Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3880 | KDB | |
PAff | 712.90 | kJ/mol | NIST |
BasG | 681.60 | kJ/mol | NIST |
μ | 3.00 | debye | KDB |
EA | [0.00; 1.00] | eV | |
EA | 0.00 | eV | NIST |
EA | 1.00 | eV | NIST |
ΔfG° | 120.20 | kJ/mol | KDB |
ΔfH°gas | 130.60 | kJ/mol | KDB |
ΔfusH° | 1.53 | kJ/mol | Joback Calculated Property |
ΔvapH° | 28.15 | kJ/mol | Joback Calculated Property |
IE | [13.59; 13.73] | eV | |
IE | 13.60 ± 0.01 | eV | NIST |
IE | 13.71 | eV | NIST |
IE | 13.59 ± 0.01 | eV | NIST |
IE | 13.60 ± 0.01 | eV | NIST |
IE | 13.73 ± 0.09 | eV | NIST |
IE | 13.70 ± 0.10 | eV | NIST |
IE | 13.61 | eV | NIST |
IE | 13.61 ± 0.00 | eV | NIST |
IE | 13.60 | eV | NIST |
IE | 13.61 ± 0.01 | eV | NIST |
log10WS | -0.11 | Crippen Calculated Property | |
logPoct/wat | 0.140 | Crippen Calculated Property | |
McVol | 26.330 | ml/mol | McGowan Calculated Property |
NFPA Fire | 4 | KDB | |
NFPA Health | 4 | KDB | |
NFPA Safety | 2 | KDB | |
Pc | 5390.00 | kPa | KDB |
Inp | [300.00; 320.00] | ||
Inp | 319.90 | NIST | |
Inp | 300.00 | NIST | |
Inp | 320.00 | NIST | |
Inp | 319.90 | NIST | |
S°liquid | 113.01 | J/mol×K | NIST |
Tboil | [298.80; 299.70] | K | |
Tboil | 299.00 | K | KDB |
Tboil | 298.90 ± 0.50 | K | NIST |
Tboil | 298.90 ± 0.40 | K | NIST |
Tboil | 299.00 ± 0.40 | K | NIST |
Tboil | 299.00 ± 1.50 | K | NIST |
Tboil | 298.90 ± 0.50 | K | NIST |
Tboil | 299.08 ± 0.40 | K | NIST |
Tboil | 298.90 ± 0.50 | K | NIST |
Tboil | 298.80 ± 0.50 | K | NIST |
Tboil | 298.90 ± 0.30 | K | NIST |
Tboil | 298.90 ± 0.40 | K | NIST |
Tboil | 299.50 ± 1.00 | K | NIST |
Tboil | 298.90 ± 1.00 | K | NIST |
Tboil | Outlier 299.70 ± 0.50 | K | NIST |
Tboil | 298.90 ± 0.50 | K | NIST |
Tboil | 299.40 ± 0.60 | K | NIST |
Tc | 456.70 | K | KDB |
Tfus | [258.29; 286.50] | K | |
Tfus | 259.70 | K | KDB |
Tfus | 259.85 ± 0.20 | K | NIST |
Tfus | 259.90 ± 0.10 | K | NIST |
Tfus | 259.88 ± 0.10 | K | NIST |
Tfus | 259.86 ± 0.05 | K | NIST |
Tfus | 258.30 ± 1.00 | K | NIST |
Tfus | Outlier 286.50 ± 0.20 | K | NIST |
Tfus | 259.20 ± 0.50 | K | NIST |
Tfus | 259.00 ± 1.50 | K | NIST |
Tfus | 258.29 ± 1.00 | K | NIST |
Tfus | 259.75 ± 0.30 | K | NIST |
Tfus | 259.80 ± 0.20 | K | NIST |
Tfus | 259.85 ± 0.30 | K | NIST |
Tfus | 259.81 ± 0.50 | K | NIST |
Tfus | 259.75 ± 0.50 | K | NIST |
Ttriple | 259.86 ± 0.02 | K | NIST |
Vc | 0.139 | m3/kmol | KDB |
Zc | 0.1973040 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [24.62; 28.13] | J/mol×K | [323.66; 514.23] | |
T(K) Ideal gas heat capacity (J/mol×K) 24.5 25 25.5 26 26.5 27 27.5 28 350 400 450 500 | ||||
Cp,gas | 24.62 | J/mol×K | 323.66 | Joback Calculated Property |
Cp,gas | 25.63 | J/mol×K | 355.42 | Joback Calculated Property |
Cp,gas | 26.44 | J/mol×K | 387.18 | Joback Calculated Property |
Cp,gas | 27.08 | J/mol×K | 418.95 | Joback Calculated Property |
Cp,gas | 27.56 | J/mol×K | 450.71 | Joback Calculated Property |
Cp,gas | 27.91 | J/mol×K | 482.47 | Joback Calculated Property |
Cp,gas | 28.13 | J/mol×K | 514.23 | Joback Calculated Property |
Cp,liquid | 71.00 | J/mol×K | 300.00 | NIST |
ΔfusH | 8.41 | kJ/mol | 259.90 | NIST |
ΔsubH | [35.60; 37.60] | kJ/mol | [228.00; 247.50] | |
ΔsubH | 37.60 | kJ/mol | 228.00 | NIST |
ΔsubH | 35.60 | kJ/mol | 247.50 | NIST |
ΔvapH | [25.22; 28.10] | kJ/mol | [276.50; 377.50] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 25 25.5 26 26.5 27 27.5 28 300 350 | ||||
ΔvapH | 28.00 | kJ/mol | 276.50 | NIST |
ΔvapH | 28.10 | kJ/mol | 279.00 | NIST |
ΔvapH | 27.80 | kJ/mol | 282.50 | NIST |
ΔvapH | 28.10 | kJ/mol | 286.00 | NIST |
ΔvapH | 27.20 | kJ/mol | 287.50 | NIST |
ΔvapH | 28.10 | kJ/mol | 288.00 | NIST |
ΔvapH | 25.22 | kJ/mol | 298.85 | NIST |
ΔvapH | 27.80 | kJ/mol | 377.50 | NIST |
ρl | 688.00 | kg/m3 | 293.00 | KDB |
ΔfusS | 32.34 | J/mol×K | 259.90 | NIST |
ΔvapS | 84.38 | J/mol×K | 298.85 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 5289.38] | kPa | [215.04; 456.65] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.64196e+01 | |||
Coefficient B | -3.69077e+03 | |||
Coefficient C | 1.37430e+01 | |||
Temperature range, min. | 215.04 | |||
Temperature range, max. | 456.65 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 | ||||
Pvap | 1.33 | kPa | 215.04 | Calculated Property |
Pvap | 7.25 | kPa | 241.89 | Calculated Property |
Pvap | 28.61 | kPa | 268.73 | Calculated Property |
Pvap | 88.92 | kPa | 295.58 | Calculated Property |
Pvap | 230.57 | kPa | 322.42 | Calculated Property |
Pvap | 519.30 | kPa | 349.27 | Calculated Property |
Pvap | 1045.86 | kPa | 376.11 | Calculated Property |
Pvap | 1924.65 | kPa | 402.96 | Calculated Property |
Pvap | 3289.76 | kPa | 429.80 | Calculated Property |
Pvap | 5289.38 | kPa | 456.65 | Calculated Property |
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