Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2160 | KDB | |
PAff | 846.50 | kJ/mol | NIST |
BasG | 815.30 | kJ/mol | NIST |
ΔcH°liquid | -2833.60 ± 1.10 | kJ/mol | NIST |
ΔfG° | 11.40 | kJ/mol | KDB |
ΔfH°gas | [-60.30; -59.66] | kJ/mol | |
ΔfH°gas | -59.66 | kJ/mol | KDB |
ΔfH°gas | -60.30 ± 1.10 | kJ/mol | NIST |
ΔfH°liquid | -92.30 ± 1.10 | kJ/mol | NIST |
ΔfusH° | 7.66 | kJ/mol | Joback Calculated Property |
ΔvapH° | [31.50; 32.00] | kJ/mol | |
ΔvapH° | 31.99 | kJ/mol | NIST |
ΔvapH° | 31.50 | kJ/mol | NIST |
ΔvapH° | 31.80 | kJ/mol | NIST |
ΔvapH° | 32.00 | kJ/mol | NIST |
IE | [8.46; 10.96] | eV | |
IE | 8.55 ± 0.01 | eV | NIST |
IE | 8.46 | eV | NIST |
IE | 8.50 ± 0.10 | eV | NIST |
IE | 8.55 ± 0.01 | eV | NIST |
IE | Outlier 10.96 | eV | NIST |
IE | 8.54 | eV | NIST |
log10WS | -0.96 | Crippen Calculated Property | |
logPoct/wat | 1.369 | Crippen Calculated Property | |
McVol | 69.480 | ml/mol | McGowan Calculated Property |
Pc | 4260.00 | kPa | KDB |
Inp | [605.00; 638.20] | ||
Inp | 625.00 | NIST | |
Inp | Outlier 638.20 | NIST | |
Inp | 618.80 | NIST | |
Inp | 621.90 | NIST | |
Inp | 616.00 | NIST | |
Inp | 608.00 | NIST | |
Inp | 616.00 | NIST | |
Inp | 623.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | 625.00 | NIST | |
Inp | 619.00 | NIST | |
Inp | 622.00 | NIST | |
Inp | 620.00 | NIST | |
Inp | 610.00 | NIST | |
Inp | 614.00 | NIST | |
Inp | 622.00 | NIST | |
Inp | 611.00 | NIST | |
Inp | 605.00 | NIST | |
Inp | 617.00 | NIST | |
Inp | 625.00 | NIST | |
Inp | 608.00 | NIST | |
I | [829.00; 859.00] | ||
I | 859.00 | NIST | |
I | 829.00 | NIST | |
I | 859.00 | NIST | |
I | 859.00 | NIST | |
Tboil | [335.20; 340.00] | K | |
Tboil | 339.80 | K | KDB |
Tboil | 339.80 | K | NIST |
Tboil | 339.80 | K | NIST |
Tboil | 340.00 ± 5.00 | K | NIST |
Tboil | 339.80 ± 0.30 | K | NIST |
Tboil | Outlier 335.20 ± 1.50 | K | NIST |
Tc | [533.00; 553.00] | K | |
Tc | 533.00 | K | KDB |
Tc | 553.00 | K | NIST |
Tfus | [167.20; 167.24] | K | |
Tfus | 167.20 | K | KDB |
Tfus | 167.24 ± 0.10 | K | NIST |
Ttriple | 167.23 ± 0.02 | K | NIST |
Vc | 0.258 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [103.79; 141.26] | J/mol×K | [336.82; 528.38] | |
Cp,gas | 103.79 | J/mol×K | 336.82 | Joback Calculated Property |
Cp,gas | 110.56 | J/mol×K | 368.75 | Joback Calculated Property |
Cp,gas | 117.12 | J/mol×K | 400.67 | Joback Calculated Property |
Cp,gas | 123.47 | J/mol×K | 432.60 | Joback Calculated Property |
Cp,gas | 129.61 | J/mol×K | 464.53 | Joback Calculated Property |
Cp,gas | 135.54 | J/mol×K | 496.46 | Joback Calculated Property |
Cp,gas | 141.26 | J/mol×K | 528.38 | Joback Calculated Property |
ΔfusH | [9.76; 9.76] | kJ/mol | [167.20; 167.20] | |
ΔfusH | 9.76 | kJ/mol | 167.20 | NIST |
ΔfusH | 9.76 | kJ/mol | 167.20 | NIST |
ΔvapH | [29.50; 33.70] | kJ/mol | [287.00; 340.20] | |
ΔvapH | 32.30 | kJ/mol | 287.00 | NIST |
ΔvapH | 32.00 ± 0.08 | kJ/mol | 301.00 | NIST |
ΔvapH | 31.64 | kJ/mol | 301.66 | NIST |
ΔvapH | 33.70 | kJ/mol | 308.00 | NIST |
ΔvapH | 31.80 | kJ/mol | 334.50 | NIST |
ΔvapH | 30.30 | kJ/mol | 338.00 | NIST |
ΔvapH | 29.53 | kJ/mol | 339.80 | NIST |
ΔvapH | 29.50 | kJ/mol | 340.20 | KDB |
Pvap | [1.00; 40.00] | kPa | [247.76; 313.35] | |
Pvap | 1.00 | kPa | 247.76 | Measure... |
Pvap | 6.00 | kPa | 272.96 | Measure... |
Pvap | 17.00 | kPa | 293.23 | Measure... |
Pvap | 17.00 | kPa | 293.41 | Measure... |
Pvap | 40.00 | kPa | 313.33 | Measure... |
Pvap | 40.00 | kPa | 313.35 | Measure... |
ρl | 837.00 | kg/m3 | 293.00 | KDB |
γ | 0.03 | N/m | 293.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 4259.64] | kPa | [247.75; 533.00] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.39945e+01 | |||
Coefficient B | -2.73161e+03 | |||
Coefficient C | -4.84660e+01 | |||
Temperature range, min. | 247.75 | |||
Temperature range, max. | 533.00 | |||
Pvap | 1.33 | kPa | 247.75 | Calculated Property |
Pvap | 8.74 | kPa | 279.44 | Calculated Property |
Pvap | 36.43 | kPa | 311.14 | Calculated Property |
Pvap | 111.60 | kPa | 342.83 | Calculated Property |
Pvap | 275.05 | kPa | 374.53 | Calculated Property |
Pvap | 577.75 | kPa | 406.22 | Calculated Property |
Pvap | 1075.49 | kPa | 437.92 | Calculated Property |
Pvap | 1823.28 | kPa | 469.61 | Calculated Property |
Pvap | 2870.84 | kPa | 501.31 | Calculated Property |
Pvap | 4259.64 | kPa | 533.00 | Calculated Property |
Pvap | [1.30; 4251.33] | kPa | [247.15; 532.80] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.85436e+01 | |||
Coefficient B | -6.34327e+03 | |||
Coefficient C | -9.63519e+00 | |||
Coefficient D | 7.77843e-06 | |||
Temperature range, min. | 247.15 | |||
Temperature range, max. | 532.80 | |||
Pvap | 1.30 | kPa | 247.15 | Calculated Property |
Pvap | 8.58 | kPa | 278.89 | Calculated Property |
Pvap | 35.90 | kPa | 310.63 | Calculated Property |
Pvap | 109.70 | kPa | 342.37 | Calculated Property |
Pvap | 268.35 | kPa | 374.11 | Calculated Property |
Pvap | 559.06 | kPa | 405.84 | Calculated Property |
Pvap | 1035.51 | kPa | 437.58 | Calculated Property |
Pvap | 1758.46 | kPa | 469.32 | Calculated Property |
Pvap | 2800.03 | kPa | 501.06 | Calculated Property |
Pvap | 4251.33 | kPa | 532.80 | Calculated Property |
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