Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2370 | KDB | |
ΔcH°liquid | [-4598.90; -4586.50] | kJ/mol |
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ΔcH°liquid | -4597.00 ± 0.80 | kJ/mol | NIST |
ΔcH°liquid | -4597.60 ± 0.60 | kJ/mol | NIST |
ΔcH°liquid | -4598.90 ± 1.70 | kJ/mol | NIST |
ΔcH°liquid | -4586.50 | kJ/mol | NIST |
ΔfG° | 63.05 | kJ/mol | KDB |
Δc,grossH | 4597.80 | kJ/mol | KDB |
Δc,netH | 4289.856 | kJ/mol | KDB |
ΔfH°gas | -119.40 | kJ/mol | KDB |
ΔfH°liquid | -156.40 ± 1.70 | kJ/mol | NIST |
ΔfusH° | 2.55 | kJ/mol | Joback Calculated Property |
ΔvapH° | [37.00; 39.40] | kJ/mol |
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ΔvapH° | 38.50 | kJ/mol | NIST |
ΔvapH° | 38.50 ± 2.10 | kJ/mol | NIST |
ΔvapH° | 38.50 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 39.40 | kJ/mol | NIST |
ΔvapH° | 37.00 | kJ/mol | NIST |
IE | [9.82; 9.97] | eV |
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IE | 9.90 ± 0.10 | eV | NIST |
IE | 9.82 ± 0.05 | eV | NIST |
IE | 9.96 | eV | NIST |
IE | 9.97 | eV | NIST |
IE | 9.88 ± 0.05 | eV | NIST |
log10WS | [-3.52; -3.51] |
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|
log10WS | -3.52 | Aq. Sol... | |
log10WS | -3.51 | Estimat... | |
logPoct/wat | 2.731 | Crippen Calculated Property | |
McVol | 98.630 | ml/mol | McGowan Calculated Property |
Pc | [3813.00; 3826.00] | kPa |
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Pc | 3820.00 | kPa | KDB |
Pc | 3820.00 ± 40.00 | kPa | NIST |
Pc | 3813.00 ± 50.00 | kPa | NIST |
Pc | 3826.00 ± 40.53 | kPa | NIST |
ρc | 277.87 ± 3.93 | kg/m3 | NIST |
Inp | [784.00; 846.00] |
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|
Inp | Outlier 837.50 | NIST | |
Inp | Outlier 836.00 | NIST | |
Inp | Outlier 837.00 | NIST | |
Inp | 794.20 | NIST | |
Inp | 800.00 | NIST | |
Inp | 806.90 | NIST | |
Inp | 819.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | 789.00 | NIST | |
Inp | 788.00 | NIST | |
Inp | 789.00 | NIST | |
Inp | 815.00 | NIST | |
Inp | 811.60 | NIST | |
Inp | 791.00 | NIST | |
Inp | 804.00 | NIST | |
Inp | 811.00 | NIST | |
Inp | 829.00 | NIST | |
Inp | 807.00 | NIST | |
Inp | 803.00 | NIST | |
Inp | 784.00 | NIST | |
Inp | 812.00 | NIST | |
Inp | 786.00 | NIST | |
Inp | 795.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | 806.00 | NIST | |
Inp | 816.00 | NIST | |
Inp | 804.00 | NIST | |
Inp | 824.00 | NIST | |
Inp | 819.00 | NIST | |
Inp | 787.00 | NIST | |
Inp | 794.00 | NIST | |
Inp | 786.00 | NIST | |
Inp | 796.00 | NIST | |
Inp | 796.00 | NIST | |
Inp | 796.00 | NIST | |
Inp | 790.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | Outlier 846.00 | NIST | |
Inp | 803.00 | NIST | |
Inp | 797.00 | NIST | |
Inp | 807.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | 787.00 | NIST | |
Inp | Outlier 837.50 | NIST | |
Inp | 806.90 | NIST | |
Inp | 789.00 | NIST | |
Inp | 811.00 | NIST | |
Inp | 812.00 | NIST | |
Inp | 816.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | 819.00 | NIST | |
Inp | 796.00 | NIST | |
Inp | 786.00 | NIST | |
I | [878.00; 899.00] |
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|
I | 899.00 | NIST | |
I | 878.00 | NIST | |
I | 892.00 | NIST | |
I | 883.00 | NIST | |
I | 883.00 | NIST | |
I | 899.00 | NIST | |
S°gas | 342.30 ± 1.30 | J/mol×K | NIST |
S°liquid | 242.55 | J/mol×K | NIST |
Tboil | [391.25; 393.00] | K |
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Tboil | 391.63 | K | KDB |
Tboil | 391.70 | K | NIST |
Tboil | Outlier 393.00 ± 2.00 | K | NIST |
Tboil | 391.99 ± 0.20 | K | NIST |
Tboil | 391.99 ± 0.30 | K | NIST |
Tboil | 391.99 ± 0.30 | K | NIST |
Tboil | 391.63 ± 0.30 | K | NIST |
Tboil | 391.25 ± 0.60 | K | NIST |
Tboil | 392.15 ± 2.00 | K | NIST |
Tc | [604.20; 604.20] | K |
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Tc | 604.20 | K | KDB |
Tc | 604.20 ± 0.50 | K | NIST |
Tc | 604.20 ± 0.50 | K | NIST |
Tfus | 265.12 | K | KDB |
Ttriple | [265.00; 265.12] | K |
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Ttriple | 265.00 ± 0.07 | K | NIST |
Ttriple | 265.12 ± 0.05 | K | NIST |
Ttriple | 265.10 ± 3.00 | K | NIST |
Vc | [0.353; 0.354] | m3/kmol |
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Vc | 0.353 | m3/kmol | KDB |
Vc | 0.353 | m3/kmol | NIST |
Vc | 0.354 ± 0.007 | m3/kmol | NIST |
Zc | 0.2684240 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [170.69; 260.93] | J/mol×K | [388.05; 600.09] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 180 200 220 240 260 400 500 600 | ||||
Cp,gas | 170.69 | J/mol×K | 388.05 | Joback Calculated Property |
Cp,gas | 187.82 | J/mol×K | 423.39 | Joback Calculated Property |
Cp,gas | 204.08 | J/mol×K | 458.73 | Joback Calculated Property |
Cp,gas | 219.50 | J/mol×K | 494.07 | Joback Calculated Property |
Cp,gas | 234.11 | J/mol×K | 529.41 | Joback Calculated Property |
Cp,gas | 247.91 | J/mol×K | 564.75 | Joback Calculated Property |
Cp,gas | 260.93 | J/mol×K | 600.09 | Joback Calculated Property |
Cp,liquid | [180.47; 180.75] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 180.61 | J/mol×K | 298.15 | NIST |
Cp,liquid | 180.47 | J/mol×K | 298.15 | NIST |
Cp,liquid | 180.75 | J/mol×K | 298.15 | NIST |
η | [0.0002763; 0.0332403] | Pa×s | [176.75; 388.05] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-3 0.01 0.02 0.02 0.03 0.03 0.04 200 250 300 350 | ||||
η | 0.0332403 | Pa×s | 176.75 | Joback Calculated Property |
η | 0.0077075 | Pa×s | 211.97 | Joback Calculated Property |
η | 0.0027104 | Pa×s | 247.18 | Joback Calculated Property |
η | 0.0012369 | Pa×s | 282.40 | Joback Calculated Property |
η | 0.0006718 | Pa×s | 317.62 | Joback Calculated Property |
η | 0.0004121 | Pa×s | 352.83 | Joback Calculated Property |
η | 0.0002763 | Pa×s | 388.05 | Joback Calculated Property |
ΔfusH | [0.29; 4.98] | kJ/mol | [134.80; 265.10] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0 1 2 3 4 5 150 200 250 | ||||
ΔfusH | 4.98 | kJ/mol | 134.80 | NIST |
ΔfusH | 0.29 | kJ/mol | 198.20 | NIST |
ΔfusH | 0.45 | kJ/mol | 212.40 | NIST |
ΔfusH | 1.88 | kJ/mol | 265.10 | NIST |
ΔfusH | 1.88 | kJ/mol | 265.10 | NIST |
ΔsubH | 53.50 | kJ/mol | 134.00 | NIST |
ΔvapH | [31.70; 38.60] | kJ/mol | [307.50; 540.00] | ![]() |
ΔvapH | 38.60 | kJ/mol | 307.50 | NIST |
ΔvapH | 36.40 | kJ/mol | 365.50 | NIST |
ΔvapH | 36.10 | kJ/mol | 387.00 | NIST |
ΔvapH | 31.70 | kJ/mol | 540.00 | NIST |
n0 | 1.44240 | 298.15 | KDB | |
ρl | 810.00 | kg/m3 | 293.00 | KDB |
ΔfusS | [1.46; 36.94] | J/mol×K | [134.80; 265.10] | ![]() |
ΔfusS | 36.94 | J/mol×K | 134.80 | NIST |
ΔfusS | 1.46 | J/mol×K | 198.20 | NIST |
ΔfusS | 2.11 | J/mol×K | 212.40 | NIST |
ΔfusS | 7.10 | J/mol×K | 265.10 | NIST |
γ | 0.03 | N/m | 298.20 | KDB |
λ | [0.11; 0.13] | W/m×K | [262.18; 320.36] | ![]() |
T(K) Liquid thermal conductivity (W/m×K) 0.12 0.12 0.13 280 300 320 | ||||
λ | 0.13 | W/m×K | 262.18 | Thermal... |
λ | 0.13 | W/m×K | 262.37 | Thermal... |
λ | 0.13 | W/m×K | 262.50 | Thermal... |
λ | 0.12 | W/m×K | 280.17 | Thermal... |
λ | 0.12 | W/m×K | 280.35 | Thermal... |
λ | 0.12 | W/m×K | 280.48 | Thermal... |
λ | 0.12 | W/m×K | 297.01 | Thermal... |
λ | 0.12 | W/m×K | 297.20 | Thermal... |
λ | 0.12 | W/m×K | 297.33 | Thermal... |
λ | 0.11 | W/m×K | 320.05 | Thermal... |
λ | 0.11 | W/m×K | 320.23 | Thermal... |
λ | 0.11 | W/m×K | 320.36 | Thermal... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.39; 202.67] | kPa | [265.12; 418.93] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41291e+01 | |||
Coefficient B | -3.26491e+03 | |||
Coefficient C | -4.86550e+01 | |||
Temperature range, min. | 265.12 | |||
Temperature range, max. | 418.93 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 0.39 | kPa | 265.12 | Calculated Property |
Pvap | 1.16 | kPa | 282.21 | Calculated Property |
Pvap | 3.01 | kPa | 299.30 | Calculated Property |
Pvap | 6.92 | kPa | 316.39 | Calculated Property |
Pvap | 14.39 | kPa | 333.48 | Calculated Property |
Pvap | 27.53 | kPa | 350.57 | Calculated Property |
Pvap | 49.13 | kPa | 367.66 | Calculated Property |
Pvap | 82.67 | kPa | 384.75 | Calculated Property |
Pvap | 132.28 | kPa | 401.84 | Calculated Property |
Pvap | 202.67 | kPa | 418.93 | Calculated Property |
Pvap | [0.39; 3831.50] | kPa | [265.12; 604.30] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.37466e+01 | |||
Coefficient B | -7.38221e+03 | |||
Coefficient C | -1.02752e+01 | |||
Coefficient D | 6.91167e-06 | |||
Temperature range, min. | 265.12 | |||
Temperature range, max. | 604.30 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 600 | ||||
Pvap | 0.39 | kPa | 265.12 | Calculated Property |
Pvap | 3.66 | kPa | 302.81 | Calculated Property |
Pvap | 19.26 | kPa | 340.49 | Calculated Property |
Pvap | 68.53 | kPa | 378.18 | Calculated Property |
Pvap | 186.24 | kPa | 415.87 | Calculated Property |
Pvap | 418.69 | kPa | 453.55 | Calculated Property |
Pvap | 822.00 | kPa | 491.24 | Calculated Property |
Pvap | 1463.67 | kPa | 528.93 | Calculated Property |
Pvap | 2428.81 | kPa | 566.61 | Calculated Property |
Pvap | 3831.50 | kPa | 604.30 | Calculated Property |
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