Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -3093.20 ± 4.20 | kJ/mol | NIST |
ΔfG° | 218.66 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 211.63 | kJ/mol | Joback Calculated Property |
ΔfusH° | 13.76 | kJ/mol | Joback Calculated Property |
ΔvapH° | 50.63 | kJ/mol | Joback Calculated Property |
IE | [8.45; 8.60] | eV |
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IE | 8.45 | eV | NIST |
IE | 8.60 | eV | NIST |
log10WS | -5.37 | Aq. Sol... | |
logPoct/wat | 2.896 | Crippen Calculated Property | |
McVol | 123.280 | ml/mol | McGowan Calculated Property |
Pc | 4316.89 | kPa | Joback Calculated Property |
Inp | [1412.00; 1450.00] |
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|
Inp | 1448.00 | NIST | |
Inp | 1450.00 | NIST | |
Inp | 1412.00 | NIST | |
Inp | 1412.00 | NIST | |
Inp | 1448.00 | NIST | |
I | [2176.00; 2176.00] |
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|
I | 2176.00 | NIST | |
I | 2176.00 | NIST | |
I | 2176.00 | NIST | |
Tboil | 558.20 | K | NIST |
Tc | 852.28 | K | Joback Calculated Property |
Tfus | [400.00; 403.98] | K |
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Tfus | 403.98 | K | Aq. Sol... |
Tfus | 403.15 | K | Thermal... |
Tfus | 402.00 ± 2.00 | K | NIST |
Tfus | 400.00 ± 2.00 | K | NIST |
Tfus | 402.15 ± 0.50 | K | NIST |
Vc | 0.440 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [177.80; 213.79] | J/mol×K | [554.62; 852.28] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 600 700 800 | ||||
Cp,gas | 177.80 | J/mol×K | 554.62 | Joback Calculated Property |
Cp,gas | 185.61 | J/mol×K | 604.23 | Joback Calculated Property |
Cp,gas | 192.55 | J/mol×K | 653.84 | Joback Calculated Property |
Cp,gas | 198.74 | J/mol×K | 703.45 | Joback Calculated Property |
Cp,gas | 204.27 | J/mol×K | 753.06 | Joback Calculated Property |
Cp,gas | 209.25 | J/mol×K | 802.67 | Joback Calculated Property |
Cp,gas | 213.79 | J/mol×K | 852.28 | Joback Calculated Property |
Cp,solid | 160.77 | J/mol×K | 298.15 | NIST |
η | [0.0003330; 0.0029814] | Pa×s | [312.44; 554.62] | ![]() |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 400 500 | ||||
η | 0.0029814 | Pa×s | 312.44 | Joback Calculated Property |
η | 0.0016788 | Pa×s | 352.80 | Joback Calculated Property |
η | 0.0010637 | Pa×s | 393.17 | Joback Calculated Property |
η | 0.0007337 | Pa×s | 433.53 | Joback Calculated Property |
η | 0.0005391 | Pa×s | 473.89 | Joback Calculated Property |
η | 0.0004158 | Pa×s | 514.26 | Joback Calculated Property |
η | 0.0003330 | Pa×s | 554.62 | Joback Calculated Property |
ΔfusH | [22.30; 22.38] | kJ/mol | [402.00; 402.40] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 22.3 22.32 22.34 22.36 22.38 402 402.2 402.40000000000003 | ||||
ΔfusH | 22.37 | kJ/mol | 402.00 | NIST |
ΔfusH | 22.37 | kJ/mol | 402.00 | NIST |
ΔfusH | 22.34 | kJ/mol | 402.00 | NIST |
ΔfusH | 22.38 | kJ/mol | 402.15 | NIST |
ΔfusH | 22.30 | kJ/mol | 402.40 | NIST |
ΔsubH | 63.40 | kJ/mol | 386.50 | NIST |
ΔvapH | 52.60 | kJ/mol | 481.00 | NIST |
ΔfusS | [55.60; 55.65] | J/mol×K | [402.00; 402.15] | ![]() |
ΔfusS | 55.65 | J/mol×K | 402.00 | NIST |
ΔfusS | 55.60 | J/mol×K | 402.00 | NIST |
ΔfusS | 55.60 | J/mol×K | 402.15 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [423.52; 590.77] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.51398e+01 | |||
Coefficient B | -4.85971e+03 | |||
Coefficient C | -9.63160e+01 | |||
Temperature range, min. | 423.52 | |||
Temperature range, max. | 590.77 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
Pvap | 1.33 | kPa | 423.52 | Calculated Property |
Pvap | 2.96 | kPa | 442.10 | Calculated Property |
Pvap | 6.07 | kPa | 460.69 | Calculated Property |
Pvap | 11.59 | kPa | 479.27 | Calculated Property |
Pvap | 20.84 | kPa | 497.85 | Calculated Property |
Pvap | 35.60 | kPa | 516.44 | Calculated Property |
Pvap | 58.11 | kPa | 535.02 | Calculated Property |
Pvap | 91.16 | kPa | 553.60 | Calculated Property |
Pvap | 138.04 | kPa | 572.19 | Calculated Property |
Pvap | 202.63 | kPa | 590.77 | Calculated Property |
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