Property | Value | Unit | Source |
---|---|---|---|
ω | 0.1890 | KDB | |
μ | 0.50 | debye | KDB |
EA | [1.02; 1.10] | eV |
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EA | 1.02 | eV | NIST |
EA | 1.10 ± 0.30 | eV | NIST |
ΔfG° | -245.50 | kJ/mol | KDB |
ΔfH°gas | [-290.00; -268.30] | kJ/mol |
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ΔfH°gas | -284.70 | kJ/mol | KDB |
ΔfH°gas | -278.00 ± 8.80 | kJ/mol | NIST |
ΔfH°gas | -268.30 ± 8.40 | kJ/mol | NIST |
ΔfH°gas | -290.00 ± 20.00 | kJ/mol | NIST |
ΔfusH° | 6.60 | kJ/mol | Joback Calculated Property |
ΔvapH° | 28.86 | kJ/mol | Joback Calculated Property |
IE | [11.46; 11.90] | eV |
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IE | 11.68 ± 0.13 | eV | NIST |
IE | 11.73 ± 0.02 | eV | NIST |
IE | Outlier 11.46 ± 0.02 | eV | NIST |
IE | 11.77 ± 0.01 | eV | NIST |
IE | 11.77 ± 0.02 | eV | NIST |
IE | 11.76 ± 0.01 | eV | NIST |
IE | 11.85 | eV | NIST |
IE | 11.90 | eV | NIST |
log10WS | -2.15 | Crippen Calculated Property | |
logPoct/wat | 2.284 | Crippen Calculated Property | |
McVol | 63.440 | ml/mol | McGowan Calculated Property |
Pc | [4370.00; 4466.00] | kPa |
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Pc | 4410.00 | kPa | KDB |
Pc | 4466.00 ± 12.00 | kPa | NIST |
Pc | 4370.00 ± 50.00 | kPa | NIST |
Pc | 4405.73 | kPa | NIST |
ρc | [553.59; 570.21] | kg/m3 |
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ρc | 570.21 ± 0.55 | kg/m3 | NIST |
ρc | 553.59 ± 5.54 | kg/m3 | NIST |
ρc | 553.59 ± 1.37 | kg/m3 | NIST |
Inp | [460.00; 486.00] |
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|
Inp | 470.00 | NIST | |
Inp | 485.00 | NIST | |
Inp | 486.00 | NIST | |
Inp | 482.00 | NIST | |
Inp | Outlier 460.00 | NIST | |
Inp | 478.00 | NIST | |
Inp | 478.00 | NIST | |
Inp | 484.00 | NIST | |
Inp | 482.00 | NIST | |
Inp | 484.00 | NIST | |
Inp | Outlier 460.00 | NIST | |
Inp | 484.00 | NIST | |
Inp | 470.00 | NIST | |
Inp | 486.00 | NIST | |
I | [605.00; 605.00] |
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|
I | 605.00 | NIST | |
I | 605.00 | NIST | |
S°liquid | 225.60 | J/mol×K | NIST |
Tboil | [296.80; 296.92] | K |
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Tboil | 296.90 | K | KDB |
Tboil | 296.90 | K | NIST |
Tboil | 296.80 ± 0.05 | K | NIST |
Tboil | 296.92 | K | NIST |
Tc | [471.10; 471.20] | K |
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Tc | 471.20 | K | KDB |
Tc | 471.10 ± 0.50 | K | NIST |
Tc | 471.15 ± 0.10 | K | NIST |
Tc | 471.15 ± 0.04 | K | NIST |
Tc | 471.15 | K | NIST |
Tc | 471.15 ± 0.40 | K | NIST |
Tfus | [162.00; 165.40] | K |
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Tfus | 162.04 | K | KDB |
Tfus | 162.00 ± 2.00 | K | NIST |
Tfus | 162.72 ± 0.01 | K | NIST |
Tfus | 162.70 ± 0.10 | K | NIST |
Tfus | Outlier 165.40 ± 0.20 | K | NIST |
Tfus | 162.67 ± 0.05 | K | NIST |
Ttriple | [162.10; 162.70] | K |
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Ttriple | 162.19 ± 0.05 | K | NIST |
Ttriple | 162.69 ± 0.06 | K | NIST |
Ttriple | 162.67 ± 0.06 | K | NIST |
Ttriple | 162.68 ± 0.03 | K | NIST |
Ttriple | 162.65 ± 0.02 | K | NIST |
Ttriple | 162.69 ± 0.03 | K | NIST |
Ttriple | 162.70 ± 0.01 | K | NIST |
Ttriple | Outlier 162.10 ± 0.20 | K | NIST |
Ttriple | 162.68 ± 0.07 | K | NIST |
Vc | [0.247; 0.248] | m3/kmol |
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Vc | 0.248 | m3/kmol | KDB |
Vc | 0.247 ± 0.006 | m3/kmol | NIST |
Zc | 0.2791570 | KDB | |
Zra | 0.27 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [80.37; 95.16] | J/mol×K | [330.61; 525.49] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 80 85 90 95 350 400 450 500 | ||||
Cp,gas | 80.37 | J/mol×K | 330.61 | Joback Calculated Property |
Cp,gas | 83.63 | J/mol×K | 363.09 | Joback Calculated Property |
Cp,gas | 86.55 | J/mol×K | 395.57 | Joback Calculated Property |
Cp,gas | 89.14 | J/mol×K | 428.05 | Joback Calculated Property |
Cp,gas | 91.42 | J/mol×K | 460.53 | Joback Calculated Property |
Cp,gas | 93.42 | J/mol×K | 493.01 | Joback Calculated Property |
Cp,gas | 95.16 | J/mol×K | 525.49 | Joback Calculated Property |
Cp,liquid | [121.55; 126.70] | J/mol×K | [298.15; 303.15] | ![]() |
Cp,liquid | 121.55 | J/mol×K | 298.15 | NIST |
Cp,liquid | 126.70 | J/mol×K | 298.15 | NIST |
Cp,liquid | 122.50 | J/mol×K | 303.15 | NIST |
ΔfusH | [6.89; 7.90] | kJ/mol | [162.68; 165.40] | ![]() |
ΔfusH | 6.89 | kJ/mol | 162.68 | NIST |
ΔfusH | 6.90 | kJ/mol | 162.70 | NIST |
ΔfusH | 7.90 | kJ/mol | 165.40 | NIST |
ΔvapH | [24.70; 28.50] | kJ/mol | [231.00; 446.00] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 25 26 27 28 300 400 | ||||
ΔvapH | 28.20 | kJ/mol | 231.00 | NIST |
ΔvapH | 28.50 | kJ/mol | 257.00 | NIST |
ΔvapH | 27.30 | kJ/mol | 265.00 | NIST |
ΔvapH | 27.10 | kJ/mol | 265.00 | NIST |
ΔvapH | 26.40 | kJ/mol | 289.00 | NIST |
ΔvapH | 25.20 | kJ/mol | 290.00 | NIST |
ΔvapH | 25.21 | kJ/mol | 290.40 | NIST |
ΔvapH | 24.77 | kJ/mol | 297.10 | KDB |
ΔvapH | 25.60 | kJ/mol | 329.00 | NIST |
ΔvapH | 24.70 | kJ/mol | 393.00 | NIST |
ΔvapH | 25.10 | kJ/mol | 446.00 | NIST |
ρl | 1494.00 | kg/m3 | 290.00 | KDB |
ΔfusS | [42.38; 47.80] | J/mol×K | [162.68; 165.40] | ![]() |
ΔfusS | 42.38 | J/mol×K | 162.68 | NIST |
ΔfusS | 47.80 | J/mol×K | 165.40 | NIST |
γ | 0.02 | N/m | 277.60 | KDB |
ΔvapS | 86.81 | J/mol×K | 290.40 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 4420.29] | kPa | [214.36; 471.11] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40921e+01 | |||
Coefficient B | -2.49136e+03 | |||
Coefficient C | -3.38850e+01 | |||
Temperature range, min. | 214.36 | |||
Temperature range, max. | 471.11 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400 | ||||
Pvap | 1.33 | kPa | 214.36 | Calculated Property |
Pvap | 8.77 | kPa | 242.89 | Calculated Property |
Pvap | 36.73 | kPa | 271.42 | Calculated Property |
Pvap | 113.08 | kPa | 299.94 | Calculated Property |
Pvap | 280.04 | kPa | 328.47 | Calculated Property |
Pvap | 590.88 | kPa | 357.00 | Calculated Property |
Pvap | 1104.49 | kPa | 385.53 | Calculated Property |
Pvap | 1879.56 | kPa | 414.05 | Calculated Property |
Pvap | 2969.72 | kPa | 442.58 | Calculated Property |
Pvap | 4420.29 | kPa | 471.11 | Calculated Property |
Pvap | [4.88e-03; 4467.78] | kPa | [162.04; 471.20] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.72409e+01 | |||
Coefficient B | -5.39795e+03 | |||
Coefficient C | -9.73971e+00 | |||
Coefficient D | 1.15758e-05 | |||
Temperature range, min. | 162.04 | |||
Temperature range, max. | 471.20 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 300 400 | ||||
Pvap | 4.88e-03 | kPa | 162.04 | Calculated Property |
Pvap | 0.29 | kPa | 196.39 | Calculated Property |
Pvap | 4.33 | kPa | 230.74 | Calculated Property |
Pvap | 28.32 | kPa | 265.09 | Calculated Property |
Pvap | 111.85 | kPa | 299.44 | Calculated Property |
Pvap | 319.38 | kPa | 333.80 | Calculated Property |
Pvap | 735.39 | kPa | 368.15 | Calculated Property |
Pvap | 1464.61 | kPa | 402.50 | Calculated Property |
Pvap | 2643.90 | kPa | 436.85 | Calculated Property |
Pvap | 4467.78 | kPa | 471.20 | Calculated Property |
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