 805.10] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 540 560 580 600 620 640 650 700 750 800 | ||||
Cp,gas | 546.12 | J/mol×K | 612.08 | Joback Calculated Property |
Cp,gas | 564.31 | J/mol×K | 644.25 | Joback Calculated Property |
Cp,gas | 581.66 | J/mol×K | 676.42 | Joback Calculated Property |
Cp,gas | 598.19 | J/mol×K | 708.59 | Joback Calculated Property |
Cp,gas | 613.93 | J/mol×K | 740.76 | Joback Calculated Property |
Cp,gas | 628.88 | J/mol×K | 772.93 | Joback Calculated Property |
Cp,gas | 643.08 | J/mol×K | 805.10 | Joback Calculated Property |
η | [0.0001420; 0.0011135] | Pa×s | [346.58; 612.08] | ![]() |
T(K) Dynamic viscosity (Pa×s) 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 400 500 600 | ||||
η | 0.0011135 | Pa×s | 346.58 | Joback Calculated Property |
η | 0.0006505 | Pa×s | 390.83 | Joback Calculated Property |
η | 0.0004239 | Pa×s | 435.08 | Joback Calculated Property |
η | 0.0002990 | Pa×s | 479.33 | Joback Calculated Property |
η | 0.0002237 | Pa×s | 523.58 | Joback Calculated Property |
η | 0.0001751 | Pa×s | 567.83 | Joback Calculated Property |
η | 0.0001420 | Pa×s | 612.08 | Joback Calculated Property |
ΔvapH | 56.50 | kJ/mol | 454.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.13; 1568.81] | kPa | [359.15; 723.64] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | -5.97616e+00 | |||
Coefficient B | -5.95488e+03 | |||
Coefficient C | 3.56766e+00 | |||
Coefficient D | -3.68029e-06 | |||
Temperature range, min. | 359.15 | |||
Temperature range, max. | 723.64 | |||
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 1400 1600 400 500 600 700 | ||||
Pvap | 0.13 | kPa | 359.15 | Calculated Property |
Pvap | 0.91 | kPa | 399.65 | Calculated Property |
Pvap | 4.47 | kPa | 440.15 | Calculated Property |
Pvap | 16.69 | kPa | 480.65 | Calculated Property |
Pvap | 50.26 | kPa | 521.15 | Calculated Property |
Pvap | 127.32 | kPa | 561.64 | Calculated Property |
Pvap | 279.99 | kPa | 602.14 | Calculated Property |
Pvap | 547.12 | kPa | 642.64 | Calculated Property |
Pvap | 967.23 | kPa | 683.14 | Calculated Property |
Pvap | 1568.81 | kPa | 723.64 | Calculated Property |
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