Property | Value | Unit | Source |
---|---|---|---|
PAff | 723.00 | kJ/mol | NIST |
BasG | 694.10 | kJ/mol | NIST |
ΔcH°solid | [-1654.20; -1653.00] | kJ/mol |
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ΔcH°solid | -1654.20 ± 0.20 | kJ/mol | NIST |
ΔcH°solid | -1653.00 ± 1.00 | kJ/mol | NIST |
ΔfG° | 240.74 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [266.00; 266.30] | kJ/mol |
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ΔfH°gas | 266.30 ± 1.00 | kJ/mol | NIST |
ΔfH°gas | 266.00 ± 2.00 | kJ/mol | NIST |
ΔfH°solid | [186.00; 187.90] | kJ/mol |
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ΔfH°solid | 187.90 ± 0.20 | kJ/mol | NIST |
ΔfH°solid | 186.00 ± 1.00 | kJ/mol | NIST |
ΔfusH° | 10.70 | kJ/mol | Fusion ... |
ΔsubH° | [78.20; 80.00] | kJ/mol |
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ΔsubH° | 78.37 ± 0.96 | kJ/mol | NIST |
ΔsubH° | 78.40 | kJ/mol | NIST |
ΔsubH° | 78.20 ± 1.00 | kJ/mol | NIST |
ΔsubH° | 79.10 ± 0.80 | kJ/mol | NIST |
ΔsubH° | 80.00 | kJ/mol | NIST |
ΔvapH° | 43.23 | kJ/mol | Joback Calculated Property |
IE | [12.70; 12.88] | eV |
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IE | 12.80 ± 0.10 | eV | NIST |
IE | 12.70 | eV | NIST |
IE | 12.88 | eV | NIST |
log10WS | -0.81 | Crippen Calculated Property | |
logPoct/wat | 0.424 | Crippen Calculated Property | |
McVol | 55.890 | ml/mol | McGowan Calculated Property |
Pc | 4130.29 | kPa | Joback Calculated Property |
Inp | 801.00 | NIST | |
S°solid,1 bar | 130.96 | J/mol×K | NIST |
Tboil | [491.70; 493.20] | K |
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Tboil | 493.20 | K | NIST |
Tboil | 491.70 | K | NIST |
Tc | 690.33 | K | Joback Calculated Property |
Tfus | [304.00; 307.60] | K |
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Tfus | 304.80 | K | KDB |
Tfus | 305.00 ± 2.00 | K | NIST |
Tfus | 304.00 ± 3.00 | K | NIST |
Tfus | 307.60 ± 0.60 | K | NIST |
Tfus | 304.65 ± 1.50 | K | NIST |
Ttriple | [304.91; 304.99] | K |
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Ttriple | 304.91 ± 0.06 | K | NIST |
Ttriple | 304.98 ± 0.02 | K | NIST |
Ttriple | 304.99 ± 0.02 | K | NIST |
Vc | 0.256 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [92.95; 110.54] | J/mol×K | [472.20; 690.33] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 95 100 105 110 500 550 600 650 | ||||
Cp,gas | 92.95 | J/mol×K | 472.20 | Joback Calculated Property |
Cp,gas | 96.26 | J/mol×K | 508.56 | Joback Calculated Property |
Cp,gas | 99.42 | J/mol×K | 544.91 | Joback Calculated Property |
Cp,gas | 102.42 | J/mol×K | 581.27 | Joback Calculated Property |
Cp,gas | 105.27 | J/mol×K | 617.62 | Joback Calculated Property |
Cp,gas | 107.98 | J/mol×K | 653.98 | Joback Calculated Property |
Cp,gas | 110.54 | J/mol×K | 690.33 | Joback Calculated Property |
Cp,solid | 110.29 | J/mol×K | 298.15 | NIST |
ΔfusH | [10.70; 10.80] | kJ/mol | [305.00; 305.00] | ![]() |
ΔfusH | 10.70 | kJ/mol | 305.00 | NIST |
ΔfusH | 10.80 | kJ/mol | 305.00 | NIST |
ΔfusH | 10.80 | kJ/mol | 305.00 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 382.20 | K | 2.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [363.09; 523.97] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.58259e+01 | |||
Coefficient B | -5.23199e+03 | |||
Coefficient C | -2.63730e+01 | |||
Temperature range, min. | 363.09 | |||
Temperature range, max. | 523.97 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 363.09 | Calculated Property |
Pvap | 2.92 | kPa | 380.97 | Calculated Property |
Pvap | 5.92 | kPa | 398.84 | Calculated Property |
Pvap | 11.27 | kPa | 416.72 | Calculated Property |
Pvap | 20.27 | kPa | 434.59 | Calculated Property |
Pvap | 34.71 | kPa | 452.47 | Calculated Property |
Pvap | 56.90 | kPa | 470.34 | Calculated Property |
Pvap | 89.79 | kPa | 488.22 | Calculated Property |
Pvap | 136.94 | kPa | 506.09 | Calculated Property |
Pvap | 202.63 | kPa | 523.97 | Calculated Property |
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