Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 590.71 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 374.92 | kJ/mol | Joback Calculated Property |
ΔfusH° | 32.46 | kJ/mol | Joback Calculated Property |
ΔvapH° | 72.90 | kJ/mol | Joback Calculated Property |
IE | 7.66 | eV | NIST |
log10WS | [-7.97; -7.94] |
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|
log10WS | -7.94 | Aq. Sol... | |
log10WS | -7.97 | Rytting... | |
logPoct/wat | 5.553 | Crippen Calculated Property | |
McVol | 213.750 | ml/mol | McGowan Calculated Property |
Pc | 2256.81 | kPa | Joback Calculated Property |
Inp | [457.90; 2959.00] |
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|
Inp | 2959.00 | NIST | |
Inp | 2959.00 | NIST | |
Inp | 2911.00 | NIST | |
Inp | 2900.00 | NIST | |
Inp | 2906.00 | NIST | |
Inp | 2906.00 | NIST | |
Inp | 2877.00 | NIST | |
Inp | 2906.00 | NIST | |
Inp | 2959.00 | NIST | |
Inp | 468.90 | NIST | |
Inp | 467.70 | NIST | |
Inp | 457.90 | NIST | |
Inp | 468.88 | NIST | |
Inp | 468.69 | NIST | |
Inp | 462.09 | NIST | |
Inp | 468.44 | NIST | |
Inp | 469.00 | NIST | |
Inp | 467.02 | NIST | |
Inp | 471.16 | NIST | |
Inp | 468.44 | NIST | |
Inp | 471.16 | NIST | |
Inp | 2959.00 | NIST | |
Inp | 468.88 | NIST | |
Inp | 2906.00 | NIST | |
Tboil | 795.54 | K | Joback Calculated Property |
Tc | 1051.83 | K | Joback Calculated Property |
Tfus | [442.40; 452.82] | K |
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Tfus | 452.82 | K | Aq. Sol... |
Tfus | 442.40 ± 0.80 | K | NIST |
Vc | 0.836 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [599.80; 685.13] | J/mol×K | [795.54; 1051.83] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 600 620 640 660 680 800 900 1000 | ||||
Cp,gas | 599.80 | J/mol×K | 795.54 | Joback Calculated Property |
Cp,gas | 614.89 | J/mol×K | 838.25 | Joback Calculated Property |
Cp,gas | 629.30 | J/mol×K | 880.97 | Joback Calculated Property |
Cp,gas | 643.27 | J/mol×K | 923.68 | Joback Calculated Property |
Cp,gas | 657.07 | J/mol×K | 966.40 | Joback Calculated Property |
Cp,gas | 670.94 | J/mol×K | 1009.11 | Joback Calculated Property |
Cp,gas | 685.13 | J/mol×K | 1051.83 | Joback Calculated Property |
η | [0.0020987; 0.0031708] | Pa×s | [539.25; 795.54] | ![]() |
T(K) Dynamic viscosity (Pa×s) 2.00e-3 2.20e-3 2.40e-3 2.60e-3 2.80e-3 3.00e-3 3.20e-3 600 700 800 | ||||
η | 0.0031708 | Pa×s | 539.25 | Joback Calculated Property |
η | 0.0028862 | Pa×s | 581.97 | Joback Calculated Property |
η | 0.0026613 | Pa×s | 624.68 | Joback Calculated Property |
η | 0.0024794 | Pa×s | 667.39 | Joback Calculated Property |
η | 0.0023298 | Pa×s | 710.11 | Joback Calculated Property |
η | 0.0022047 | Pa×s | 752.83 | Joback Calculated Property |
η | 0.0020987 | Pa×s | 795.54 | Joback Calculated Property |
ΔsubH | [127.20; 127.20] | kJ/mol | [401.00; 413.00] | ![]() |
ΔsubH | 127.20 | kJ/mol | 401.00 | NIST |
ΔsubH | 127.20 ± 2.40 | kJ/mol | 413.00 | NIST |
ΔvapH | 93.80 | kJ/mol | 398.00 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 553.20 | K | 11.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.68] | kPa | [545.94; 633.36] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 3.66850e+01 | |||
Coefficient B | -1.98707e+04 | |||
Temperature range, min. | 545.94 | |||
Temperature range, max. | 633.36 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 560 580 600 620 | ||||
Pvap | 1.33 | kPa | 545.94 | Calculated Property |
Pvap | 2.52 | kPa | 555.65 | Calculated Property |
Pvap | 4.66 | kPa | 565.37 | Calculated Property |
Pvap | 8.43 | kPa | 575.08 | Calculated Property |
Pvap | 14.97 | kPa | 584.79 | Calculated Property |
Pvap | 26.08 | kPa | 594.51 | Calculated Property |
Pvap | 44.64 | kPa | 604.22 | Calculated Property |
Pvap | 75.10 | kPa | 613.93 | Calculated Property |
Pvap | 124.33 | kPa | 623.65 | Calculated Property |
Pvap | 202.68 | kPa | 633.36 | Calculated Property |
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