Property | Value | Unit | Source |
---|---|---|---|
ω | 0.1050 | KDB | |
PAff | 628.50 | kJ/mol | NIST |
BasG | 602.60 | kJ/mol | NIST |
μ | 0.70 | debye | KDB |
EA | [0.40; 0.46] | eV | |
EA | 0.46 ± 0.20 | eV | NIST |
EA | 0.40 | eV | NIST |
ΔfG° | -165.80 | kJ/mol | KDB |
ΔfH°gas | [-139.00; -138.50] | kJ/mol | |
ΔfH°gas | -138.50 | kJ/mol | KDB |
ΔfH°gas | -139.00 ± 1.00 | kJ/mol | NIST |
ΔfH°gas | -139.00 ± 1.00 | kJ/mol | NIST |
ΔfH°(+) ion | 937.00 | kJ/mol | NIST |
ΔfH(+) ion,0K | 937.00 | kJ/mol | NIST |
ΔfusH° | 11.59 | kJ/mol | Joback Calculated Property |
ΔvapH° | 30.69 | kJ/mol | Joback Calculated Property |
IE | [11.00; 11.30] | eV | |
IE | 11.18 ± 0.01 | eV | NIST |
IE | 11.19 ± 0.00 | eV | NIST |
IE | Outlier 11.00 ± 1.00 | eV | NIST |
IE | 11.17 ± 0.00 | eV | NIST |
IE | 11.18 ± 0.00 | eV | NIST |
IE | 11.19 ± 0.05 | eV | NIST |
IE | 11.17 ± 0.00 | eV | NIST |
IE | 11.19 | eV | NIST |
IE | 11.22 | eV | NIST |
IE | 11.18 ± 0.01 | eV | NIST |
IE | Outlier 11.30 | eV | NIST |
IE | 11.19 ± 0.01 | eV | NIST |
IE | 11.23 ± 0.01 | eV | NIST |
IE | 11.18 ± 0.01 | eV | NIST |
IE | 11.18 ± 0.01 | eV | NIST |
IE | 11.22 ± 0.01 | eV | NIST |
IE | 11.23 ± 0.01 | eV | NIST |
IE | 11.18 ± 0.01 | eV | NIST |
IE | 11.22 | eV | NIST |
IE | 11.19 | eV | NIST |
log10WS | -4.93 | Crippen Calculated Property | |
logPoct/wat | 0.251 | Crippen Calculated Property | |
McVol | 38.570 | ml/mol | McGowan Calculated Property |
NFPA Fire | 4 | KDB | |
NFPA Health | 3 | KDB | |
NFPA Safety | 1 | KDB | |
Pc | [5880.00; 6349.00] | kPa | |
Pc | 5880.00 | kPa | KDB |
Pc | 6349.00 ± 5.00 | kPa | NIST |
Inp | [277.00; 305.00] | ||
Inp | 301.00 | NIST | |
Inp | 303.00 | NIST | |
Inp | 304.00 | NIST | |
Inp | 305.00 | NIST | |
Inp | 277.00 | NIST | |
Inp | 277.00 | NIST | |
I | [680.00; 680.00] | ||
I | 680.00 | NIST | |
I | 680.00 | NIST | |
S°liquid | 136.31 | J/mol×K | NIST |
Tboil | 223.00 | K | KDB |
Tc | [375.00; 378.80] | K | |
Tc | 375.00 | K | KDB |
Tc | 378.80 ± 0.10 | K | NIST |
Tfus | 134.30 | K | KDB |
Ttriple | [134.31; 134.33] | K | |
Ttriple | 134.31 ± 0.20 | K | NIST |
Ttriple | 134.33 ± 0.02 | K | NIST |
Vc | [0.135; 0.137] | m3/kmol | |
Vc | 0.137 | m3/kmol | KDB |
Vc | 0.135 ± 0.002 | m3/kmol | NIST |
Zc | 0.2583630 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [46.99; 53.92] | J/mol×K | [282.43; 462.27] | |
T(K) Ideal gas heat capacity (J/mol×K) 47 48 49 50 51 52 53 54 300 350 400 450 | ||||
Cp,gas | 46.99 | J/mol×K | 282.43 | Joback Calculated Property |
Cp,gas | 48.69 | J/mol×K | 312.40 | Joback Calculated Property |
Cp,gas | 50.15 | J/mol×K | 342.38 | Joback Calculated Property |
Cp,gas | 51.38 | J/mol×K | 372.35 | Joback Calculated Property |
Cp,gas | 52.41 | J/mol×K | 402.32 | Joback Calculated Property |
Cp,gas | 53.25 | J/mol×K | 432.30 | Joback Calculated Property |
Cp,gas | 53.92 | J/mol×K | 462.27 | Joback Calculated Property |
Cp,liquid | 71.25 | J/mol×K | 220.00 | NIST |
ΔfusH | [4.73; 4.73] | kJ/mol | [134.30; 134.33] | |
ΔfusH | 4.73 | kJ/mol | 134.30 | NIST |
ΔfusH | 4.73 | kJ/mol | 134.33 | NIST |
ΔvapH | [18.30; 20.89] | kJ/mol | [182.00; 331.50] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 18.5 19 19.5 20 20.5 21 200 250 300 | ||||
ΔvapH | 19.50 | kJ/mol | 182.00 | NIST |
ΔvapH | 19.50 | kJ/mol | 193.00 | NIST |
ΔvapH | 19.00 ± 0.10 | kJ/mol | 214.00 | NIST |
ΔvapH | 20.40 | kJ/mol | 222.50 | NIST |
ΔvapH | 20.89 | kJ/mol | 222.90 | KDB |
ΔvapH | 18.51 | kJ/mol | 222.91 | NIST |
ΔvapH | 18.30 | kJ/mol | 331.50 | NIST |
Pvap | [282.15; 651.42] | kPa | [248.15; 273.15] | |
Pvap | 282.15 | kPa | 248.15 | Vapor L... |
Pvap | 287.13 | kPa | 248.15 | Vapor L... |
Pvap | 638.23 | kPa | 273.15 | Vapor L... |
Pvap | 651.42 | kPa | 273.15 | Vapor L... |
ρl | 1274.00 | kg/m3 | 174.00 | KDB |
ΔfusS | 35.20 | J/mol×K | 134.33 | NIST |
γ | 0.02 | N/m | 218.20 | KDB |
ΔvapS | 83.02 | J/mol×K | 222.91 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 6352.00] | kPa | [159.78; 378.77] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41200e+01 | |||
Coefficient B | -1.91842e+03 | |||
Coefficient C | -2.10860e+01 | |||
Temperature range, min. | 159.78 | |||
Temperature range, max. | 378.77 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 200 250 300 350 | ||||
Pvap | 1.33 | kPa | 159.78 | Calculated Property |
Pvap | 10.51 | kPa | 184.11 | Calculated Property |
Pvap | 48.46 | kPa | 208.44 | Calculated Property |
Pvap | 157.21 | kPa | 232.78 | Calculated Property |
Pvap | 400.16 | kPa | 257.11 | Calculated Property |
Pvap | 855.34 | kPa | 281.44 | Calculated Property |
Pvap | 1605.65 | kPa | 305.77 | Calculated Property |
Pvap | 2729.54 | kPa | 330.11 | Calculated Property |
Pvap | 4294.25 | kPa | 354.44 | Calculated Property |
Pvap | 6352.00 | kPa | 378.77 | Calculated Property |
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