Property | Value | Unit | Source |
---|---|---|---|
PAff | 802.50 | kJ/mol | NIST |
BasG | 772.70 | kJ/mol | NIST |
ΔcH°liquid | [-2300.70; -2292.10] | kJ/mol | |
ΔcH°liquid | -2300.70 ± 0.63 | kJ/mol | NIST |
ΔcH°liquid | -2292.10 ± 1.20 | kJ/mol | NIST |
EA | 9.99e-04 | eV | NIST |
ΔfG° | -83.43 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-101.00; -91.60] | kJ/mol | |
ΔfH°gas | -91.60 | kJ/mol | NIST |
ΔfH°gas | -101.00 ± 1.00 | kJ/mol | NIST |
ΔfH°liquid | [-139.50; -131.00] | kJ/mol | |
ΔfH°liquid | -131.00 | kJ/mol | NIST |
ΔfH°liquid | -139.50 ± 1.20 | kJ/mol | NIST |
ΔfusH° | 0.59 | kJ/mol | Joback Calculated Property |
ΔvapH° | [38.20; 38.40] | kJ/mol | |
ΔvapH° | 38.30 | kJ/mol | NIST |
ΔvapH° | 38.40 | kJ/mol | NIST |
ΔvapH° | 38.20 ± 0.42 | kJ/mol | NIST |
ΔvapH° | 38.20 ± 0.40 | kJ/mol | NIST |
IE | [9.35; 9.61] | eV | |
IE | 9.35 | eV | NIST |
IE | 9.40 ± 0.10 | eV | NIST |
IE | 9.60 ± 0.10 | eV | NIST |
IE | 9.35 | eV | NIST |
IE | 9.61 ± 0.02 | eV | NIST |
log10WS | -0.67 | Crippen Calculated Property | |
logPoct/wat | 0.739 | Crippen Calculated Property | |
McVol | 57.930 | ml/mol | McGowan Calculated Property |
Pc | 5258.62 | kPa | Joback Calculated Property |
Inp | [633.00; 647.00] | ||
Inp | 642.00 | NIST | |
Inp | 639.00 | NIST | |
Inp | 641.00 | NIST | |
Inp | 641.00 | NIST | |
Inp | 645.00 | NIST | |
Inp | 647.00 | NIST | |
Inp | 639.00 | NIST | |
Inp | Outlier 633.00 | NIST | |
Inp | 642.00 | NIST | |
Inp | 647.00 | NIST | |
Tboil | [372.05; 1171.15] | K | |
Tboil | 372.05 | K | KDB |
Tboil | 372.20 | K | NIST |
Tboil | 1171.15 ± 1.50 | K | NIST |
Tboil | 372.90 ± 0.50 | K | NIST |
Tboil | 372.20 ± 4.00 | K | NIST |
Tc | 587.84 | K | Joback Calculated Property |
Tfus | 221.72 | K | Joback Calculated Property |
Vc | 0.216 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [93.90; 142.11] | J/mol×K | [374.42; 587.84] | |
T(K) Ideal gas heat capacity (J/mol×K) 90 100 110 120 130 140 400 450 500 550 | ||||
Cp,gas | 93.90 | J/mol×K | 374.42 | Joback Calculated Property |
Cp,gas | 102.89 | J/mol×K | 409.99 | Joback Calculated Property |
Cp,gas | 111.48 | J/mol×K | 445.56 | Joback Calculated Property |
Cp,gas | 119.70 | J/mol×K | 481.13 | Joback Calculated Property |
Cp,gas | 127.54 | J/mol×K | 516.70 | Joback Calculated Property |
Cp,gas | 135.01 | J/mol×K | 552.27 | Joback Calculated Property |
Cp,gas | 142.11 | J/mol×K | 587.84 | Joback Calculated Property |
ΔfusH | [10.80; 10.80] | kJ/mol | [220.50; 220.50] | |
ΔfusH | 10.80 | kJ/mol | 220.50 | NIST |
ΔfusH | 10.80 | kJ/mol | 220.50 | NIST |
ΔvapH | [36.30; 38.50] | kJ/mol | [273.50; 348.50] | |
ΔvapH | 38.50 | kJ/mol | 273.50 | NIST |
ΔvapH | 37.70 | kJ/mol | 322.50 | NIST |
ΔvapH | 36.30 | kJ/mol | 348.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [274.32; 396.31] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.46360e+01 | |||
Coefficient B | -3.24879e+03 | |||
Coefficient C | -4.78950e+01 | |||
Temperature range, min. | 274.32 | |||
Temperature range, max. | 396.31 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 274.32 | Calculated Property |
Pvap | 3.00 | kPa | 287.87 | Calculated Property |
Pvap | 6.18 | kPa | 301.43 | Calculated Property |
Pvap | 11.85 | kPa | 314.98 | Calculated Property |
Pvap | 21.32 | kPa | 328.54 | Calculated Property |
Pvap | 36.35 | kPa | 342.09 | Calculated Property |
Pvap | 59.12 | kPa | 355.65 | Calculated Property |
Pvap | 92.28 | kPa | 369.20 | Calculated Property |
Pvap | 138.95 | kPa | 382.76 | Calculated Property |
Pvap | 202.67 | kPa | 396.31 | Calculated Property |
Pvap | [0.26; 128.91] | kPa | [249.15; 380.15] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.68593e+01 | |||
Coefficient B | -7.17622e+03 | |||
Coefficient C | -1.08793e+01 | |||
Coefficient D | 1.04245e-05 | |||
Temperature range, min. | 249.15 | |||
Temperature range, max. | 380.15 | |||
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 120 140 250 300 350 | ||||
Pvap | 0.26 | kPa | 249.15 | Calculated Property |
Pvap | 0.76 | kPa | 263.71 | Calculated Property |
Pvap | 1.90 | kPa | 278.26 | Calculated Property |
Pvap | 4.29 | kPa | 292.82 | Calculated Property |
Pvap | 8.84 | kPa | 307.37 | Calculated Property |
Pvap | 16.90 | kPa | 321.93 | Calculated Property |
Pvap | 30.28 | kPa | 336.48 | Calculated Property |
Pvap | 51.34 | kPa | 351.04 | Calculated Property |
Pvap | 83.02 | kPa | 365.59 | Calculated Property |
Pvap | 128.91 | kPa | 380.15 | Calculated Property |
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