Property | Value | Unit | Source |
---|---|---|---|
EA | 0.59 ± 0.01 | eV | NIST |
ΔfG° | 644.48 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 328.00 ± 11.00 | kJ/mol | NIST |
ΔfH°solid | 179.00 ± 10.00 | kJ/mol | NIST |
ΔfusH° | 24.50 | kJ/mol | Solid v... |
ΔsubH° | [142.00; 162.00] | kJ/mol | |
ΔsubH° | 148.90 ± 4.20 | kJ/mol | NIST |
ΔsubH° | 162.00 ± 6.00 | kJ/mol | NIST |
ΔsubH° | 162.00 ± 6.00 | kJ/mol | NIST |
ΔsubH° | 142.00 | kJ/mol | NIST |
ΔvapH° | 131.10 ± 1.40 | kJ/mol | NIST |
IE | [7.38; 7.80] | eV | |
IE | 7.39 ± 0.01 | eV | NIST |
IE | 7.38 ± 0.02 | eV | NIST |
IE | 7.60 ± 0.10 | eV | NIST |
IE | 7.57 | eV | NIST |
IE | 7.58 | eV | NIST |
IE | Outlier 7.80 | eV | NIST |
IE | 7.42 | eV | NIST |
IE | 7.38 | eV | NIST |
IE | 7.41 | eV | NIST |
IE | 7.38 ± 0.04 | eV | NIST |
log10WS | -8.69 | Crippen Calculated Property | |
logPoct/wat | 6.299 | Crippen Calculated Property | |
McVol | 219.240 | ml/mol | McGowan Calculated Property |
Pc | 2347.36 | kPa | Joback Calculated Property |
Inp | [488.20; 3137.00] | ||
Inp | 3089.00 | NIST | |
Inp | 3137.00 | NIST | |
Inp | 3137.00 | NIST | |
Inp | 3089.00 | NIST | |
Inp | 3095.00 | NIST | |
Inp | 3114.00 | NIST | |
Inp | 3080.00 | NIST | |
Inp | 3060.00 | NIST | |
Inp | 3108.00 | NIST | |
Inp | 3096.00 | NIST | |
Inp | 3099.00 | NIST | |
Inp | 3137.00 | NIST | |
Inp | 495.40 | NIST | |
Inp | 496.10 | NIST | |
Inp | 495.45 | NIST | |
Inp | 494.50 | NIST | |
Inp | 494.91 | NIST | |
Inp | 495.92 | NIST | |
Inp | 493.42 | NIST | |
Inp | 490.31 | NIST | |
Inp | 493.34 | NIST | |
Inp | 493.51 | NIST | |
Inp | 492.15 | NIST | |
Inp | 488.20 | NIST | |
Inp | 495.66 | NIST | |
Inp | 492.41 | NIST | |
Inp | 495.92 | NIST | |
Inp | 491.01 | NIST | |
Inp | 496.20 | NIST | |
Inp | 495.45 | NIST | |
Inp | 495.89 | NIST | |
Inp | 495.45 | NIST | |
Inp | 495.89 | NIST | |
Inp | 495.92 | NIST | |
Inp | 499.00 | NIST | |
Inp | 489.00 | NIST | |
Inp | 491.45 | NIST | |
Inp | 491.82 | NIST | |
Inp | 494.50 | NIST | |
Inp | 495.50 | NIST | |
Inp | 499.00 | NIST | |
Inp | 494.50 | NIST | |
Inp | 491.85 | NIST | |
Inp | 491.99 | NIST | |
Inp | 496.20 | NIST | |
Inp | 494.19 | NIST | |
Inp | 499.02 | NIST | |
Inp | 495.45 | NIST | |
Inp | 495.51 | NIST | |
Inp | 493.09 | NIST | |
Inp | 493.92 | NIST | |
Inp | 495.45 | NIST | |
Inp | 501.23 | NIST | |
Inp | 495.45 | NIST | |
Inp | 490.31 | NIST | |
Inp | 495.66 | NIST | |
Tboil | 797.20 | K | NIST |
Tc | 1089.89 | K | Joback Calculated Property |
Tfus | [533.15; 544.20] | K | |
Tfus | 544.20 ± 0.40 | K | NIST |
Tfus | 535.00 ± 5.00 | K | NIST |
Tfus | 537.65 ± 1.00 | K | NIST |
Tfus | 543.00 ± 2.00 | K | NIST |
Tfus | 533.15 ± 2.00 | K | NIST |
Vc | 0.848 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [607.64; 691.04] | J/mol×K | [820.30; 1089.89] | |
T(K) Ideal gas heat capacity (J/mol×K) 600 620 640 660 680 900 1000 | ||||
Cp,gas | 607.64 | J/mol×K | 820.30 | Joback Calculated Property |
Cp,gas | 622.45 | J/mol×K | 865.23 | Joback Calculated Property |
Cp,gas | 636.52 | J/mol×K | 910.16 | Joback Calculated Property |
Cp,gas | 650.13 | J/mol×K | 955.09 | Joback Calculated Property |
Cp,gas | 663.56 | J/mol×K | 1000.03 | Joback Calculated Property |
Cp,gas | 677.10 | J/mol×K | 1044.96 | Joback Calculated Property |
Cp,gas | 691.04 | J/mol×K | 1089.89 | Joback Calculated Property |
η | [0.0011148; 0.0022584] | Pa×s | [532.48; 820.30] | |
T(K) Dynamic viscosity (Pa×s) 1.20e-3 1.40e-3 1.60e-3 1.80e-3 2.00e-3 2.20e-3 600 700 800 | ||||
η | 0.0022584 | Pa×s | 532.48 | Joback Calculated Property |
η | 0.0019125 | Pa×s | 580.45 | Joback Calculated Property |
η | 0.0016611 | Pa×s | 628.42 | Joback Calculated Property |
η | 0.0014719 | Pa×s | 676.39 | Joback Calculated Property |
η | 0.0013254 | Pa×s | 724.36 | Joback Calculated Property |
η | 0.0012090 | Pa×s | 772.33 | Joback Calculated Property |
η | 0.0011148 | Pa×s | 820.30 | Joback Calculated Property |
ΔfusH | [28.40; 31.16] | kJ/mol | [539.70; 544.20] | |
ΔfusH | 28.40 | kJ/mol | 539.70 | NIST |
ΔfusH | 31.16 | kJ/mol | 544.20 | NIST |
ΔfusH | 31.16 | kJ/mol | 544.20 | NIST |
ΔsubH | 141.80 | kJ/mol | 459.50 | NIST |
ΔvapH | 99.40 | kJ/mol | 398.00 | NIST |
Pvap | [3.35e-10; 0.10] | kPa | [298.15; 510.00] | |
T(K) Vapor pressure (kPa) 0 0.02 0.04 0.06 0.08 0.1 300 400 500 | ||||
Pvap | 3.35e-10 | kPa | 298.15 | Hypothe... |
Pvap | 4.67e-10 | kPa | 300.00 | Hypothe... |
Pvap | 2.59e-09 | kPa | 310.00 | Hypothe... |
Pvap | 1.26e-08 | kPa | 320.00 | Hypothe... |
Pvap | 5.47e-08 | kPa | 330.00 | Hypothe... |
Pvap | 2.13e-07 | kPa | 340.00 | Hypothe... |
Pvap | 7.49e-07 | kPa | 350.00 | Hypothe... |
Pvap | 2.41e-06 | kPa | 360.00 | Hypothe... |
Pvap | 7.14e-06 | kPa | 370.00 | Hypothe... |
Pvap | 1.96e-05 | kPa | 380.00 | Hypothe... |
Pvap | 5.03e-05 | kPa | 390.00 | Hypothe... |
Pvap | 1.21e-04 | kPa | 400.00 | Hypothe... |
Pvap | 2.75e-04 | kPa | 410.00 | Hypothe... |
Pvap | 5.93e-04 | kPa | 420.00 | Hypothe... |
Pvap | 1.21e-03 | kPa | 430.00 | Hypothe... |
Pvap | 2.38e-03 | kPa | 440.00 | Hypothe... |
Pvap | 4.47e-03 | kPa | 450.00 | Hypothe... |
Pvap | 8.07e-03 | kPa | 460.00 | Hypothe... |
Pvap | 0.01 | kPa | 470.00 | Hypothe... |
Pvap | 0.02 | kPa | 480.00 | Hypothe... |
Pvap | 0.04 | kPa | 490.00 | Hypothe... |
Pvap | 0.06 | kPa | 500.00 | Hypothe... |
Pvap | 0.10 | kPa | 510.00 | Hypothe... |
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