Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -104.84 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-133.00; -125.00] | kJ/mol | |
ΔfH°gas | -125.00 ± 3.60 | kJ/mol | NIST |
ΔfH°gas | -127.00 ± 2.00 | kJ/mol | NIST |
ΔfH°gas | -133.00 | kJ/mol | NIST |
ΔfH°liquid | [-166.30; -162.30] | kJ/mol | |
ΔfH°liquid | -162.30 ± 0.88 | kJ/mol | NIST |
ΔfH°liquid | -166.30 ± 0.20 | kJ/mol | NIST |
ΔfH°liquid | -166.30 ± 0.30 | kJ/mol | NIST |
ΔfusH° | 6.94 | kJ/mol | Joback Calculated Property |
ΔvapH° | [33.00; 38.50] | kJ/mol | |
ΔvapH° | 38.50 ± 3.30 | kJ/mol | NIST |
ΔvapH° | 33.00 | kJ/mol | NIST |
log10WS | -1.38 | Crippen Calculated Property | |
logPoct/wat | 0.968 | Crippen Calculated Property | |
McVol | 66.430 | ml/mol | McGowan Calculated Property |
Pc | 5335.72 | kPa | Joback Calculated Property |
Tboil | [378.00; 381.20] | K | |
Tboil | 381.20 | K | NIST |
Tboil | 381.00 | K | NIST |
Tboil | 381.00 | K | NIST |
Tboil | 378.00 ± 3.00 | K | NIST |
Tc | 615.29 | K | Joback Calculated Property |
Tfus | 220.29 | K | Joback Calculated Property |
Vc | 0.241 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [80.35; 100.35] | J/mol×K | [392.17; 615.29] | |
T(K) Ideal gas heat capacity (J/mol×K) 80 85 90 95 100 400 500 600 | ||||
Cp,gas | 80.35 | J/mol×K | 392.17 | Joback Calculated Property |
Cp,gas | 84.27 | J/mol×K | 429.36 | Joback Calculated Property |
Cp,gas | 87.94 | J/mol×K | 466.54 | Joback Calculated Property |
Cp,gas | 91.37 | J/mol×K | 503.73 | Joback Calculated Property |
Cp,gas | 94.57 | J/mol×K | 540.92 | Joback Calculated Property |
Cp,gas | 97.56 | J/mol×K | 578.11 | Joback Calculated Property |
Cp,gas | 100.35 | J/mol×K | 615.29 | Joback Calculated Property |
η | [0.0005242; 0.0046802] | Pa×s | [220.29; 392.17] | |
T(K) Dynamic viscosity (Pa×s) 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 250 300 350 | ||||
η | 0.0046802 | Pa×s | 220.29 | Joback Calculated Property |
η | 0.0026341 | Pa×s | 248.94 | Joback Calculated Property |
η | 0.0016692 | Pa×s | 277.58 | Joback Calculated Property |
η | 0.0011520 | Pa×s | 306.23 | Joback Calculated Property |
η | 0.0008472 | Pa×s | 334.88 | Joback Calculated Property |
η | 0.0006539 | Pa×s | 363.52 | Joback Calculated Property |
η | 0.0005242 | Pa×s | 392.17 | Joback Calculated Property |
ΔvapH | 37.10 | kJ/mol | 289.00 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [309.00; 309.20] | K | [6.70; 6.70] | |
Tboilr | 309.20 | K | 6.70 | NIST |
Tboilr | 309.00 | K | 6.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.00; 202.66] | kPa | [272.55; 402.81] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 2.14626e+01 | |||
Coefficient B | -8.50106e+03 | |||
Coefficient C | 1.23536e+02 | |||
Temperature range, min. | 272.55 | |||
Temperature range, max. | 402.81 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.00 | kPa | 272.55 | Calculated Property |
Pvap | 2.13 | kPa | 287.02 | Calculated Property |
Pvap | 4.31 | kPa | 301.50 | Calculated Property |
Pvap | 8.33 | kPa | 315.97 | Calculated Property |
Pvap | 15.44 | kPa | 330.44 | Calculated Property |
Pvap | 27.54 | kPa | 344.92 | Calculated Property |
Pvap | 47.44 | kPa | 359.39 | Calculated Property |
Pvap | 79.17 | kPa | 373.86 | Calculated Property |
Pvap | 128.36 | kPa | 388.34 | Calculated Property |
Pvap | 202.66 | kPa | 402.81 | Calculated Property |
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