Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | [-1518.00; -1492.00] | kJ/mol |
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ΔcH°solid | -1515.30 | kJ/mol | NIST |
ΔcH°solid | -1515.70 ± 0.30 | kJ/mol | NIST |
ΔcH°solid | -1492.00 ± 1.00 | kJ/mol | NIST |
ΔcH°solid | -1518.00 | kJ/mol | NIST |
ΔfG° | -251.82 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-489.50; -464.00] | kJ/mol |
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ΔfH°gas | -465.76 ± 0.50 | kJ/mol | NIST |
ΔfH°gas | -489.50 | kJ/mol | NIST |
ΔfH°gas | -464.00 | kJ/mol | NIST |
ΔfH°solid | [-546.00; -520.49] | kJ/mol |
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ΔfH°solid | -522.30 ± 0.40 | kJ/mol | NIST |
ΔfH°solid | -546.00 ± 11.00 | kJ/mol | NIST |
ΔfH°solid | -520.49 | kJ/mol | NIST |
ΔfusH° | 18.23 | kJ/mol | Joback Calculated Property |
ΔsubH° | [48.50; 56.60] | kJ/mol |
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ΔsubH° | 55.60 | kJ/mol | NIST |
ΔsubH° | 56.50 | kJ/mol | NIST |
ΔsubH° | 56.60 ± 0.20 | kJ/mol | NIST |
ΔsubH° | 56.50 | kJ/mol | NIST |
ΔsubH° | 56.20 ± 0.20 | kJ/mol | NIST |
ΔsubH° | Outlier 48.50 ± 2.50 | kJ/mol | NIST |
ΔvapH° | 36.54 | kJ/mol | Joback Calculated Property |
IE | [10.30; 10.80] | eV |
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IE | 10.30 | eV | NIST |
IE | 10.59 ± 0.05 | eV | NIST |
IE | 10.80 | eV | NIST |
log10WS | 0.28 | Crippen Calculated Property | |
logPoct/wat | -0.078 | Crippen Calculated Property | |
McVol | 59.880 | ml/mol | McGowan Calculated Property |
Pc | 5962.94 | kPa | Joback Calculated Property |
Inp | [650.00; 660.00] |
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|
Inp | 650.00 | NIST | |
Inp | 660.00 | NIST | |
Inp | 658.00 | NIST | |
I | [1167.00; 1167.00] |
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|
I | 1167.00 | NIST | |
I | 1167.00 | NIST | |
S°gas | 284.90 ± 3.40 | J/mol×K | NIST |
S°solid,1 bar | [133.00; 142.89] | J/mol×K |
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S°solid,1 bar | 142.89 | J/mol×K | NIST |
S°solid,1 bar | 133.00 | J/mol×K | NIST |
Tboil | 373.11 | K | Joback Calculated Property |
Tc | 585.00 | K | Joback Calculated Property |
Tfus | 335.65 ± 1.50 | K | NIST |
Ttriple | 333.44 ± 0.02 | K | NIST |
Vc | 0.201 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [109.71; 158.33] | J/mol×K | [373.11; 585.00] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 110 120 130 140 150 160 400 450 500 550 | ||||
Cp,gas | 109.71 | J/mol×K | 373.11 | Joback Calculated Property |
Cp,gas | 118.97 | J/mol×K | 408.43 | Joback Calculated Property |
Cp,gas | 127.75 | J/mol×K | 443.74 | Joback Calculated Property |
Cp,gas | 136.06 | J/mol×K | 479.06 | Joback Calculated Property |
Cp,gas | 143.93 | J/mol×K | 514.37 | Joback Calculated Property |
Cp,gas | 151.34 | J/mol×K | 549.69 | Joback Calculated Property |
Cp,gas | 158.33 | J/mol×K | 585.00 | Joback Calculated Property |
Cp,solid | [111.40; 113.08] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,solid | 113.08 | J/mol×K | 298.15 | NIST |
Cp,solid | 111.40 | J/mol×K | 298.15 | NIST |
η | [0.0005292; 0.0136050] | Pa×s | [214.90; 373.11] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 0.01 0.01 250 300 350 | ||||
η | 0.0136050 | Pa×s | 214.90 | Joback Calculated Property |
η | 0.0058920 | Pa×s | 241.27 | Joback Calculated Property |
η | 0.0030091 | Pa×s | 267.64 | Joback Calculated Property |
η | 0.0017337 | Pa×s | 294.00 | Joback Calculated Property |
η | 0.0010937 | Pa×s | 320.37 | Joback Calculated Property |
η | 0.0007401 | Pa×s | 346.74 | Joback Calculated Property |
η | 0.0005292 | Pa×s | 373.11 | Joback Calculated Property |
ΔfusH | [15.10; 15.11] | kJ/mol | [333.40; 333.44] | ![]() |
ΔfusH | 15.10 | kJ/mol | 333.40 | NIST |
ΔfusH | 15.10 | kJ/mol | 333.40 | NIST |
ΔfusH | 15.11 | kJ/mol | 333.40 | NIST |
ΔfusH | 15.11 | kJ/mol | 333.44 | NIST |
ΔsubH | 57.90 | kJ/mol | 221.50 | NIST |
ΔvapH | 40.00 | kJ/mol | 357.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [288.76; 412.48] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.47991e+01 | |||
Coefficient B | -3.39060e+03 | |||
Coefficient C | -5.51110e+01 | |||
Temperature range, min. | 288.76 | |||
Temperature range, max. | 412.48 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 288.76 | Calculated Property |
Pvap | 2.99 | kPa | 302.51 | Calculated Property |
Pvap | 6.14 | kPa | 316.25 | Calculated Property |
Pvap | 11.76 | kPa | 330.00 | Calculated Property |
Pvap | 21.16 | kPa | 343.75 | Calculated Property |
Pvap | 36.10 | kPa | 357.49 | Calculated Property |
Pvap | 58.78 | kPa | 371.24 | Calculated Property |
Pvap | 91.90 | kPa | 384.99 | Calculated Property |
Pvap | 138.64 | kPa | 398.73 | Calculated Property |
Pvap | 202.64 | kPa | 412.48 | Calculated Property |
Pvap | [11.31; 5791.65] | kPa | [329.00; 604.40] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.45411e+01 | |||
Coefficient B | -7.85949e+03 | |||
Coefficient C | -1.01570e+01 | |||
Coefficient D | 5.95284e-06 | |||
Temperature range, min. | 329.00 | |||
Temperature range, max. | 604.40 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 400 500 600 | ||||
Pvap | 11.31 | kPa | 329.00 | Calculated Property |
Pvap | 39.68 | kPa | 359.60 | Calculated Property |
Pvap | 110.17 | kPa | 390.20 | Calculated Property |
Pvap | 256.62 | kPa | 420.80 | Calculated Property |
Pvap | 523.03 | kPa | 451.40 | Calculated Property |
Pvap | 961.82 | kPa | 482.00 | Calculated Property |
Pvap | 1633.08 | kPa | 512.60 | Calculated Property |
Pvap | 2605.42 | kPa | 543.20 | Calculated Property |
Pvap | 3959.17 | kPa | 573.80 | Calculated Property |
Pvap | 5791.65 | kPa | 604.40 | Calculated Property |
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