Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -6736.20 ± 2.80 | kJ/mol | NIST |
ΔfG° | -481.32 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -820.63 | kJ/mol | Joback Calculated Property |
ΔfusH° | 0.06 | kJ/mol | Vaporiz... |
ΔsubH° | 153.00 ± 3.00 | kJ/mol | NIST |
ΔvapH° | 130.00 ± 2.30 | kJ/mol | NIST |
log10WS | -3.04 | Crippen Calculated Property | |
logPoct/wat | 3.057 | Crippen Calculated Property | |
McVol | 194.820 | ml/mol | McGowan Calculated Property |
Pc | 2150.00 | kPa | Critica... |
Tboil | 766.06 | K | Joback Calculated Property |
Tc | 943.42 | K | Joback Calculated Property |
Tfus | 402.50 ± 0.50 | K | NIST |
Vc | 0.757 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [579.68; 638.80] | J/mol×K | [766.06; 943.42] | ![]() |
Cp,gas | 579.68 | J/mol×K | 766.06 | Joback Calculated Property |
Cp,gas | 590.93 | J/mol×K | 795.62 | Joback Calculated Property |
Cp,gas | 601.59 | J/mol×K | 825.18 | Joback Calculated Property |
Cp,gas | 611.69 | J/mol×K | 854.74 | Joback Calculated Property |
Cp,gas | 621.24 | J/mol×K | 884.30 | Joback Calculated Property |
Cp,gas | 630.27 | J/mol×K | 913.86 | Joback Calculated Property |
Cp,gas | 638.80 | J/mol×K | 943.42 | Joback Calculated Property |
η | [0.0000096; 0.0014511] | Pa×s | [446.50; 766.06] | ![]() |
η | 0.0014511 | Pa×s | 446.50 | Joback Calculated Property |
η | 0.0004026 | Pa×s | 499.76 | Joback Calculated Property |
η | 0.0001430 | Pa×s | 553.02 | Joback Calculated Property |
η | 0.0000609 | Pa×s | 606.28 | Joback Calculated Property |
η | 0.0000298 | Pa×s | 659.54 | Joback Calculated Property |
η | 0.0000162 | Pa×s | 712.80 | Joback Calculated Property |
η | 0.0000096 | Pa×s | 766.06 | Joback Calculated Property |
ΔfusH | [49.80; 52.50] | kJ/mol | [400.30; 402.50] | ![]() |
ΔfusH | 49.80 | kJ/mol | 400.30 | NIST |
ΔfusH | 52.50 | kJ/mol | 401.60 | NIST |
ΔfusH | 50.56 | kJ/mol | 402.50 | NIST |
ΔfusH | 50.57 | kJ/mol | 402.50 | NIST |
ΔsubH | [153.10; 169.00] | kJ/mol | [307.00; 361.50] | ![]() |
ΔsubH | 156.00 | kJ/mol | 307.00 | NIST |
ΔsubH | 153.10 ± 2.90 | kJ/mol | 335.50 | NIST |
ΔsubH | 169.00 ± 4.00 | kJ/mol | 361.50 | NIST |
ΔfusS | 125.60 | J/mol×K | 402.50 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 518.20 | K | 1.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [520.47; 712.78] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.56665e+01 | |||
Coefficient B | -6.09579e+03 | |||
Coefficient C | -1.24099e+02 | |||
Temperature range, min. | 520.47 | |||
Temperature range, max. | 712.78 | |||
Pvap | 1.33 | kPa | 520.47 | Calculated Property |
Pvap | 2.93 | kPa | 541.84 | Calculated Property |
Pvap | 5.96 | kPa | 563.21 | Calculated Property |
Pvap | 11.34 | kPa | 584.57 | Calculated Property |
Pvap | 20.40 | kPa | 605.94 | Calculated Property |
Pvap | 34.91 | kPa | 627.31 | Calculated Property |
Pvap | 57.18 | kPa | 648.68 | Calculated Property |
Pvap | 90.10 | kPa | 670.04 | Calculated Property |
Pvap | 137.21 | kPa | 691.41 | Calculated Property |
Pvap | 202.66 | kPa | 712.78 | Calculated Property |
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