Property | Value | Unit | Source |
---|---|---|---|
ω | 0.0920 | KDB | |
ΔcH°liquid | -2380.00 | kJ/mol | NIST |
ΔfG° | 306.20 | kJ/mol | KDB |
ΔfH°gas | [295.00; 304.80] | kJ/mol |
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ΔfH°gas | 304.80 | kJ/mol | KDB |
ΔfH°gas | 295.00 | kJ/mol | NIST |
ΔfusH° | 7.81 | kJ/mol | Joback Calculated Property |
ΔvapH° | 23.69 | kJ/mol | Joback Calculated Property |
IE | [9.58; 9.90] | eV |
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IE | 9.58 ± 0.02 | eV | NIST |
IE | 9.58 ± 0.02 | eV | NIST |
IE | 9.58 ± 0.02 | eV | NIST |
IE | 9.58 ± 0.02 | eV | NIST |
IE | 9.63 | eV | NIST |
IE | 9.90 | eV | NIST |
IE | 9.90 | eV | NIST |
IE | 9.87 | eV | NIST |
IE | 9.90 | eV | NIST |
IE | 9.90 | eV | NIST |
IE | 9.64 ± 0.03 | eV | NIST |
log10WS | -1.15 | Crippen Calculated Property | |
logPoct/wat | 0.806 | Crippen Calculated Property | |
McVol | 54.320 | ml/mol | McGowan Calculated Property |
Pc | 4960.00 | kPa | KDB |
Inp | [373.00; 410.00] |
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|
Inp | 373.00 | NIST | |
Inp | 373.00 | NIST | |
Inp | 374.00 | NIST | |
Inp | 374.00 | NIST | |
Inp | 407.15 | NIST | |
Inp | 404.00 | NIST | |
Inp | 410.00 | NIST | |
Tboil | [276.15; 278.10] | K |
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Tboil | 278.10 | K | KDB |
Tboil | 276.15 ± 3.00 | K | NIST |
Tc | 455.00 | K | KDB |
Tfus | 227.60 | K | KDB |
Vc | 0.202 | m3/kmol | KDB |
Zc | 0.2648410 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [70.14; 95.56] | J/mol×K | [277.72; 454.49] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 70 75 80 85 90 95 300 350 400 450 | ||||
Cp,gas | 70.14 | J/mol×K | 277.72 | Joback Calculated Property |
Cp,gas | 74.98 | J/mol×K | 307.18 | Joback Calculated Property |
Cp,gas | 79.56 | J/mol×K | 336.64 | Joback Calculated Property |
Cp,gas | 83.89 | J/mol×K | 366.11 | Joback Calculated Property |
Cp,gas | 88.00 | J/mol×K | 395.57 | Joback Calculated Property |
Cp,gas | 91.89 | J/mol×K | 425.03 | Joback Calculated Property |
Cp,gas | 95.56 | J/mol×K | 454.49 | Joback Calculated Property |
ΔvapH | [24.48; 26.00] | kJ/mol | [229.00; 278.10] | ![]() |
ΔvapH | 26.00 | kJ/mol | 229.00 | NIST |
ΔvapH | 24.48 | kJ/mol | 278.10 | KDB |
ρl | 710.00 | kg/m3 | 273.00 | KDB |
γ | 0.02 | N/m | 298.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 223.95] | kPa | [205.72; 297.13] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.35875e+01 | |||
Coefficient B | -1.93992e+03 | |||
Coefficient C | -5.98620e+01 | |||
Temperature range, min. | 205.72 | |||
Temperature range, max. | 297.13 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 220 240 260 280 | ||||
Pvap | 1.33 | kPa | 205.72 | Calculated Property |
Pvap | 3.17 | kPa | 215.88 | Calculated Property |
Pvap | 6.78 | kPa | 226.03 | Calculated Property |
Pvap | 13.27 | kPa | 236.19 | Calculated Property |
Pvap | 24.17 | kPa | 246.35 | Calculated Property |
Pvap | 41.36 | kPa | 256.50 | Calculated Property |
Pvap | 67.14 | kPa | 266.66 | Calculated Property |
Pvap | 104.16 | kPa | 276.82 | Calculated Property |
Pvap | 155.36 | kPa | 286.97 | Calculated Property |
Pvap | 223.95 | kPa | 297.13 | Calculated Property |
Pvap | [0.14; 4773.01] | kPa | [179.95; 454.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.14672e+01 | |||
Coefficient B | -5.12322e+03 | |||
Coefficient C | -8.71388e+00 | |||
Coefficient D | 7.76544e-06 | |||
Temperature range, min. | 179.95 | |||
Temperature range, max. | 454.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 200 300 400 | ||||
Pvap | 0.14 | kPa | 179.95 | Calculated Property |
Pvap | 2.34 | kPa | 210.40 | Calculated Property |
Pvap | 17.42 | kPa | 240.85 | Calculated Property |
Pvap | 75.86 | kPa | 271.30 | Calculated Property |
Pvap | 231.15 | kPa | 301.75 | Calculated Property |
Pvap | 550.88 | kPa | 332.20 | Calculated Property |
Pvap | 1103.81 | kPa | 362.65 | Calculated Property |
Pvap | 1952.70 | kPa | 393.10 | Calculated Property |
Pvap | 3155.54 | kPa | 423.55 | Calculated Property |
Pvap | 4773.01 | kPa | 454.00 | Calculated Property |
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