Property | Value | Unit | Source |
---|---|---|---|
PAff | 836.70 | kJ/mol | NIST |
BasG | 805.70 | kJ/mol | NIST |
ΔcH°solid | [-3868.00; -3862.30] | kJ/mol |
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ΔcH°solid | -3862.30 ± 0.90 | kJ/mol | NIST |
ΔcH°solid | -3862.30 ± 0.92 | kJ/mol | NIST |
ΔcH°solid | -3868.00 | kJ/mol | NIST |
ΔfG° | -146.48 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-330.40; -324.50] | kJ/mol |
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ΔfH°gas | -330.40 ± 1.50 | kJ/mol | NIST |
ΔfH°gas | -330.40 | kJ/mol | NIST |
ΔfH°gas | -324.50 | kJ/mol | NIST |
ΔfH°solid | [-429.20; -423.30] | kJ/mol |
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ΔfH°solid | -429.20 ± 1.50 | kJ/mol | NIST |
ΔfH°solid | -429.20 ± 1.10 | kJ/mol | NIST |
ΔfH°solid | -423.30 ± 3.80 | kJ/mol | NIST |
ΔfusH° | 22.48 | kJ/mol | Thermod... |
ΔsubH° | [98.60; 98.80] | kJ/mol |
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ΔsubH° | 98.60 ± 0.60 | kJ/mol | NIST |
ΔsubH° | 98.80 ± 0.30 | kJ/mol | NIST |
ΔsubH° | 98.80 ± 0.30 | kJ/mol | NIST |
ΔsubH° | 98.80 | kJ/mol | NIST |
ΔvapH° | 59.77 | kJ/mol | Joback Calculated Property |
IE | [9.20; 9.40] | eV |
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IE | 9.20 ± 0.20 | eV | NIST |
IE | 9.40 | eV | NIST |
log10WS | -2.60 | Aq. Sol... | |
logPoct/wat | 1.693 | Crippen Calculated Property | |
McVol | 107.260 | ml/mol | McGowan Calculated Property |
Pc | 4356.87 | kPa | Joback Calculated Property |
Inp | [1213.00; 1213.00] |
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|
Inp | 1213.00 | NIST | |
Inp | 1213.00 | NIST | |
Inp | 1213.00 | NIST | |
Tboil | 547.70 | K | NIST |
Tc | 775.00 | K | Vapor-l... |
Tfus | [450.15; 455.10] | K |
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Tfus | 453.46 | K | Aq. Sol... |
Tfus | 453.30 | K | Benzoic... |
Tfus | 455.10 | K | Solid-L... |
Tfus | 455.00 ± 2.00 | K | NIST |
Tfus | 450.15 ± 2.50 | K | NIST |
Tfus | 452.80 ± 0.30 | K | NIST |
Vc | 0.401 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [235.84; 283.75] | J/mol×K | [560.15; 767.50] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 240 250 260 270 280 600 650 700 750 | ||||
Cp,gas | 235.84 | J/mol×K | 560.15 | Joback Calculated Property |
Cp,gas | 245.16 | J/mol×K | 594.71 | Joback Calculated Property |
Cp,gas | 253.91 | J/mol×K | 629.27 | Joback Calculated Property |
Cp,gas | 262.13 | J/mol×K | 663.82 | Joback Calculated Property |
Cp,gas | 269.83 | J/mol×K | 698.38 | Joback Calculated Property |
Cp,gas | 277.03 | J/mol×K | 732.94 | Joback Calculated Property |
Cp,gas | 283.75 | J/mol×K | 767.50 | Joback Calculated Property |
Cp,solid | 169.00 | J/mol×K | 298.00 | NIST |
η | [0.0001208; 0.0051891] | Pa×s | [329.61; 560.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 400 500 | ||||
η | 0.0051891 | Pa×s | 329.61 | Joback Calculated Property |
η | 0.0019990 | Pa×s | 368.03 | Joback Calculated Property |
η | 0.0009222 | Pa×s | 406.46 | Joback Calculated Property |
η | 0.0004863 | Pa×s | 444.88 | Joback Calculated Property |
η | 0.0002839 | Pa×s | 483.30 | Joback Calculated Property |
η | 0.0001794 | Pa×s | 521.73 | Joback Calculated Property |
η | 0.0001208 | Pa×s | 560.15 | Joback Calculated Property |
ΔfusH | [22.72; 22.72] | kJ/mol | [452.80; 452.80] | ![]() |
ΔfusH | 22.72 | kJ/mol | 452.80 | NIST |
ΔfusH | 22.72 | kJ/mol | 452.80 | NIST |
ΔfusH | 22.72 | kJ/mol | 452.80 | NIST |
ΔfusS | 50.20 | J/mol×K | 452.80 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [421.56; 577.86] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.54810e+01 | |||
Coefficient B | -4.80703e+03 | |||
Coefficient C | -1.05173e+02 | |||
Temperature range, min. | 421.56 | |||
Temperature range, max. | 577.86 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
Pvap | 1.33 | kPa | 421.56 | Calculated Property |
Pvap | 2.94 | kPa | 438.93 | Calculated Property |
Pvap | 5.99 | kPa | 456.29 | Calculated Property |
Pvap | 11.42 | kPa | 473.66 | Calculated Property |
Pvap | 20.55 | kPa | 491.03 | Calculated Property |
Pvap | 35.14 | kPa | 508.39 | Calculated Property |
Pvap | 57.49 | kPa | 525.76 | Calculated Property |
Pvap | 90.46 | kPa | 543.13 | Calculated Property |
Pvap | 137.49 | kPa | 560.49 | Calculated Property |
Pvap | 202.64 | kPa | 577.86 | Calculated Property |
Pvap | [5.17; 3829.19] | kPa | [452.75; 773.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.46674e+02 | |||
Coefficient B | -1.53125e+04 | |||
Coefficient C | -1.83932e+01 | |||
Coefficient D | 6.20185e-06 | |||
Temperature range, min. | 452.75 | |||
Temperature range, max. | 773.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 500 600 700 | ||||
Pvap | 5.17 | kPa | 452.75 | Calculated Property |
Pvap | 18.61 | kPa | 488.33 | Calculated Property |
Pvap | 53.69 | kPa | 523.92 | Calculated Property |
Pvap | 130.64 | kPa | 559.50 | Calculated Property |
Pvap | 278.55 | kPa | 595.08 | Calculated Property |
Pvap | 535.78 | kPa | 630.67 | Calculated Property |
Pvap | 950.63 | kPa | 666.25 | Calculated Property |
Pvap | 1583.31 | kPa | 701.83 | Calculated Property |
Pvap | 2509.94 | kPa | 737.42 | Calculated Property |
Pvap | 3829.19 | kPa | 773.00 | Calculated Property |
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