Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | [-3229.96; -3223.50] | kJ/mol |
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ΔcH°solid | -3223.50 ± 0.50 | kJ/mol | NIST |
ΔcH°solid | -3223.70 | kJ/mol | NIST |
ΔcH°solid | -3229.96 | kJ/mol | NIST |
ΔfG° | -412.22 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -513.01 | kJ/mol | Joback Calculated Property |
ΔfH°solid | [-782.12; -781.91] | kJ/mol |
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ΔfH°solid | -782.12 | kJ/mol | NIST |
ΔfH°solid | -781.91 | kJ/mol | NIST |
ΔfusH° | 21.50 | kJ/mol | Joback Calculated Property |
ΔsubH° | 129.80 ± 0.60 | kJ/mol | NIST |
ΔvapH° | 83.19 | kJ/mol | Joback Calculated Property |
log10WS | -2.41 | Aq. Sol... | |
logPoct/wat | 1.083 | Crippen Calculated Property | |
McVol | 114.700 | ml/mol | McGowan Calculated Property |
Pc | 5406.57 | kPa | Joback Calculated Property |
Inp | [225.33; 1643.00] |
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|
Inp | 1643.00 | NIST | |
Inp | 225.33 | NIST | |
S°solid,1 bar | 207.94 | J/mol×K | NIST |
Tboil | 706.20 | K | Joback Calculated Property |
Tc | 907.67 | K | Joback Calculated Property |
Tfus | 480.00 ± 3.00 | K | NIST |
Vc | 0.425 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [282.80; 315.57] | J/mol×K | [706.20; 907.67] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 280 285 290 295 300 305 310 315 750 800 850 900 | ||||
Cp,gas | 282.80 | J/mol×K | 706.20 | Joback Calculated Property |
Cp,gas | 289.37 | J/mol×K | 739.78 | Joback Calculated Property |
Cp,gas | 295.47 | J/mol×K | 773.36 | Joback Calculated Property |
Cp,gas | 301.12 | J/mol×K | 806.93 | Joback Calculated Property |
Cp,gas | 306.34 | J/mol×K | 840.51 | Joback Calculated Property |
Cp,gas | 311.15 | J/mol×K | 874.09 | Joback Calculated Property |
Cp,gas | 315.57 | J/mol×K | 907.67 | Joback Calculated Property |
Cp,solid | [188.11; 201.70] | J/mol×K | [298.10; 323.00] | ![]() |
Cp,solid | 188.11 | J/mol×K | 298.10 | NIST |
Cp,solid | 201.70 | J/mol×K | 323.00 | NIST |
Cp,solid | 201.70 | J/mol×K | 323.00 | NIST |
η | [0.0000196; 0.0013822] | Pa×s | [440.36; 706.20] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 500 600 700 | ||||
η | 0.0013822 | Pa×s | 440.36 | Joback Calculated Property |
η | 0.0004918 | Pa×s | 484.67 | Joback Calculated Property |
η | 0.0002081 | Pa×s | 528.97 | Joback Calculated Property |
η | 0.0001006 | Pa×s | 573.28 | Joback Calculated Property |
η | 0.0000539 | Pa×s | 617.59 | Joback Calculated Property |
η | 0.0000314 | Pa×s | 661.89 | Joback Calculated Property |
η | 0.0000196 | Pa×s | 706.20 | Joback Calculated Property |
ΔfusH | 36.50 | kJ/mol | 463.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.78; 3924.44] | kPa | [464.15; 800.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.08639e+02 | |||
Coefficient B | -2.17466e+04 | |||
Coefficient C | -2.66695e+01 | |||
Coefficient D | 7.96015e-06 | |||
Temperature range, min. | 464.15 | |||
Temperature range, max. | 800.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 500 600 700 800 | ||||
Pvap | 0.78 | kPa | 464.15 | Calculated Property |
Pvap | 4.29 | kPa | 501.47 | Calculated Property |
Pvap | 17.37 | kPa | 538.78 | Calculated Property |
Pvap | 55.37 | kPa | 576.10 | Calculated Property |
Pvap | 146.93 | kPa | 613.42 | Calculated Property |
Pvap | 338.14 | kPa | 650.73 | Calculated Property |
Pvap | 696.78 | kPa | 688.05 | Calculated Property |
Pvap | 1317.82 | kPa | 725.37 | Calculated Property |
Pvap | 2332.59 | kPa | 762.68 | Calculated Property |
Pvap | 3924.44 | kPa | 800.00 | Calculated Property |
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