Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2670 | KDB | |
PAff | 688.40 | kJ/mol | NIST |
BasG | 657.70 | kJ/mol | NIST |
ΔfG° | -462.20 | kJ/mol | KDB |
ΔfH°gas | [-496.60; -460.00] | kJ/mol | |
ΔfH°gas | -495.70 | kJ/mol | KDB |
ΔfH°gas | -460.00 ± 30.00 | kJ/mol | NIST |
ΔfH°gas | -496.60 ± 0.63 | kJ/mol | NIST |
ΔfusH° | 4.27 | kJ/mol | Joback Calculated Property |
ΔvapH° | 26.78 | kJ/mol | Joback Calculated Property |
IE | [13.86; 14.30] | eV | |
IE | 13.93 ± 0.07 | eV | NIST |
IE | 14.00 | eV | NIST |
IE | 13.86 | eV | NIST |
IE | 14.30 | eV | NIST |
log10WS | -1.19 | Crippen Calculated Property | |
logPoct/wat | 1.072 | Crippen Calculated Property | |
McVol | 45.730 | ml/mol | McGowan Calculated Property |
Pc | [3618.00; 3618.00] | kPa | |
Pc | 3618.00 | kPa | KDB |
Pc | 3618.00 ± 3.44 | kPa | NIST |
ρc | 470.37 ± 4.69 | kg/m3 | NIST |
Inp | [246.00; 246.00] | ||
Inp | 246.00 | NIST | |
Inp | 246.00 | NIST | |
S°liquid | 184.43 | J/mol×K | NIST |
Tboil | [204.33; 209.00] | K | |
Tboil | 204.33 | K | KDB |
Tboil | 209.00 | K | NIST |
Tboil | 209.00 | K | NIST |
Tc | [311.11; 311.11] | K | |
Tc | 311.11 | K | KDB |
Tc | 311.11 ± 0.20 | K | NIST |
Tfus | 181.48 | K | Joback Calculated Property |
Ttriple | 128.73 ± 0.02 | K | NIST |
Vc | 0.202 | m3/kmol | KDB |
Zc | 0.2825330 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [82.59; 101.24] | J/mol×K | [341.82; 516.00] | |
T(K) Ideal gas heat capacity (J/mol×K) 85 90 95 100 350 400 450 500 | ||||
Cp,gas | 82.59 | J/mol×K | 341.82 | Joback Calculated Property |
Cp,gas | 86.37 | J/mol×K | 370.85 | Joback Calculated Property |
Cp,gas | 89.86 | J/mol×K | 399.88 | Joback Calculated Property |
Cp,gas | 93.07 | J/mol×K | 428.91 | Joback Calculated Property |
Cp,gas | 96.03 | J/mol×K | 457.94 | Joback Calculated Property |
Cp,gas | 98.75 | J/mol×K | 486.97 | Joback Calculated Property |
Cp,gas | 101.24 | J/mol×K | 516.00 | Joback Calculated Property |
Cp,liquid | 118.11 | J/mol×K | 205.00 | NIST |
ΔfusH | [4.97; 4.97] | kJ/mol | [128.70; 128.73] | |
ΔfusH | 4.97 | kJ/mol | 128.70 | NIST |
ΔfusH | 4.97 | kJ/mol | 128.70 | NIST |
ΔfusH | 4.97 | kJ/mol | 128.73 | NIST |
ΔvapH | [17.40; 19.30] | kJ/mol | [172.00; 309.00] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 17.5 18 18.5 19 200 250 300 | ||||
ΔvapH | 19.20 | kJ/mol | 172.00 | NIST |
ΔvapH | 19.20 | kJ/mol | 174.00 | NIST |
ΔvapH | 19.30 | kJ/mol | 178.50 | NIST |
ΔvapH | 17.83 | kJ/mol | 205.47 | NIST |
ΔvapH | 18.50 | kJ/mol | 219.00 | NIST |
ΔvapH | 17.40 | kJ/mol | 291.50 | NIST |
ΔvapH | 17.40 | kJ/mol | 309.00 | NIST |
ΔfusS | 38.62 | J/mol×K | 128.73 | NIST |
ΔvapS | 86.79 | J/mol×K | 205.47 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.00; 202.64] | kPa | [147.05; 217.38] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.56198e+01 | |||
Coefficient B | -2.13202e+03 | |||
Coefficient C | -1.05560e+01 | |||
Temperature range, min. | 147.05 | |||
Temperature range, max. | 217.38 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 160 180 200 | ||||
Pvap | 1.00 | kPa | 147.05 | Calculated Property |
Pvap | 2.33 | kPa | 154.86 | Calculated Property |
Pvap | 4.98 | kPa | 162.68 | Calculated Property |
Pvap | 9.87 | kPa | 170.49 | Calculated Property |
Pvap | 18.36 | kPa | 178.31 | Calculated Property |
Pvap | 32.33 | kPa | 186.12 | Calculated Property |
Pvap | 54.25 | kPa | 193.94 | Calculated Property |
Pvap | 87.25 | kPa | 201.75 | Calculated Property |
Pvap | 135.19 | kPa | 209.57 | Calculated Property |
Pvap | 202.64 | kPa | 217.38 | Calculated Property |
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