Property | Value | Unit | Source |
---|---|---|---|
ω | 0.9890 | KDB | |
ΔcH°solid | -8517.80 ± 0.90 | kJ/mol | NIST |
ΔfG° | -78.24 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -463.88 | kJ/mol | Joback Calculated Property |
ΔfH°solid | -599.50 ± 0.90 | kJ/mol | NIST |
ΔfusH° | [1.50; 94.70] | kJ/mol |
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ΔfusH° | 1.50 | kJ/mol | Heat ca... |
ΔfusH° | 94.70 | kJ/mol | Evaluat... |
ΔvapH° | [94.70; 95.80] | kJ/mol |
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ΔvapH° | 94.70 ± 0.40 | kJ/mol | NIST |
ΔvapH° | 95.80 | kJ/mol | NIST |
log10WS | -4.53 | Crippen Calculated Property | |
logPoct/wat | 4.290 | Crippen Calculated Property | |
McVol | 199.900 | ml/mol | McGowan Calculated Property |
NFPA Fire | 1 | KDB | |
Pc | 1935.00 | kPa | KDB |
Inp | [220.20; 1599.00] |
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|
Inp | 1563.60 | NIST | |
Inp | 1585.50 | NIST | |
Inp | 1577.00 | NIST | |
Inp | 1565.00 | NIST | |
Inp | 1560.00 | NIST | |
Inp | 1563.00 | NIST | |
Inp | 1575.00 | NIST | |
Inp | 1572.00 | NIST | |
Inp | 1585.30 | NIST | |
Inp | 1580.00 | NIST | |
Inp | 1580.00 | NIST | |
Inp | 1556.00 | NIST | |
Inp | 1585.00 | NIST | |
Inp | 1593.00 | NIST | |
Inp | 1547.00 | NIST | |
Inp | 1577.00 | NIST | |
Inp | 1577.00 | NIST | |
Inp | 1569.00 | NIST | |
Inp | 1577.00 | NIST | |
Inp | 1586.00 | NIST | |
Inp | 1586.00 | NIST | |
Inp | 1585.00 | NIST | |
Inp | 1577.00 | NIST | |
Inp | 1572.00 | NIST | |
Inp | 1580.00 | NIST | |
Inp | 1577.00 | NIST | |
Inp | 1565.00 | NIST | |
Inp | 1599.00 | NIST | |
Inp | Outlier 266.83 | NIST | |
Inp | Outlier 268.36 | NIST | |
Inp | Outlier 220.20 | NIST | |
Inp | 1575.00 | NIST | |
Inp | Outlier 266.83 | NIST | |
Inp | 1580.00 | NIST | |
Inp | 1547.00 | NIST | |
I | [2033.00; 2093.00] |
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|
I | 2033.00 | NIST | |
I | 2074.00 | NIST | |
I | 2076.00 | NIST | |
I | 2034.00 | NIST | |
I | 2093.00 | NIST | |
I | 2041.00 | NIST | |
I | 2041.00 | NIST | |
I | 2077.00 | NIST | |
I | 2063.00 | NIST | |
I | 2078.00 | NIST | |
I | 2077.00 | NIST | |
I | 2077.00 | NIST | |
I | 2034.00 | NIST | |
Tboil | 547.20 | K | KDB |
Tc | 734.00 | K | KDB |
Tfus | [301.70; 305.60] | K |
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Tfus | 305.60 | K | KDB |
Tfus | 303.05 ± 0.50 | K | NIST |
Tfus | 301.70 ± 1.00 | K | NIST |
Tfus | 304.89 ± 0.05 | K | NIST |
Tfus | 304.63 ± 0.04 | K | NIST |
Tfus | 303.50 ± 0.05 | K | NIST |
Vc | 0.782 | m3/kmol | KDB |
Zc | 0.2481030 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [529.76; 612.65] | J/mol×K | [589.02; 746.78] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 540 560 580 600 620 600 650 700 750 | ||||
Cp,gas | 529.76 | J/mol×K | 589.02 | Joback Calculated Property |
Cp,gas | 545.01 | J/mol×K | 615.31 | Joback Calculated Property |
Cp,gas | 559.66 | J/mol×K | 641.61 | Joback Calculated Property |
Cp,gas | 573.73 | J/mol×K | 667.90 | Joback Calculated Property |
Cp,gas | 587.24 | J/mol×K | 694.19 | Joback Calculated Property |
Cp,gas | 600.21 | J/mol×K | 720.48 | Joback Calculated Property |
Cp,gas | 612.65 | J/mol×K | 746.78 | Joback Calculated Property |
Cp,liquid | [476.00; 487.50] | J/mol×K | [305.00; 313.15] | ![]() |
Cp,liquid | 476.00 | J/mol×K | 305.00 | NIST |
Cp,liquid | 487.50 | J/mol×K | 313.15 | NIST |
Cp,solid | 378.00 | J/mol×K | 298.15 | NIST |
η | [0.0000718; 0.0163656] | Pa×s | [297.09; 589.02] | ![]() |
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 0.02 300 400 500 | ||||
η | 0.0163656 | Pa×s | 297.09 | Joback Calculated Property |
η | 0.0035036 | Pa×s | 345.75 | Joback Calculated Property |
η | 0.0010971 | Pa×s | 394.40 | Joback Calculated Property |
η | 0.0004434 | Pa×s | 443.06 | Joback Calculated Property |
η | 0.0002143 | Pa×s | 491.71 | Joback Calculated Property |
η | 0.0001181 | Pa×s | 540.37 | Joback Calculated Property |
η | 0.0000718 | Pa×s | 589.02 | Joback Calculated Property |
ΔfusH | [18.74; 44.78] | kJ/mol | [304.70; 306.60] | ![]() |
ΔfusH | 44.78 | kJ/mol | 304.70 | NIST |
ΔfusH | 18.74 | kJ/mol | 306.60 | NIST |
ΔvapH | [69.20; 91.10] | kJ/mol | [327.50; 499.50] | ![]() |
ΔvapH | 91.10 | kJ/mol | 327.50 | NIST |
ΔvapH | 87.40 | kJ/mol | 343.00 | NIST |
ΔvapH | 69.20 | kJ/mol | 499.50 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 428.70 | K | 2.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [429.88; 566.36] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.76371e+01 | |||
Coefficient B | -5.80912e+03 | |||
Coefficient C | -9.50510e+01 | |||
Temperature range, min. | 429.88 | |||
Temperature range, max. | 566.36 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
Pvap | 1.33 | kPa | 429.88 | Calculated Property |
Pvap | 2.83 | kPa | 445.04 | Calculated Property |
Pvap | 5.63 | kPa | 460.21 | Calculated Property |
Pvap | 10.62 | kPa | 475.37 | Calculated Property |
Pvap | 19.08 | kPa | 490.54 | Calculated Property |
Pvap | 32.82 | kPa | 505.70 | Calculated Property |
Pvap | 54.31 | kPa | 520.87 | Calculated Property |
Pvap | 86.82 | kPa | 536.03 | Calculated Property |
Pvap | 134.54 | kPa | 551.20 | Calculated Property |
Pvap | 202.67 | kPa | 566.36 | Calculated Property |
Pvap | [1.27e-04; 1887.26] | kPa | [303.75; 731.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.67240e+02 | |||
Coefficient B | -2.16241e+04 | |||
Coefficient C | -3.61080e+01 | |||
Coefficient D | 1.49630e-05 | |||
Temperature range, min. | 303.75 | |||
Temperature range, max. | 731.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 400 600 | ||||
Pvap | 1.27e-04 | kPa | 303.75 | Calculated Property |
Pvap | 0.02 | kPa | 351.22 | Calculated Property |
Pvap | 0.43 | kPa | 398.69 | Calculated Property |
Pvap | 4.34 | kPa | 446.17 | Calculated Property |
Pvap | 23.24 | kPa | 493.64 | Calculated Property |
Pvap | 82.14 | kPa | 541.11 | Calculated Property |
Pvap | 220.87 | kPa | 588.58 | Calculated Property |
Pvap | 497.07 | kPa | 636.06 | Calculated Property |
Pvap | 1000.37 | kPa | 683.53 | Calculated Property |
Pvap | 1887.26 | kPa | 731.00 | Calculated Property |
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