Property | Value | Unit | Source |
---|---|---|---|
PAff | 924.80 | kJ/mol | NIST |
BasG | 890.80 | kJ/mol | NIST |
ΔcH°liquid | [-3013.50; -2987.00] | kJ/mol | |
ΔcH°liquid | -3013.50 ± 0.42 | kJ/mol | NIST |
ΔcH°liquid | -2987.00 | kJ/mol | NIST |
ΔfG° | 46.81 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-144.10; -98.62] | kJ/mol | |
ΔfH°gas | -98.62 ± 0.54 | kJ/mol | NIST |
ΔfH°gas | -144.10 | kJ/mol | NIST |
ΔfH°liquid | [-178.00; -132.50] | kJ/mol | |
ΔfH°liquid | -132.50 ± 0.50 | kJ/mol | NIST |
ΔfH°liquid | -178.00 | kJ/mol | NIST |
ΔfusH° | 7.79 | kJ/mol | Joback Calculated Property |
ΔvapH° | 34.75 | kJ/mol | Joback Calculated Property |
IE | [8.50; 8.70] | eV | |
IE | 8.50 ± 0.10 | eV | NIST |
IE | 8.70 | eV | NIST |
log10WS | -0.69 | Crippen Calculated Property | |
logPoct/wat | 0.601 | Crippen Calculated Property | |
McVol | 77.200 | ml/mol | McGowan Calculated Property |
Pc | 4233.04 | kPa | Joback Calculated Property |
Inp | [543.00; 605.00] | ||
Inp | 600.00 | NIST | |
Inp | 605.00 | NIST | |
Inp | 581.00 | NIST | |
Inp | 548.00 | NIST | |
Inp | Outlier 543.00 | NIST | |
Inp | 591.00 | NIST | |
Inp | 591.00 | NIST | |
Inp | 588.00 | NIST | |
Inp | 588.00 | NIST | |
Inp | 591.00 | NIST | |
Inp | 600.00 | NIST | |
I | [840.00; 860.00] | ||
I | 842.00 | NIST | |
I | 842.00 | NIST | |
I | 860.00 | NIST | |
I | 855.00 | NIST | |
I | 840.00 | NIST | |
I | 842.00 | NIST | |
Tboil | [340.15; 342.00] | K | |
Tboil | 341.70 | K | NIST |
Tboil | 340.70 | K | NIST |
Tboil | 342.00 ± 3.00 | K | NIST |
Tboil | 341.15 ± 1.50 | K | NIST |
Tboil | 340.85 ± 0.30 | K | NIST |
Tboil | 340.15 ± 1.00 | K | NIST |
Tboil | 341.15 ± 2.00 | K | NIST |
Tboil | 341.15 ± 0.50 | K | NIST |
Tboil | 341.65 ± 1.50 | K | NIST |
Tc | 516.90 | K | NIST |
Tfus | [186.50; 188.55] | K | |
Tfus | 186.50 ± 0.50 | K | NIST |
Tfus | 188.55 ± 1.50 | K | NIST |
Tfus | 187.65 ± 0.50 | K | NIST |
Vc | 0.282 | m3/kmol | Joback Calculated Property |
Vm | 1.01e-04 | m3/mol | Thermod... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [138.58; 187.35] | J/mol×K | [363.01; 549.17] | |
Cp,gas | 138.58 | J/mol×K | 363.01 | Joback Calculated Property |
Cp,gas | 147.57 | J/mol×K | 394.04 | Joback Calculated Property |
Cp,gas | 156.20 | J/mol×K | 425.06 | Joback Calculated Property |
Cp,gas | 164.49 | J/mol×K | 456.09 | Joback Calculated Property |
Cp,gas | 172.44 | J/mol×K | 487.12 | Joback Calculated Property |
Cp,gas | 180.06 | J/mol×K | 518.14 | Joback Calculated Property |
Cp,gas | 187.35 | J/mol×K | 549.17 | Joback Calculated Property |
Cp,liquid | 194.00 | J/mol×K | 298.15 | NIST |
ΔvapH | [30.61; 37.60] | kJ/mol | [297.50; 340.70] | |
ΔvapH | 37.60 | kJ/mol | 297.50 | NIST |
ΔvapH | 32.70 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 33.50 | kJ/mol | 318.50 | NIST |
ΔvapH | 31.60 ± 0.10 | kJ/mol | 328.00 | NIST |
ΔvapH | 30.61 | kJ/mol | 340.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [2.86e-03; 20044.30] | kPa | [188.55; 664.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.78232e+01 | |||
Coefficient B | -6.17764e+03 | |||
Coefficient C | -7.84560e+00 | |||
Coefficient D | 5.37349e-06 | |||
Temperature range, min. | 188.55 | |||
Temperature range, max. | 664.00 | |||
Pvap | 2.86e-03 | kPa | 188.55 | Calculated Property |
Pvap | 0.61 | kPa | 241.38 | Calculated Property |
Pvap | 14.79 | kPa | 294.21 | Calculated Property |
Pvap | 118.72 | kPa | 347.03 | Calculated Property |
Pvap | 507.22 | kPa | 399.86 | Calculated Property |
Pvap | 1480.78 | kPa | 452.69 | Calculated Property |
Pvap | 3403.17 | kPa | 505.52 | Calculated Property |
Pvap | 6706.84 | kPa | 558.34 | Calculated Property |
Pvap | 11967.67 | kPa | 611.17 | Calculated Property |
Pvap | 20044.30 | kPa | 664.00 | Calculated Property |
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