Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2050 | KDB | |
PAff | 948.90 | kJ/mol | NIST |
BasG | 918.10 | kJ/mol | NIST |
ΔcH°liquid | [-2484.00; -2430.00] | kJ/mol | |
ΔcH°liquid | -2484.00 | kJ/mol | NIST |
ΔcH°liquid | -2430.00 | kJ/mol | NIST |
μ | 0.60 | debye | KDB |
ΔfG° | 98.98 | kJ/mol | KDB |
Rg | 2.7360 | KDB | |
ΔfH°gas | [-30.70; -23.70] | kJ/mol | |
ΔfH°gas | -23.86 | kJ/mol | KDB |
ΔfH°gas | -23.70 ± 0.75 | kJ/mol | NIST |
ΔfH°gas | -30.70 | kJ/mol | NIST |
ΔfH°liquid | [-52.70; -45.73] | kJ/mol | |
ΔfH°liquid | -45.73 ± 0.71 | kJ/mol | NIST |
ΔfH°liquid | -52.70 | kJ/mol | NIST |
ΔfusH° | 6.55 | kJ/mol | Joback Calculated Property |
ΔvapH° | [22.00; 22.18] | kJ/mol | |
ΔvapH° | 22.18 | kJ/mol | NIST |
ΔvapH° | 22.00 ± 0.08 | kJ/mol | NIST |
ΔvapH° | 22.00 | kJ/mol | NIST |
IE | [7.80; 8.56] | eV | |
IE | 7.85 ± 0.05 | eV | NIST |
IE | 7.80 | eV | NIST |
IE | 8.40 | eV | NIST |
IE | 7.80 ± 0.10 | eV | NIST |
IE | 7.88 | eV | NIST |
IE | 7.83 ± 0.05 | eV | NIST |
IE | 7.83 ± 0.02 | eV | NIST |
IE | 7.95 ± 0.10 | eV | NIST |
IE | 7.80 | eV | NIST |
IE | 7.82 ± 0.02 | eV | NIST |
IE | 8.54 | eV | NIST |
IE | 8.47 | eV | NIST |
IE | 8.45 | eV | NIST |
IE | 8.44 | eV | NIST |
IE | 8.56 | eV | NIST |
IE | 8.54 | eV | NIST |
IE | 8.50 | eV | NIST |
IE | 8.45 ± 0.01 | eV | NIST |
IE | 8.50 ± 0.10 | eV | NIST |
log10WS | 0.84 | Aq. Sol... | |
logPoct/wat | 0.178 | Crippen Calculated Property | |
McVol | 63.110 | ml/mol | McGowan Calculated Property |
NFPA Fire | 4 | KDB | |
NFPA Health | 2 | KDB | |
Pc | [4077.12; 4087.00] | kPa | |
Pc | 4087.00 | kPa | KDB |
Pc | 4087.00 ± 3.00 | kPa | NIST |
Pc | 4077.12 ± 10.66 | kPa | NIST |
Inp | [479.00; 518.00] | ||
Inp | 479.00 | NIST | |
Inp | 518.00 | NIST | |
Inp | 503.00 | NIST | |
Inp | 479.00 | NIST | |
I | [546.00; 610.00] | ||
I | 576.00 | NIST | |
I | 570.00 | NIST | |
I | 609.00 | NIST | |
I | 609.00 | NIST | |
I | 570.00 | NIST | |
I | 553.00 | NIST | |
I | 546.00 | NIST | |
I | 554.00 | NIST | |
I | 570.00 | NIST | |
I | 561.00 | NIST | |
I | 610.00 | NIST | |
S°liquid | 197.82 | J/mol×K | NIST |
Tboil | 276.02 | K | KDB |
Tc | [432.79; 433.30] | K | |
Tc | 432.79 | K | KDB |
Tc | 433.20 | K | NIST |
Tc | 432.79 ± 0.15 | K | NIST |
Tc | 433.30 ± 0.30 | K | NIST |
Tfus | [149.15; 156.11] | K | |
Tfus | 156.00 | K | KDB |
Tfus | 156.11 | K | Aq. Sol... |
Tfus | 155.95 ± 0.20 | K | NIST |
Tfus | 149.40 ± 0.50 | K | NIST |
Tfus | 155.95 ± 2.00 | K | NIST |
Tfus | 155.85 ± 0.50 | K | NIST |
Tfus | 149.15 ± 1.00 | K | NIST |
Ttriple | 156.08 ± 0.05 | K | NIST |
Vc | [0.254; 30.000] | m3/kmol | |
Vc | 0.254 | m3/kmol | KDB |
Vc | 30.000 ± 0.070 | m3/kmol | NIST |
Zc | 0.2884860 | KDB | |
Zra | 0.27 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [86.78; 127.54] | J/mol×K | [280.48; 439.88] | |
Cp,gas | 86.78 | J/mol×K | 280.48 | Joback Calculated Property |
Cp,gas | 94.24 | J/mol×K | 307.05 | Joback Calculated Property |
Cp,gas | 101.42 | J/mol×K | 333.61 | Joback Calculated Property |
Cp,gas | 108.34 | J/mol×K | 360.18 | Joback Calculated Property |
Cp,gas | 114.99 | J/mol×K | 386.75 | Joback Calculated Property |
Cp,gas | 121.39 | J/mol×K | 413.32 | Joback Calculated Property |
Cp,gas | 127.54 | J/mol×K | 439.88 | Joback Calculated Property |
Cp,liquid | 132.55 | J/mol×K | 280.00 | NIST |
ΔfusH | [6.54; 6.54] | kJ/mol | [156.08; 156.10] | |
ΔfusH | 6.54 | kJ/mol | 156.08 | NIST |
ΔfusH | 6.54 | kJ/mol | 156.10 | NIST |
ΔvapH | [22.94; 24.60] | kJ/mol | [234.50; 368.00] | |
ΔvapH | 24.60 | kJ/mol | 234.50 | NIST |
ΔvapH | 24.50 | kJ/mol | 250.00 | NIST |
ΔvapH | 24.10 | kJ/mol | 276.00 | KDB |
ΔvapH | 22.94 | kJ/mol | 276.00 | NIST |
ΔvapH | 22.94 ± 0.03 | kJ/mol | 276.03 | NIST |
ΔvapH | 22.94 | kJ/mol | 276.03 | NIST |
ΔvapH | 24.35 | kJ/mol | 276.20 | NIST |
ΔvapH | 24.10 | kJ/mol | 293.00 | NIST |
ΔvapH | 23.00 | kJ/mol | 368.00 | NIST |
ρl | 633.00 | kg/m3 | 293.00 | KDB |
ΔfusS | 41.93 | J/mol×K | 156.08 | NIST |
γ | 0.01 | N/m | 293.20 | KDB |
ΔvapS | 83.10 | J/mol×K | 276.03 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 4387.25] | kPa | [199.69; 433.25] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41103e+01 | |||
Coefficient B | -2.28172e+03 | |||
Coefficient C | -3.46150e+01 | |||
Temperature range, min. | 199.69 | |||
Temperature range, max. | 433.25 | |||
Pvap | 1.33 | kPa | 199.69 | Calculated Property |
Pvap | 8.72 | kPa | 225.64 | Calculated Property |
Pvap | 36.39 | kPa | 251.59 | Calculated Property |
Pvap | 111.91 | kPa | 277.54 | Calculated Property |
Pvap | 277.07 | kPa | 303.49 | Calculated Property |
Pvap | 584.76 | kPa | 329.45 | Calculated Property |
Pvap | 1093.66 | kPa | 355.40 | Calculated Property |
Pvap | 1862.47 | kPa | 381.35 | Calculated Property |
Pvap | 2945.07 | kPa | 407.30 | Calculated Property |
Pvap | 4387.25 | kPa | 433.25 | Calculated Property |
Pvap | [0.01; 4152.02] | kPa | [156.08; 433.25] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.65213e+01 | |||
Coefficient B | -5.32656e+03 | |||
Coefficient C | -1.13601e+01 | |||
Coefficient D | 1.63841e-05 | |||
Temperature range, min. | 156.08 | |||
Temperature range, max. | 433.25 | |||
Pvap | 0.01 | kPa | 156.08 | Calculated Property |
Pvap | 0.44 | kPa | 186.88 | Calculated Property |
Pvap | 5.34 | kPa | 217.67 | Calculated Property |
Pvap | 31.21 | kPa | 248.47 | Calculated Property |
Pvap | 114.84 | kPa | 279.27 | Calculated Property |
Pvap | 313.25 | kPa | 310.06 | Calculated Property |
Pvap | 700.51 | kPa | 340.86 | Calculated Property |
Pvap | 1371.39 | kPa | 371.66 | Calculated Property |
Pvap | 2456.58 | kPa | 402.45 | Calculated Property |
Pvap | 4152.02 | kPa | 433.25 | Calculated Property |
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