Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2430 | KDB | |
AP | 316.950 | K | KDB |
ΔcH°liquid | -5222.60 ± 1.50 | kJ/mol | NIST |
μ | 0.00 | debye | KDB |
ΔfG° | 39.27 | kJ/mol | KDB |
Δc,grossH | 5222.59 | kJ/mol | KDB |
Δc,netH | 4870.511 | kJ/mol | KDB |
ΔfH°gas | [-172.60; -171.80] | kJ/mol |
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ΔfH°gas | -171.90 | kJ/mol | KDB |
ΔfH°gas | -172.60 | kJ/mol | NIST |
ΔfH°gas | -171.80 ± 1.50 | kJ/mol | NIST |
ΔfH°liquid | [-213.00; -212.20] | kJ/mol |
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ΔfH°liquid | -213.00 | kJ/mol | NIST |
ΔfH°liquid | -212.20 ± 1.50 | kJ/mol | NIST |
ΔfusH° | 8.31 | kJ/mol | Joback Calculated Property |
ΔvapH° | 33.83 | kJ/mol | Joback Calculated Property |
IE | [9.54; 9.67] | eV |
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IE | 9.54 | eV | NIST |
IE | 9.67 ± 0.02 | eV | NIST |
log10WS | [-4.25; -4.25] |
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|
log10WS | -4.25 | Aq. Sol... | |
log10WS | -4.25 | Estimat... | |
logPoct/wat | 2.977 | Crippen Calculated Property | |
McVol | 112.720 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
NFPA Health | 1 | KDB | |
Pc | [3000.00; 3250.00] | kPa |
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Pc | 3000.00 | kPa | KDB |
Pc | 3250.00 | kPa | Critica... |
Inp | [818.00; 867.90] |
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|
Inp | 846.00 | NIST | |
Inp | 851.00 | NIST | |
Inp | 829.00 | NIST | |
Inp | 842.20 | NIST | |
Inp | Outlier 859.70 | NIST | |
Inp | Outlier 867.90 | NIST | |
Inp | 828.00 | NIST | |
Inp | 833.60 | NIST | |
Inp | 839.00 | NIST | |
Inp | 843.00 | NIST | |
Inp | 834.30 | NIST | |
Inp | 842.80 | NIST | |
Inp | 831.30 | NIST | |
Inp | 831.70 | NIST | |
Inp | 853.00 | NIST | |
Inp | 837.00 | NIST | |
Inp | 838.00 | NIST | |
Inp | 848.00 | NIST | |
Inp | 842.00 | NIST | |
Inp | 842.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 840.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 840.00 | NIST | |
Inp | 832.00 | NIST | |
Inp | 836.00 | NIST | |
Inp | 838.00 | NIST | |
Inp | 841.00 | NIST | |
Inp | 844.00 | NIST | |
Inp | 834.30 | NIST | |
Inp | 832.00 | NIST | |
Inp | Outlier 856.00 | NIST | |
Inp | 842.00 | NIST | |
Inp | 825.00 | NIST | |
Inp | 828.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 839.00 | NIST | |
Inp | 845.00 | NIST | |
Inp | 839.00 | NIST | |
Inp | 839.00 | NIST | |
Inp | 839.00 | NIST | |
Inp | 839.00 | NIST | |
Inp | 842.00 | NIST | |
Inp | 835.92 | NIST | |
Inp | 824.00 | NIST | |
Inp | 843.00 | NIST | |
Inp | 845.00 | NIST | |
Inp | Outlier 854.00 | NIST | |
Inp | 840.00 | NIST | |
Inp | 832.00 | NIST | |
Inp | 841.00 | NIST | |
Inp | 832.20 | NIST | |
Inp | 829.10 | NIST | |
Inp | 828.40 | NIST | |
Inp | 826.90 | NIST | |
Inp | 829.10 | NIST | |
Inp | 830.90 | NIST | |
Inp | 838.10 | NIST | |
Inp | 830.10 | NIST | |
Inp | Outlier 818.00 | NIST | |
Inp | 826.90 | NIST | |
Inp | 829.10 | NIST | |
Inp | 830.90 | NIST | |
Inp | 829.10 | NIST | |
Inp | 828.40 | NIST | |
Inp | 827.00 | NIST | |
Inp | 821.60 | NIST | |
Inp | 824.96 | NIST | |
Inp | 827.15 | NIST | |
Inp | 827.11 | NIST | |
Inp | 830.63 | NIST | |
Inp | 832.99 | NIST | |
Inp | 841.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 828.00 | NIST | |
Inp | 833.00 | NIST | |
Inp | 843.00 | NIST | |
Inp | 833.00 | NIST | |
Inp | 836.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 827.00 | NIST | |
Inp | 831.70 | NIST | |
Inp | 834.00 | NIST | |
Inp | 825.00 | NIST | |
Inp | 835.00 | NIST | |
Inp | 837.90 | NIST | |
Inp | 841.40 | NIST | |
Inp | 844.00 | NIST | |
Inp | 846.20 | NIST | |
Inp | 825.00 | NIST | |
Inp | 824.00 | NIST | |
Inp | 837.00 | NIST | |
Inp | 839.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 831.00 | NIST | |
Inp | 827.00 | NIST | |
Inp | 827.00 | NIST | |
Inp | 840.00 | NIST | |
Inp | 837.00 | NIST | |
Inp | 827.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 840.00 | NIST | |
Inp | 834.00 | NIST | |
I | [885.00; 925.20] |
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|
I | 920.00 | NIST | |
I | 915.00 | NIST | |
I | 920.00 | NIST | |
I | 925.20 | NIST | |
I | 905.50 | NIST | |
I | 910.10 | NIST | |
I | 920.00 | NIST | |
I | Outlier 885.00 | NIST | |
I | 920.00 | NIST | |
I | 910.10 | NIST | |
S°gas | 382.67 | J/mol×K | NIST |
S°liquid | [280.91; 281.60] | J/mol×K |
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S°liquid | 280.91 | J/mol×K | NIST |
S°liquid | 281.60 | J/mol×K | NIST |
Tboil | 404.90 | K | KDB |
Tc | [606.90; 609.00] | K |
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Tc | 609.00 | K | KDB |
Tc | 606.90 | K | Gas-Liq... |
Tc | 609.00 | K | NIST |
Tfus | [161.80; 162.00] | K |
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Tfus | 161.80 | K | KDB |
Tfus | 162.00 | K | Aq. Sol... |
Ttriple | [161.40; 161.84] | K |
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Ttriple | 161.84 ± 0.05 | K | NIST |
Ttriple | 161.40 ± 0.20 | K | NIST |
Vc | 0.450 | m3/kmol | KDB |
Zc | 0.2666120 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [152.23; 239.88] | J/mol×K | [298.15; 448.15] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 160 180 200 220 240 300 350 400 450 | ||||
Cp,gas | 152.23 | J/mol×K | 298.15 | NIST |
Cp,gas | 170.36 | J/mol×K | 323.15 | NIST |
Cp,gas | 197.90 | J/mol×K | 373.15 | NIST |
Cp,gas | 217.63 | J/mol×K | 408.15 | NIST |
Cp,gas | 239.88 | J/mol×K | 448.15 | NIST |
Cp,liquid | [211.79; 214.20] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 211.79 | J/mol×K | 298.15 | NIST |
Cp,liquid | 214.20 | J/mol×K | 298.15 | NIST |
η | [0.0002793; 0.0082639] | Pa×s | [187.30; 401.99] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 200 300 400 | ||||
η | 0.0082639 | Pa×s | 187.30 | Joback Calculated Property |
η | 0.0029878 | Pa×s | 223.08 | Joback Calculated Property |
η | 0.0014311 | Pa×s | 258.86 | Joback Calculated Property |
η | 0.0008196 | Pa×s | 294.64 | Joback Calculated Property |
η | 0.0005297 | Pa×s | 330.43 | Joback Calculated Property |
η | 0.0003728 | Pa×s | 366.21 | Joback Calculated Property |
η | 0.0002793 | Pa×s | 401.99 | Joback Calculated Property |
ΔfusH | [8.28; 8.50] | kJ/mol | [161.40; 161.84] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 8.3 8.35 8.4 8.45 8.5 161.4 161.60000000000002 161.8 | ||||
ΔfusH | 8.33 | kJ/mol | 161.40 | NIST |
ΔfusH | 8.28 | kJ/mol | 161.40 | NIST |
ΔfusH | 8.28 | kJ/mol | 161.40 | NIST |
ΔfusH | 8.50 | kJ/mol | 161.50 | NIST |
ΔfusH | 8.33 | kJ/mol | 161.84 | NIST |
ΔvapH | [34.04; 39.80] | kJ/mol | [313.00; 405.00] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 34 35 36 37 38 39 40 350 400 | ||||
ΔvapH | 39.80 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 38.90 ± 0.10 | kJ/mol | 328.00 | NIST |
ΔvapH | 37.90 ± 0.10 | kJ/mol | 343.00 | NIST |
ΔvapH | 37.00 ± 0.10 | kJ/mol | 358.00 | NIST |
ΔvapH | 38.60 | kJ/mol | 365.00 | NIST |
ΔvapH | 36.30 ± 0.10 | kJ/mol | 368.00 | NIST |
ΔvapH | 34.31 | kJ/mol | 404.90 | KDB |
ΔvapH | 34.04 | kJ/mol | 405.00 | NIST |
Pvap | [2.10; 73.20] | kPa | [303.15; 393.15] | ![]() |
T(K) Vapor pressure (kPa) 0 10 20 30 40 50 60 70 80 320 340 360 380 | ||||
Pvap | 2.10 | kPa | 303.15 | Bubble ... |
Pvap | 3.70 | kPa | 313.15 | Bubble ... |
Pvap | 6.00 | kPa | 323.15 | Bubble ... |
Pvap | 9.30 | kPa | 333.15 | Bubble ... |
Pvap | 13.90 | kPa | 343.15 | Bubble ... |
Pvap | 20.40 | kPa | 353.15 | Bubble ... |
Pvap | 28.90 | kPa | 363.15 | Bubble ... |
Pvap | 40.30 | kPa | 373.15 | Bubble ... |
Pvap | 54.80 | kPa | 383.15 | Bubble ... |
Pvap | 73.20 | kPa | 393.15 | Bubble ... |
n0 | [1.42750; 1.43073] | [293.15; 298.15] | ![]() |
|
n0 | 1.42750 | 293.15 | Density... | |
n0 | 1.43073 | 298.15 | KDB | |
ρl | [747.03; 788.02] | kg/m3 | [293.00; 343.15] | ![]() |
T(K) Liquid Density (kg/m3) 750 760 770 780 790 300 320 340 | ||||
ρl | 788.00 | kg/m3 | 293.00 | KDB |
ρl | 787.98 | kg/m3 | 293.15 | Densiti... |
ρl | 787.98 | kg/m3 | 293.15 | Densiti... |
ρl | 787.98 | kg/m3 | 293.15 | Density... |
ρl | 788.02 | kg/m3 | 293.15 | Excess ... |
ρl | 783.97 | kg/m3 | 298.15 | Densiti... |
ρl | 783.95 | kg/m3 | 298.15 | Density... |
ρl | 784.01 | kg/m3 | 298.15 | Excess ... |
ρl | 779.93 | kg/m3 | 303.15 | Densiti... |
ρl | 779.98 | kg/m3 | 303.15 | Excess ... |
ρl | 779.91 | kg/m3 | 303.15 | Densiti... |
ρl | 779.92 | kg/m3 | 303.15 | Density... |
ρl | 775.88 | kg/m3 | 308.15 | Densiti... |
ρl | 775.87 | kg/m3 | 308.15 | Density... |
ρl | 775.93 | kg/m3 | 308.15 | Excess ... |
ρl | 771.82 | kg/m3 | 313.15 | Densiti... |
ρl | 771.79 | kg/m3 | 313.15 | Densiti... |
ρl | 771.86 | kg/m3 | 313.15 | Excess ... |
ρl | 771.80 | kg/m3 | 313.15 | Density... |
ρl | 767.69 | kg/m3 | 318.15 | Densiti... |
ρl | 767.72 | kg/m3 | 318.15 | Density... |
ρl | 767.78 | kg/m3 | 318.15 | Excess ... |
ρl | 763.62 | kg/m3 | 323.15 | Density... |
ρl | 763.60 | kg/m3 | 323.15 | Densiti... |
ρl | 763.59 | kg/m3 | 323.15 | Densiti... |
ρl | 755.35 | kg/m3 | 333.15 | Densiti... |
ρl | 755.36 | kg/m3 | 333.15 | Densiti... |
ρl | 747.03 | kg/m3 | 343.15 | Densiti... |
ΔfusS | [51.30; 51.49] | J/mol×K | [161.40; 161.84] | ![]() |
ΔfusS | 51.30 | J/mol×K | 161.40 | NIST |
ΔfusS | 51.49 | J/mol×K | 161.84 | NIST |
γ | 0.03 | N/m | 293.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [291.27; 433.70] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40223e+01 | |||
Coefficient B | -3.39182e+03 | |||
Coefficient C | -4.43220e+01 | |||
Temperature range, min. | 291.27 | |||
Temperature range, max. | 433.70 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 291.27 | Calculated Property |
Pvap | 3.05 | kPa | 307.10 | Calculated Property |
Pvap | 6.35 | kPa | 322.92 | Calculated Property |
Pvap | 12.21 | kPa | 338.75 | Calculated Property |
Pvap | 21.97 | kPa | 354.57 | Calculated Property |
Pvap | 37.35 | kPa | 370.40 | Calculated Property |
Pvap | 60.45 | kPa | 386.22 | Calculated Property |
Pvap | 93.76 | kPa | 402.05 | Calculated Property |
Pvap | 140.11 | kPa | 417.87 | Calculated Property |
Pvap | 202.64 | kPa | 433.70 | Calculated Property |
Pvap | [3.59e-07; 3033.23] | kPa | [161.84; 609.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.23704e+01 | |||
Coefficient B | -7.17302e+03 | |||
Coefficient C | -8.45462e+00 | |||
Coefficient D | 4.40351e-06 | |||
Temperature range, min. | 161.84 | |||
Temperature range, max. | 609.15 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 400 600 | ||||
Pvap | 3.59e-07 | kPa | 161.84 | Calculated Property |
Pvap | 1.35e-03 | kPa | 211.54 | Calculated Property |
Pvap | 0.16 | kPa | 261.24 | Calculated Property |
Pvap | 3.32 | kPa | 310.94 | Calculated Property |
Pvap | 26.41 | kPa | 360.64 | Calculated Property |
Pvap | 116.75 | kPa | 410.35 | Calculated Property |
Pvap | 355.10 | kPa | 460.05 | Calculated Property |
Pvap | 843.49 | kPa | 509.75 | Calculated Property |
Pvap | 1694.41 | kPa | 559.45 | Calculated Property |
Pvap | 3033.23 | kPa | 609.15 | Calculated Property |
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