Property | Value | Unit | Source |
---|---|---|---|
ΔvapH° | 26.00 ± 0.60 | kJ/mol | NIST |
IE | [9.40; 10.57] | eV | |
IE | 9.80 ± 0.04 | eV | NIST |
IE | 9.80 ± 0.03 | eV | NIST |
IE | 9.60 | eV | NIST |
IE | 9.99 ± 0.03 | eV | NIST |
IE | 9.79 ± 0.04 | eV | NIST |
IE | 9.40 ± 0.10 | eV | NIST |
IE | 9.85 ± 0.16 | eV | NIST |
IE | 9.74 ± 0.05 | eV | NIST |
IE | 9.86 ± 0.02 | eV | NIST |
IE | 9.85 ± 0.16 | eV | NIST |
IE | 9.90 ± 0.10 | eV | NIST |
IE | 9.98 ± 0.03 | eV | NIST |
IE | 10.29 | eV | NIST |
IE | 10.40 | eV | NIST |
IE | Outlier 10.57 | eV | NIST |
log10WS | 1.03 | Crippen Calculated Property | |
logPoct/wat | 1.954 | Crippen Calculated Property | |
Pc | 2821.00 ± 1.00 | kPa | NIST |
Inp | [419.00; 430.00] | ||
Inp | 428.10 | NIST | |
Inp | 428.00 | NIST | |
Inp | 428.40 | NIST | |
Inp | 427.60 | NIST | |
Inp | 426.80 | NIST | |
Inp | 425.90 | NIST | |
Inp | 424.80 | NIST | |
Inp | 423.60 | NIST | |
Inp | 422.40 | NIST | |
Inp | 430.00 | NIST | |
Inp | 429.80 | NIST | |
Inp | 429.40 | NIST | |
Inp | 429.00 | NIST | |
Inp | 429.40 | NIST | |
Inp | 420.00 | NIST | |
Inp | 420.00 | NIST | |
Inp | 419.00 | NIST | |
Inp | 428.10 | NIST | |
Inp | 425.90 | NIST | |
Inp | 429.80 | NIST | |
Inp | 419.00 | NIST | |
Inp | 420.00 | NIST | |
S°liquid | [272.04; 277.27] | J/mol×K | |
S°liquid | 272.04 | J/mol×K | NIST |
S°liquid | 277.27 | J/mol×K | NIST |
Tboil | [299.00; 299.70] | K | |
Tboil | 299.70 | K | NIST |
Tboil | 299.00 ± 3.00 | K | NIST |
Tc | 448.64 ± 0.03 | K | NIST |
Ttriple | [165.92; 174.12] | K | |
Ttriple | Outlier 165.92 ± 0.01 | K | NIST |
Ttriple | 171.01 ± 0.01 | K | NIST |
Ttriple | 174.07 ± 0.01 | K | NIST |
Ttriple | 170.98 ± 0.01 | K | NIST |
Ttriple | 174.04 ± 0.01 | K | NIST |
Ttriple | 171.04 ± 0.02 | K | NIST |
Ttriple | 174.12 ± 0.02 | K | NIST |
Vc | 0.362 ± 0.008 | m3/kmol | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,liquid | [164.56; 197.90] | J/mol×K | [177.45; 290.00] | |
Cp,liquid | 164.56 | J/mol×K | 177.45 | NIST |
Cp,liquid | 189.84 | J/mol×K | 290.00 | NIST |
Cp,liquid | 197.90 | J/mol×K | 290.00 | NIST |
ΔfusH | [6.74; 6.74] | kJ/mol | [174.00; 174.00] | |
ΔfusH | 6.74 | kJ/mol | 174.00 | NIST |
ΔfusH | 6.74 | kJ/mol | 174.00 | NIST |
ΔvapH | [24.20; 24.20] | kJ/mol | [299.00; 299.80] | |
ΔvapH | 24.20 ± 0.10 | kJ/mol | 299.00 | NIST |
ΔvapH | 24.20 | kJ/mol | 299.80 | NIST |
ΔvapS | 80.73 | J/mol×K | 299.80 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.62] | kPa | [214.68; 321.34] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.38189e+01 | |||
Coefficient B | -2.44422e+03 | |||
Coefficient C | -3.40420e+01 | |||
Temperature range, min. | 214.68 | |||
Temperature range, max. | 321.34 | |||
Pvap | 1.33 | kPa | 214.68 | Calculated Property |
Pvap | 3.07 | kPa | 226.53 | Calculated Property |
Pvap | 6.41 | kPa | 238.38 | Calculated Property |
Pvap | 12.34 | kPa | 250.23 | Calculated Property |
Pvap | 22.21 | kPa | 262.08 | Calculated Property |
Pvap | 37.72 | kPa | 273.94 | Calculated Property |
Pvap | 60.94 | kPa | 285.79 | Calculated Property |
Pvap | 94.29 | kPa | 297.64 | Calculated Property |
Pvap | 140.51 | kPa | 309.49 | Calculated Property |
Pvap | 202.62 | kPa | 321.34 | Calculated Property |
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