Property | Value | Unit | Source |
---|---|---|---|
ω | 0.1350 | KDB | |
PAff | 568.40 | kJ/mol | NIST |
BasG | [538.60; 554.00] | kJ/mol | |
BasG | 538.60 | kJ/mol | NIST |
BasG | 554.00 | kJ/mol | NIST |
μ | 0.20 | debye | KDB |
ΔfG° | -90.10 | kJ/mol | KDB |
ΔfH°gas | -131.60 | kJ/mol | KDB |
ΔfusH° | 8.02 | kJ/mol | Joback Calculated Property |
ΔvapH° | 15.19 | kJ/mol | Joback Calculated Property |
IE | [12.94; 13.83] | eV | |
IE | 12.94 ± 0.01 | eV | NIST |
IE | 13.50 ± 0.20 | eV | NIST |
IE | 12.94 ± 0.01 | eV | NIST |
IE | 13.00 | eV | NIST |
IE | 13.10 ± 0.06 | eV | NIST |
IE | 12.97 ± 0.04 | eV | NIST |
IE | 13.20 ± 0.10 | eV | NIST |
IE | 13.00 ± 0.02 | eV | NIST |
IE | 13.60 ± 0.20 | eV | NIST |
IE | 13.83 | eV | NIST |
IE | 13.75 | eV | NIST |
IE | 13.73 | eV | NIST |
IE | 13.73 ± 0.03 | eV | NIST |
log10WS | -0.92 | Crippen Calculated Property | |
logPoct/wat | 0.942 | Crippen Calculated Property | |
McVol | 26.150 | ml/mol | McGowan Calculated Property |
Pc | 4460.00 | kPa | KDB |
Tboil | [144.00; 144.40] | K | |
Tboil | 144.40 | K | KDB |
Tboil | 144.00 ± 1.50 | K | NIST |
Tboil | 144.20 ± 0.40 | K | NIST |
Tc | 234.00 | K | KDB |
Tfus | [64.70; 66.36] | K | |
Tfus | 66.36 | K | KDB |
Tfus | 64.70 ± 0.50 | K | NIST |
Vc | 0.126 | m3/kmol | KDB |
Zc | 0.2888370 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [38.99; 51.05] | J/mol×K | [209.65; 332.82] | |
T(K) Ideal gas heat capacity (J/mol×K) 38 40 42 44 46 48 50 52 250 300 | ||||
Cp,gas | 38.99 | J/mol×K | 209.65 | Joback Calculated Property |
Cp,gas | 41.22 | J/mol×K | 230.18 | Joback Calculated Property |
Cp,gas | 43.36 | J/mol×K | 250.71 | Joback Calculated Property |
Cp,gas | 45.41 | J/mol×K | 271.23 | Joback Calculated Property |
Cp,gas | 47.38 | J/mol×K | 291.76 | Joback Calculated Property |
Cp,gas | 49.26 | J/mol×K | 312.29 | Joback Calculated Property |
Cp,gas | 51.05 | J/mol×K | 332.82 | Joback Calculated Property |
ρl | 1540.00 | kg/m3 | 144.00 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [2.63e-04; 4520.50] | kPa | [66.36; 233.85] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41411e+01 | |||
Coefficient B | -1.28834e+03 | |||
Coefficient C | -8.80000e+00 | |||
Temperature range, min. | 66.36 | |||
Temperature range, max. | 233.85 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 100 150 200 | ||||
Pvap | 2.63e-04 | kPa | 66.36 | Calculated Property |
Pvap | 0.06 | kPa | 84.97 | Calculated Property |
Pvap | 1.73 | kPa | 103.58 | Calculated Property |
Pvap | 16.10 | kPa | 122.19 | Calculated Property |
Pvap | 79.91 | kPa | 140.80 | Calculated Property |
Pvap | 266.91 | kPa | 159.41 | Calculated Property |
Pvap | 683.80 | kPa | 178.02 | Calculated Property |
Pvap | 1453.88 | kPa | 196.63 | Calculated Property |
Pvap | 2698.13 | kPa | 215.24 | Calculated Property |
Pvap | 4520.50 | kPa | 233.85 | Calculated Property |
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