Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | [-253.50; -242.90] | kJ/mol |
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ΔcH°solid | -242.90 ± 0.92 | kJ/mol | NIST |
ΔcH°solid | -253.50 ± 0.46 | kJ/mol | NIST |
ΔfG° | -565.52 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -614.23 | kJ/mol | Joback Calculated Property |
ΔfH°solid | [-829.94; -828.93] | kJ/mol |
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ΔfH°solid | -828.93 ± 0.46 | kJ/mol | NIST |
ΔfH°solid | -829.94 ± 0.96 | kJ/mol | NIST |
ΔfusH° | 12.31 | kJ/mol | Joback Calculated Property |
ΔsubH° | 97.91 | kJ/mol | NIST |
ΔvapH° | 66.90 | kJ/mol | Joback Calculated Property |
IE | [11.20; 11.20] | eV |
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IE | 11.20 | eV | NIST |
IE | 11.20 | eV | NIST |
IE | 11.20 | eV | NIST |
log10WS | 0.38 | Aq. Sol... | |
logPoct/wat | -0.844 | Crippen Calculated Property | |
McVol | 53.920 | ml/mol | McGowan Calculated Property |
Pc | 8264.46 | kPa | Joback Calculated Property |
Inp | 748.00 | NIST | |
S°solid,1 bar | 115.60 | J/mol×K | NIST |
Tboil | 537.26 | K | Joback Calculated Property |
Tc | 716.26 | K | Joback Calculated Property |
Tfus | [374.65; 464.45] | K |
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Tfus | 374.65 | K | Aq. Sol... |
Tfus | 464.45 ± 1.50 | K | NIST |
Vc | 0.198 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [107.84; 123.35] | J/mol×K | [537.26; 716.26] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 110 115 120 550 600 650 700 | ||||
Cp,gas | 107.84 | J/mol×K | 537.26 | Joback Calculated Property |
Cp,gas | 110.79 | J/mol×K | 567.09 | Joback Calculated Property |
Cp,gas | 113.60 | J/mol×K | 596.93 | Joback Calculated Property |
Cp,gas | 116.25 | J/mol×K | 626.76 | Joback Calculated Property |
Cp,gas | 118.76 | J/mol×K | 656.60 | Joback Calculated Property |
Cp,gas | 121.13 | J/mol×K | 686.43 | Joback Calculated Property |
Cp,gas | 123.35 | J/mol×K | 716.26 | Joback Calculated Property |
Cp,solid | [105.90; 146.00] | J/mol×K | [298.10; 340.00] | ![]() |
Cp,solid | 120.10 | J/mol×K | 298.10 | NIST |
Cp,solid | 105.90 | J/mol×K | 298.15 | NIST |
Cp,solid | 118.00 | J/mol×K | 323.00 | NIST |
Cp,solid | 146.00 | J/mol×K | 340.00 | NIST |
η | [0.0000942; 0.0143582] | Pa×s | [333.80; 537.26] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 0.01 0.01 350 400 450 500 | ||||
η | 0.0143582 | Pa×s | 333.80 | Joback Calculated Property |
η | 0.0042222 | Pa×s | 367.71 | Joback Calculated Property |
η | 0.0015266 | Pa×s | 401.62 | Joback Calculated Property |
η | 0.0006467 | Pa×s | 435.53 | Joback Calculated Property |
η | 0.0003102 | Pa×s | 469.44 | Joback Calculated Property |
η | 0.0001642 | Pa×s | 503.35 | Joback Calculated Property |
η | 0.0000942 | Pa×s | 537.26 | Joback Calculated Property |
ΔsubH | [61.80; 90.60] | kJ/mol | [306.00; 355.50] | ![]() |
ΔsubH | 61.80 | kJ/mol | 306.00 | NIST |
ΔsubH | 90.60 | kJ/mol | 355.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [448.83; 691.18] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.20464e+01 | |||
Coefficient B | -3.82034e+03 | |||
Coefficient C | -1.23938e+02 | |||
Temperature range, min. | 448.83 | |||
Temperature range, max. | 691.18 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 500 600 | ||||
Pvap | 1.33 | kPa | 448.83 | Calculated Property |
Pvap | 3.28 | kPa | 475.76 | Calculated Property |
Pvap | 7.10 | kPa | 502.69 | Calculated Property |
Pvap | 13.86 | kPa | 529.61 | Calculated Property |
Pvap | 24.91 | kPa | 556.54 | Calculated Property |
Pvap | 41.80 | kPa | 583.47 | Calculated Property |
Pvap | 66.22 | kPa | 610.40 | Calculated Property |
Pvap | 99.98 | kPa | 637.32 | Calculated Property |
Pvap | 144.87 | kPa | 664.25 | Calculated Property |
Pvap | 202.65 | kPa | 691.18 | Calculated Property |
Pvap | [2.15; 7034.56] | kPa | [462.65; 804.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.87705e+02 | |||
Coefficient B | -1.97651e+04 | |||
Coefficient C | -2.37488e+01 | |||
Coefficient D | 7.12656e-06 | |||
Temperature range, min. | 462.65 | |||
Temperature range, max. | 804.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 7000 500 600 700 800 | ||||
Pvap | 2.15 | kPa | 462.65 | Calculated Property |
Pvap | 10.91 | kPa | 500.58 | Calculated Property |
Pvap | 41.14 | kPa | 538.51 | Calculated Property |
Pvap | 123.58 | kPa | 576.43 | Calculated Property |
Pvap | 311.75 | kPa | 614.36 | Calculated Property |
Pvap | 687.16 | kPa | 652.29 | Calculated Property |
Pvap | 1364.11 | kPa | 690.22 | Calculated Property |
Pvap | 2496.93 | kPa | 728.14 | Calculated Property |
Pvap | 4292.86 | kPa | 766.07 | Calculated Property |
Pvap | 7034.56 | kPa | 804.00 | Calculated Property |
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