Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -3444.50 ± 0.79 | kJ/mol | NIST |
ΔfG° | 94.22 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -54.86 ± 0.92 | kJ/mol | NIST |
ΔfH°liquid | -95.14 ± 0.84 | kJ/mol | NIST |
ΔfusH° | 7.84 | kJ/mol | Joback Calculated Property |
ΔvapH° | [40.20; 40.30] | kJ/mol | |
ΔvapH° | 40.20 ± 0.42 | kJ/mol | NIST |
ΔvapH° | 40.30 | kJ/mol | NIST |
ΔvapH° | 40.20 ± 0.40 | kJ/mol | NIST |
log10WS | -1.36 | Crippen Calculated Property | |
logPoct/wat | 0.888 | Crippen Calculated Property | |
McVol | 80.430 | ml/mol | McGowan Calculated Property |
Pc | 4684.89 | kPa | Joback Calculated Property |
S°liquid | 241.04 | J/mol×K | NIST |
Tboil | [381.00; 381.62] | K | |
Tboil | 381.20 | K | NIST |
Tboil | 381.62 ± 0.20 | K | NIST |
Tboil | 381.00 ± 6.00 | K | NIST |
Tc | 615.99 | K | Joback Calculated Property |
Tfus | [187.45; 187.45] | K | |
Tfus | 187.45 ± 0.30 | K | NIST |
Tfus | 187.45 ± 0.50 | K | NIST |
Ttriple | 190.45 ± 0.02 | K | NIST |
Vc | 0.285 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [153.21; 222.65] | J/mol×K | [401.61; 615.99] | |
T(K) Ideal gas heat capacity (J/mol×K) 150 160 170 180 190 200 210 220 400 500 600 | ||||
Cp,gas | 153.21 | J/mol×K | 401.61 | Joback Calculated Property |
Cp,gas | 166.54 | J/mol×K | 437.34 | Joback Calculated Property |
Cp,gas | 179.13 | J/mol×K | 473.07 | Joback Calculated Property |
Cp,gas | 191.01 | J/mol×K | 508.80 | Joback Calculated Property |
Cp,gas | 202.21 | J/mol×K | 544.53 | Joback Calculated Property |
Cp,gas | 212.74 | J/mol×K | 580.26 | Joback Calculated Property |
Cp,gas | 222.65 | J/mol×K | 615.99 | Joback Calculated Property |
Cp,liquid | 181.21 | J/mol×K | 298.00 | NIST |
ΔfusH | [0.48; 8.31] | kJ/mol | [184.50; 190.40] | |
ΔfusH | 0.48 | kJ/mol | 184.50 | NIST |
ΔfusH | 8.31 | kJ/mol | 190.40 | NIST |
ΔfusH | 8.31 | kJ/mol | 190.40 | NIST |
ΔvapH | 38.30 | kJ/mol | 368.00 | NIST |
ΔfusS | [2.58; 43.65] | J/mol×K | [184.50; 190.40] | |
ΔfusS | 2.58 | J/mol×K | 184.50 | NIST |
ΔfusS | 43.65 | J/mol×K | 190.40 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [283.09; 405.36] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.46343e+01 | |||
Coefficient B | -3.25532e+03 | |||
Coefficient C | -5.61860e+01 | |||
Temperature range, min. | 283.09 | |||
Temperature range, max. | 405.36 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 283.09 | Calculated Property |
Pvap | 3.00 | kPa | 296.68 | Calculated Property |
Pvap | 6.18 | kPa | 310.26 | Calculated Property |
Pvap | 11.85 | kPa | 323.85 | Calculated Property |
Pvap | 21.32 | kPa | 337.43 | Calculated Property |
Pvap | 36.34 | kPa | 351.02 | Calculated Property |
Pvap | 59.11 | kPa | 364.60 | Calculated Property |
Pvap | 92.27 | kPa | 378.19 | Calculated Property |
Pvap | 138.93 | kPa | 391.77 | Calculated Property |
Pvap | 202.63 | kPa | 405.36 | Calculated Property |
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