Property | Value | Unit | Source |
---|---|---|---|
PAff | [828.90; 840.90] | kJ/mol |
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PAff | 840.90 | kJ/mol | NIST |
PAff | 828.90 | kJ/mol | NIST |
BasG | [804.60; 810.10] | kJ/mol |
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BasG | 810.10 | kJ/mol | NIST |
BasG | 804.60 | kJ/mol | NIST |
ΔcH°solid | -8943.40 ± 2.10 | kJ/mol | NIST |
EA | [0.32; 0.40] | eV |
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EA | 0.32 ± 0.01 | eV | NIST |
EA | 0.40 ± 0.01 | eV | NIST |
EA | 0.33 | eV | NIST |
ΔfG° | 513.78 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 268.70 ± 4.70 | kJ/mol | NIST |
ΔfH°solid | 145.30 ± 2.20 | kJ/mol | NIST |
ΔfusH° | 26.70 | kJ/mol | Joback Calculated Property |
ΔsubH° | [123.40; 131.00] | kJ/mol |
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ΔsubH° | 123.40 ± 4.20 | kJ/mol | NIST |
ΔsubH° | 131.00 ± 4.00 | kJ/mol | NIST |
ΔsubH° | 131.00 ± 4.00 | kJ/mol | NIST |
ΔvapH° | [97.00; 106.20] | kJ/mol |
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ΔvapH° | 106.20 | kJ/mol | NIST |
ΔvapH° | 97.00 ± 1.40 | kJ/mol | NIST |
IE | [7.59; 8.00] | eV |
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IE | 7.60 ± 0.01 | eV | NIST |
IE | 7.60 ± 0.03 | eV | NIST |
IE | Outlier 8.00 ± 0.20 | eV | NIST |
IE | 7.59 ± 0.05 | eV | NIST |
IE | 7.60 ± 0.01 | eV | NIST |
IE | Outlier 8.00 ± 0.30 | eV | NIST |
IE | 7.82 | eV | NIST |
IE | 7.83 | eV | NIST |
IE | 7.68 | eV | NIST |
IE | 7.75 | eV | NIST |
IE | 7.80 | eV | NIST |
IE | 7.78 | eV | NIST |
IE | 7.72 | eV | NIST |
IE | 7.59 ± 0.02 | eV | NIST |
IE | 7.59 | eV | NIST |
IE | 7.61 | eV | NIST |
log10WS | [-8.06; -8.06] |
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|
log10WS | -8.06 | Aq. Sol... | |
log10WS | -8.06 | Estimat... | |
logPoct/wat | 5.146 | Crippen Calculated Property | |
McVol | 182.340 | ml/mol | McGowan Calculated Property |
Pc | 2511.00 | kPa | KDB |
Inp | [2397.00; 2494.90] |
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|
Inp | 2406.00 | NIST | |
Inp | 2429.00 | NIST | |
Inp | 2438.00 | NIST | |
Inp | 2439.00 | NIST | |
Inp | 2447.00 | NIST | |
Inp | 2480.00 | NIST | |
Inp | 2486.00 | NIST | |
Inp | 2488.00 | NIST | |
Inp | 2491.00 | NIST | |
Inp | 2461.90 | NIST | |
Inp | 2408.00 | NIST | |
Inp | 2456.00 | NIST | |
Inp | 2489.00 | NIST | |
Inp | 2490.00 | NIST | |
Inp | 2472.30 | NIST | |
Inp | 2471.80 | NIST | |
Inp | 2434.20 | NIST | |
Inp | 2472.30 | NIST | |
Inp | 2494.90 | NIST | |
Inp | 2474.40 | NIST | |
Inp | 2442.66 | NIST | |
Inp | 2442.50 | NIST | |
Inp | 2434.20 | NIST | |
Inp | 2472.30 | NIST | |
Inp | 2494.90 | NIST | |
Inp | 2412.30 | NIST | |
Inp | 2471.80 | NIST | |
Inp | 2463.10 | NIST | |
Inp | 2432.20 | NIST | |
Inp | 2465.00 | NIST | |
Inp | 2454.00 | NIST | |
Inp | 2400.00 | NIST | |
Inp | 2400.00 | NIST | |
Inp | 2400.00 | NIST | |
Inp | 2400.00 | NIST | |
Inp | 2400.00 | NIST | |
Inp | 2413.00 | NIST | |
Inp | 2413.00 | NIST | |
Inp | 2413.00 | NIST | |
Inp | 2413.00 | NIST | |
Inp | 2422.00 | NIST | |
Inp | 2422.00 | NIST | |
Inp | 2424.00 | NIST | |
Inp | 2431.00 | NIST | |
Inp | 2434.00 | NIST | |
Inp | 2437.00 | NIST | |
Inp | 2397.00 | NIST | |
Inp | 2409.82 | NIST | |
Inp | 2471.68 | NIST | |
Inp | 2486.00 | NIST | |
Inp | 2443.00 | NIST | |
Inp | 2441.00 | NIST | |
Inp | 2401.00 | NIST | |
Inp | 2450.00 | NIST | |
Inp | 2451.00 | NIST | |
Inp | 2457.00 | NIST | |
Inp | 2458.00 | NIST | |
Inp | 2462.00 | NIST | |
Inp | 2463.00 | NIST | |
Inp | 2491.00 | NIST | |
Inp | 2492.00 | NIST | |
Inp | 2428.00 | NIST | |
Inp | 2453.00 | NIST | |
Inp | 2456.00 | NIST | |
Inp | 2411.00 | NIST | |
Inp | 2465.00 | NIST | |
Inp | 2472.30 | NIST | |
Inp | 2474.40 | NIST | |
Inp | 2494.90 | NIST | |
Inp | 2465.00 | NIST | |
Inp | 2400.00 | NIST | |
Inp | 2413.00 | NIST | |
Inp | 2434.00 | NIST | |
Inp | 2406.00 | NIST | |
Inp | 2480.00 | NIST | |
Inp | 2408.00 | NIST | |
Inp | 2411.00 | NIST | |
Tboil | [721.15; 721.20] | K |
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Tboil | 721.15 | K | KDB |
Tboil | 721.20 | K | NIST |
Tc | 984.20 | K | KDB |
Tfus | [527.35; 531.40] | K |
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Tfus | 529.18 | K | Aq. Sol... |
Tfus | 528.90 | K | KDB |
Tfus | Outlier 531.40 ± 0.20 | K | NIST |
Tfus | 529.00 ± 2.00 | K | NIST |
Tfus | 527.35 ± 1.00 | K | NIST |
Tfus | 529.20 ± 1.00 | K | NIST |
Tfus | 527.90 ± 0.50 | K | NIST |
Vc | 0.700 | m3/kmol | KDB |
Zc | 0.2147950 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [468.00; 543.24] | J/mol×K | [704.82; 968.39] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 480 500 520 540 700 800 900 | ||||
Cp,gas | 468.00 | J/mol×K | 704.82 | Joback Calculated Property |
Cp,gas | 482.86 | J/mol×K | 748.75 | Joback Calculated Property |
Cp,gas | 496.51 | J/mol×K | 792.68 | Joback Calculated Property |
Cp,gas | 509.15 | J/mol×K | 836.61 | Joback Calculated Property |
Cp,gas | 521.02 | J/mol×K | 880.54 | Joback Calculated Property |
Cp,gas | 532.31 | J/mol×K | 924.47 | Joback Calculated Property |
Cp,gas | 543.24 | J/mol×K | 968.39 | Joback Calculated Property |
η | [0.0007153; 0.0017235] | Pa×s | [442.18; 704.82] | ![]() |
T(K) Dynamic viscosity (Pa×s) 8.00e-4 1.00e-3 1.20e-3 1.40e-3 1.60e-3 1.80e-3 500 600 700 | ||||
η | 0.0017235 | Pa×s | 442.18 | Joback Calculated Property |
η | 0.0013935 | Pa×s | 485.95 | Joback Calculated Property |
η | 0.0011669 | Pa×s | 529.73 | Joback Calculated Property |
η | 0.0010040 | Pa×s | 573.50 | Joback Calculated Property |
η | 0.0008825 | Pa×s | 617.27 | Joback Calculated Property |
η | 0.0007890 | Pa×s | 661.05 | Joback Calculated Property |
η | 0.0007153 | Pa×s | 704.82 | Joback Calculated Property |
ΔfusH | [3.22; 26.15] | kJ/mol | [512.20; 531.40] | ![]() |
ΔfusH | 3.22 | kJ/mol | 512.20 | NIST |
ΔfusH | 23.60 | kJ/mol | 527.00 | NIST |
ΔfusH | 26.15 | kJ/mol | 531.40 | NIST |
ΔfusH | 26.15 | kJ/mol | 531.40 | NIST |
ΔsubH | [118.00; 121.40] | kJ/mol | [293.00; 400.00] | ![]() |
T(K) Enthalpy of sublimation at a given temperature (kJ/mol) 118 118.5 119 119.5 120 120.5 121 121.5 300 350 400 | ||||
ΔsubH | 118.00 | kJ/mol | 293.00 | NIST |
ΔsubH | 119.00 | kJ/mol | 353.00 | NIST |
ΔsubH | 118.80 | kJ/mol | 383.00 | NIST |
ΔsubH | 121.40 | kJ/mol | 385.50 | NIST |
ΔsubH | 118.00 ± 4.00 | kJ/mol | 400.00 | NIST |
ΔvapH | [89.60; 106.18] | kJ/mol | [298.00; 398.00] | ![]() |
ΔvapH | 106.18 | kJ/mol | 298.00 | Enthalp... |
ΔvapH | 89.60 | kJ/mol | 398.00 | NIST |
Psub | [1.74e-05; 3.79e-04] | kPa | [372.40; 408.60] | ![]() |
T(K) Sublimation pressure (kPa) 0 5.00e-5 1.00e-4 1.50e-4 2.00e-4 2.50e-4 3.00e-4 3.50e-4 4.00e-4 380 390 400 | ||||
Psub | 1.74e-05 | kPa | 372.40 | Vapor P... |
Psub | 3.72e-05 | kPa | 380.70 | Vapor P... |
Psub | 5.37e-05 | kPa | 385.20 | Vapor P... |
Psub | 7.61e-05 | kPa | 389.20 | Vapor P... |
Psub | 7.50e-05 | kPa | 389.40 | Vapor P... |
Psub | 1.03e-04 | kPa | 393.60 | Vapor P... |
Psub | 1.36e-04 | kPa | 394.20 | Vapor P... |
Psub | 1.48e-04 | kPa | 396.10 | Vapor P... |
Psub | 1.68e-04 | kPa | 398.10 | Vapor P... |
Psub | 1.58e-04 | kPa | 398.20 | Vapor P... |
Psub | 2.02e-04 | kPa | 400.00 | Vapor P... |
Psub | 2.12e-04 | kPa | 400.40 | Vapor P... |
Psub | 2.63e-04 | kPa | 402.80 | Vapor P... |
Psub | 2.54e-04 | kPa | 403.00 | Vapor P... |
Psub | 2.77e-04 | kPa | 404.80 | Vapor P... |
Psub | 2.92e-04 | kPa | 404.90 | Vapor P... |
Psub | 3.06e-04 | kPa | 405.10 | Vapor P... |
Psub | 3.36e-04 | kPa | 406.80 | Vapor P... |
Psub | 3.79e-04 | kPa | 408.60 | Vapor P... |
ρl | 1278.44 | kg/m3 | 293.10 | KDB |
ΔfusS | [6.29; 49.21] | J/mol×K | [512.20; 531.40] | ![]() |
ΔfusS | 6.29 | J/mol×K | 512.20 | NIST |
ΔfusS | 49.21 | J/mol×K | 531.40 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.32; 201.39] | kPa | [538.15; 766.15] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.44202e+01 | |||
Coefficient B | -5.84669e+03 | |||
Coefficient C | -1.24711e+02 | |||
Temperature range, min. | 538.15 | |||
Temperature range, max. | 766.15 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 600 700 | ||||
Pvap | 1.32 | kPa | 538.15 | Calculated Property |
Pvap | 2.99 | kPa | 563.48 | Calculated Property |
Pvap | 6.19 | kPa | 588.82 | Calculated Property |
Pvap | 11.88 | kPa | 614.15 | Calculated Property |
Pvap | 21.38 | kPa | 639.48 | Calculated Property |
Pvap | 36.42 | kPa | 664.82 | Calculated Property |
Pvap | 59.15 | kPa | 690.15 | Calculated Property |
Pvap | 92.16 | kPa | 715.48 | Calculated Property |
Pvap | 138.44 | kPa | 740.82 | Calculated Property |
Pvap | 201.39 | kPa | 766.15 | Calculated Property |
Pvap | [1.03; 2366.14] | kPa | [531.15; 979.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.25778e+02 | |||
Coefficient B | -1.72689e+04 | |||
Coefficient C | -1.49941e+01 | |||
Coefficient D | 3.01277e-06 | |||
Temperature range, min. | 531.15 | |||
Temperature range, max. | 979.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 600 700 800 900 | ||||
Pvap | 1.03 | kPa | 531.15 | Calculated Property |
Pvap | 5.14 | kPa | 580.91 | Calculated Property |
Pvap | 18.75 | kPa | 630.67 | Calculated Property |
Pvap | 54.12 | kPa | 680.43 | Calculated Property |
Pvap | 130.84 | kPa | 730.19 | Calculated Property |
Pvap | 276.09 | kPa | 779.96 | Calculated Property |
Pvap | 524.57 | kPa | 829.72 | Calculated Property |
Pvap | 918.84 | kPa | 879.48 | Calculated Property |
Pvap | 1510.99 | kPa | 929.24 | Calculated Property |
Pvap | 2366.14 | kPa | 979.00 | Calculated Property |
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