Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -2030.00 ± 3.00 | kJ/mol | NIST |
ΔfG° | -27.90 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -11.70 ± 4.40 | kJ/mol | NIST |
ΔfH°liquid | -79.20 ± 3.10 | kJ/mol | NIST |
ΔfusH° | 22.41 | kJ/mol | Joback Calculated Property |
ΔvapH° | 67.00 ± 1.00 | kJ/mol | NIST |
log10WS | -5.18 | Aq. Sol... | |
logPoct/wat | 4.552 | Crippen Calculated Property | |
McVol | 135.290 | ml/mol | McGowan Calculated Property |
Pc | 3530.46 | kPa | Joback Calculated Property |
Inp | [228.10; 1328.00] |
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|
Inp | 1314.30 | NIST | |
Inp | 1326.80 | NIST | |
Inp | 1328.00 | NIST | |
Inp | 1318.00 | NIST | |
Inp | 1318.00 | NIST | |
Inp | Outlier 228.10 | NIST | |
Tboil | 572.14 | K | Joback Calculated Property |
Tc | 830.91 | K | Joback Calculated Property |
Tfus | 412.03 | K | Joback Calculated Property |
Vc | 0.520 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [201.40; 222.01] | J/mol×K | [572.14; 830.91] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 200 205 210 215 220 600 700 800 | ||||
Cp,gas | 201.40 | J/mol×K | 572.14 | Joback Calculated Property |
Cp,gas | 205.15 | J/mol×K | 615.27 | Joback Calculated Property |
Cp,gas | 208.54 | J/mol×K | 658.40 | Joback Calculated Property |
Cp,gas | 211.76 | J/mol×K | 701.52 | Joback Calculated Property |
Cp,gas | 214.97 | J/mol×K | 744.65 | Joback Calculated Property |
Cp,gas | 218.33 | J/mol×K | 787.78 | Joback Calculated Property |
Cp,gas | 222.01 | J/mol×K | 830.91 | Joback Calculated Property |
ΔsubH | 73.60 | kJ/mol | 283.00 | NIST |
ΔvapH | 53.70 | kJ/mol | 423.50 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 512.20 | K | 100.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [2.31e-03; 2930.13] | kPa | [284.49; 746.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.04916e+02 | |||
Coefficient B | -1.11253e+04 | |||
Coefficient C | -1.27868e+01 | |||
Coefficient D | 4.60213e-06 | |||
Temperature range, min. | 284.49 | |||
Temperature range, max. | 746.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 400 600 | ||||
Pvap | 2.31e-03 | kPa | 284.49 | Calculated Property |
Pvap | 0.13 | kPa | 335.77 | Calculated Property |
Pvap | 1.96 | kPa | 387.05 | Calculated Property |
Pvap | 13.98 | kPa | 438.33 | Calculated Property |
Pvap | 60.34 | kPa | 489.61 | Calculated Property |
Pvap | 185.64 | kPa | 540.88 | Calculated Property |
Pvap | 452.22 | kPa | 592.16 | Calculated Property |
Pvap | 935.51 | kPa | 643.44 | Calculated Property |
Pvap | 1724.42 | kPa | 694.72 | Calculated Property |
Pvap | 2930.13 | kPa | 746.00 | Calculated Property |
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