Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2780 | KDB | |
PAff | 674.70 | kJ/mol | NIST |
BasG | [621.70; 645.80] | kJ/mol | |
BasG | 645.80 | kJ/mol | NIST |
BasG | 622.80 | kJ/mol | NIST |
BasG | 621.70 | kJ/mol | NIST |
BasG | 642.00 | kJ/mol | NIST |
ΔcH°gas | [-1096.00; -1051.90] | kJ/mol | |
ΔcH°gas | -1096.00 ± 1.80 | kJ/mol | NIST |
ΔcH°gas | -1051.90 ± 5.00 | kJ/mol | NIST |
ΔcH°gas | -1093.70 ± 0.84 | kJ/mol | NIST |
μ | 0.20 | debye | KDB |
ΔfG° | 297.40 | kJ/mol | KDB |
ΔfH°gas | [263.00; 309.20] | kJ/mol | |
ΔfH°gas | 309.20 | kJ/mol | KDB |
ΔfH°gas | 308.90 ± 1.80 | kJ/mol | NIST |
ΔfH°gas | 263.00 | kJ/mol | NIST |
ΔfH°gas | 306.70 ± 0.84 | kJ/mol | NIST |
ΔfusH° | 3.95 | kJ/mol | Joback Calculated Property |
ΔvapH° | 20.80 | kJ/mol | NIST |
IE | [13.36; 13.51] | eV | |
IE | 13.37 ± 0.01 | eV | NIST |
IE | 13.50 ± 0.30 | eV | NIST |
IE | 13.36 ± 0.01 | eV | NIST |
IE | 13.37 ± 0.01 | eV | NIST |
IE | 13.50 | eV | NIST |
IE | 13.51 | eV | NIST |
log10WS | -0.39 | Crippen Calculated Property | |
logPoct/wat | 0.034 | Crippen Calculated Property | |
McVol | 41.800 | ml/mol | McGowan Calculated Property |
Pc | 5980.00 | kPa | KDB |
Ptriple | 75.10 ± 1.33 | kPa | NIST |
Inp | [259.20; 273.00] | ||
Inp | 259.20 | NIST | |
Inp | 273.00 | NIST | |
Inp | 259.20 | NIST | |
S°liquid | 138.83 | J/mol×K | NIST |
Tboil | [252.00; 252.00] | K | |
Tboil | 252.00 | K | KDB |
Tboil | 252.00 | K | NIST |
Tboil | 252.00 | K | NIST |
Tc | 400.00 | K | KDB |
Tfus | 245.20 | K | KDB |
Ttriple | 245.32 ± 0.02 | K | NIST |
Vc | 0.200 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [58.91; 67.25] | J/mol×K | [449.32; 670.74] | |
Cp,gas | 58.91 | J/mol×K | 449.32 | Joback Calculated Property |
Cp,gas | 60.46 | J/mol×K | 486.22 | Joback Calculated Property |
Cp,gas | 61.94 | J/mol×K | 523.13 | Joback Calculated Property |
Cp,gas | 63.36 | J/mol×K | 560.03 | Joback Calculated Property |
Cp,gas | 64.72 | J/mol×K | 596.93 | Joback Calculated Property |
Cp,gas | 66.02 | J/mol×K | 633.84 | Joback Calculated Property |
Cp,gas | 67.25 | J/mol×K | 670.74 | Joback Calculated Property |
Cp,liquid | 105.73 | J/mol×K | 255.00 | NIST |
ΔfusH | [8.11; 8.11] | kJ/mol | [245.30; 245.32] | |
ΔfusH | 8.11 | kJ/mol | 245.30 | NIST |
ΔfusH | 8.11 | kJ/mol | 245.32 | NIST |
ΔsubH | [32.40; 34.40] | kJ/mol | [203.50; 223.50] | |
ΔsubH | 33.60 | kJ/mol | 203.50 | NIST |
ΔsubH | 32.40 | kJ/mol | 219.00 | NIST |
ΔsubH | 33.00 | kJ/mol | 220.50 | NIST |
ΔsubH | 34.40 | kJ/mol | 223.50 | NIST |
ΔvapH | [23.30; 24.50] | kJ/mol | [246.50; 259.50] | |
ΔvapH | 24.50 | kJ/mol | 246.50 | NIST |
ΔvapH | 23.30 ± 0.20 | kJ/mol | 251.95 | NIST |
ΔvapH | 23.33 | kJ/mol | 252.00 | NIST |
ΔvapH | 23.33 | kJ/mol | 252.00 | NIST |
ΔvapH | 23.90 | kJ/mol | 259.50 | NIST |
ΔvapH | 23.50 | kJ/mol | 259.50 | NIST |
ρl | 954.00 | kg/m3 | 252.00 | KDB |
ΔfusS | 33.05 | J/mol×K | 245.32 | NIST |
γ | 0.02 | N/m | 217.00 | KDB |
ΔvapS | 92.58 | J/mol×K | 252.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 5979.48] | kPa | [191.32; 400.15] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.39745e+01 | |||
Coefficient B | -1.79426e+03 | |||
Coefficient C | -6.02280e+01 | |||
Temperature range, min. | 191.32 | |||
Temperature range, max. | 400.15 | |||
Pvap | 1.33 | kPa | 191.32 | Calculated Property |
Pvap | 10.44 | kPa | 214.52 | Calculated Property |
Pvap | 47.75 | kPa | 237.73 | Calculated Property |
Pvap | 153.64 | kPa | 260.93 | Calculated Property |
Pvap | 388.02 | kPa | 284.13 | Calculated Property |
Pvap | 823.46 | kPa | 307.34 | Calculated Property |
Pvap | 1535.79 | kPa | 330.54 | Calculated Property |
Pvap | 2595.50 | kPa | 353.74 | Calculated Property |
Pvap | 4061.80 | kPa | 376.95 | Calculated Property |
Pvap | 5979.48 | kPa | 400.15 | Calculated Property |
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