Property | Value | Unit | Source |
---|---|---|---|
PAff | [828.90; 832.00] | kJ/mol |
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PAff | 832.00 | kJ/mol | NIST |
PAff | 828.90 | kJ/mol | NIST |
BasG | [798.70; 801.30] | kJ/mol |
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BasG | 801.30 | kJ/mol | NIST |
BasG | 798.70 | kJ/mol | NIST |
ΔcH°liquid | -4289.90 | kJ/mol | NIST |
ΔfG° | 351.96 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 306.60 ± 1.70 | kJ/mol | NIST |
ΔfH°liquid | [-261.00; 284.30] | kJ/mol |
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ΔfH°liquid | 284.30 ± 4.00 | kJ/mol | NIST |
ΔfH°liquid | -261.00 | kJ/mol | NIST |
ΔfusH° | 13.49 | kJ/mol | Joback Calculated Property |
ΔvapH° | 35.54 | kJ/mol | Joback Calculated Property |
IE | [8.75; 9.56] | eV |
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IE | 8.82 ± 0.02 | eV | NIST |
IE | 8.82 ± 0.00 | eV | NIST |
IE | 8.82 ± 0.08 | eV | NIST |
IE | 8.90 | eV | NIST |
IE | 8.75 | eV | NIST |
IE | 8.81 ± 0.01 | eV | NIST |
IE | Outlier 9.56 ± 0.02 | eV | NIST |
IE | 8.78 | eV | NIST |
IE | 8.80 | eV | NIST |
IE | 8.82 ± 0.02 | eV | NIST |
IE | 8.78 | eV | NIST |
IE | 8.88 ± 0.02 | eV | NIST |
log10WS | -2.17 | Crippen Calculated Property | |
logPoct/wat | 1.668 | Crippen Calculated Property | |
McVol | 91.220 | ml/mol | McGowan Calculated Property |
Pc | 4403.25 | kPa | Joback Calculated Property |
Inp | [122.00; 881.00] |
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|
Inp | 870.00 | NIST | |
Inp | 833.00 | NIST | |
Inp | 830.00 | NIST | |
Inp | 862.10 | NIST | |
Inp | 875.00 | NIST | |
Inp | 862.00 | NIST | |
Inp | 830.40 | NIST | |
Inp | 834.10 | NIST | |
Inp | 830.40 | NIST | |
Inp | 834.10 | NIST | |
Inp | 868.00 | NIST | |
Inp | 833.00 | NIST | |
Inp | 875.00 | NIST | |
Inp | 881.00 | NIST | |
Inp | 877.00 | NIST | |
Inp | 875.90 | NIST | |
Inp | 856.00 | NIST | |
Inp | 849.00 | NIST | |
Inp | 863.00 | NIST | |
Inp | 862.00 | NIST | |
Inp | Outlier 122.00 | NIST | |
Inp | Outlier 122.10 | NIST | |
Inp | Outlier 122.70 | NIST | |
Inp | 881.00 | NIST | |
I | [1354.00; 1372.00] |
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|
I | 1357.20 | NIST | |
I | 1370.00 | NIST | |
I | 1372.00 | NIST | |
I | 1354.00 | NIST | |
I | 1372.00 | NIST | |
I | 1361.00 | NIST | |
I | 1357.20 | NIST | |
S°liquid | 221.20 | J/mol×K | NIST |
Tboil | [412.65; 416.20] | K |
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Tboil | 416.00 ± 1.00 | K | NIST |
Tboil | 416.20 | K | NIST |
Tboil | 415.65 ± 1.50 | K | NIST |
Tboil | 414.65 ± 3.00 | K | NIST |
Tboil | 412.65 ± 1.50 | K | NIST |
Tc | 625.47 | K | Joback Calculated Property |
Tfus | 228.35 ± 0.40 | K | NIST |
Ttriple | 228.04 ± 0.02 | K | NIST |
Vc | 0.338 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [149.68; 204.88] | J/mol×K | [399.24; 625.47] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 150 160 170 180 190 200 210 400 500 600 | ||||
Cp,gas | 149.68 | J/mol×K | 399.24 | Joback Calculated Property |
Cp,gas | 160.67 | J/mol×K | 436.95 | Joback Calculated Property |
Cp,gas | 170.89 | J/mol×K | 474.65 | Joback Calculated Property |
Cp,gas | 180.38 | J/mol×K | 512.36 | Joback Calculated Property |
Cp,gas | 189.18 | J/mol×K | 550.06 | Joback Calculated Property |
Cp,gas | 197.33 | J/mol×K | 587.77 | Joback Calculated Property |
Cp,gas | 204.88 | J/mol×K | 625.47 | Joback Calculated Property |
Cp,liquid | [179.50; 180.10] | J/mol×K | [298.15; 298.50] | ![]() |
Cp,liquid | 180.10 | J/mol×K | 298.15 | NIST |
Cp,liquid | 179.50 | J/mol×K | 298.50 | NIST |
ΔfusH | [9.46; 9.46] | kJ/mol | [228.00; 228.04] | ![]() |
ΔfusH | 9.46 | kJ/mol | 228.00 | NIST |
ΔfusH | 9.46 | kJ/mol | 228.00 | NIST |
ΔfusH | 9.46 | kJ/mol | 228.04 | NIST |
ΔvapH | [38.00; 45.20] | kJ/mol | [278.00; 364.50] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 38 39 40 41 42 43 44 45 300 350 | ||||
ΔvapH | 43.90 | kJ/mol | 278.00 | NIST |
ΔvapH | 45.20 | kJ/mol | 281.00 | NIST |
ΔvapH | 42.60 ± 0.10 | kJ/mol | 364.50 | NIST |
ΔvapH | 40.40 ± 0.10 | kJ/mol | 364.50 | NIST |
ΔvapH | 38.00 ± 0.20 | kJ/mol | 364.50 | NIST |
ΔfusS | 41.50 | J/mol×K | 228.04 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [315.74; 418.69] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.72233e+01 | |||
Coefficient B | -4.13406e+03 | |||
Coefficient C | -7.16380e+01 | |||
Temperature range, min. | 315.74 | |||
Temperature range, max. | 418.69 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
Pvap | 1.33 | kPa | 315.74 | Calculated Property |
Pvap | 2.85 | kPa | 327.18 | Calculated Property |
Pvap | 5.69 | kPa | 338.62 | Calculated Property |
Pvap | 10.75 | kPa | 350.06 | Calculated Property |
Pvap | 19.32 | kPa | 361.50 | Calculated Property |
Pvap | 33.20 | kPa | 372.93 | Calculated Property |
Pvap | 54.83 | kPa | 384.37 | Calculated Property |
Pvap | 87.42 | kPa | 395.81 | Calculated Property |
Pvap | 135.02 | kPa | 407.25 | Calculated Property |
Pvap | 202.64 | kPa | 418.69 | Calculated Property |
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