Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -21149.00 ± 21.00 | kJ/mol | NIST |
ΔfG° | 1126.98 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 882.00 | kJ/mol | NIST |
ΔfH°solid | [620.00; 620.00] | kJ/mol |
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ΔfH°solid | 620.00 ± 22.00 | kJ/mol | NIST |
ΔfH°solid | 620.00 ± 21.00 | kJ/mol | NIST |
ΔfusH° | 63.46 | kJ/mol | Joback Calculated Property |
ΔsubH° | 262.00 | kJ/mol | NIST |
ΔvapH° | 129.36 | kJ/mol | Joback Calculated Property |
IE | 6.41 | eV | NIST |
log10WS | -17.30 | Crippen Calculated Property | |
logPoct/wat | 11.814 | Crippen Calculated Property | |
McVol | 425.460 | ml/mol | McGowan Calculated Property |
Pc | 1149.10 | kPa | Joback Calculated Property |
Tboil | 1380.58 | K | Joback Calculated Property |
Tc | 1695.98 | K | Joback Calculated Property |
Tfus | 868.42 | K | Joback Calculated Property |
Vc | 1.613 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [1493.96; 1755.33] | J/mol×K | [1380.58; 1695.98] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 1500 1550 1600 1650 1700 1750 1400 1500 1600 1700 | ||||
Cp,gas | 1493.96 | J/mol×K | 1380.58 | Joback Calculated Property |
Cp,gas | 1526.79 | J/mol×K | 1433.15 | Joback Calculated Property |
Cp,gas | 1563.09 | J/mol×K | 1485.71 | Joback Calculated Property |
Cp,gas | 1603.47 | J/mol×K | 1538.28 | Joback Calculated Property |
Cp,gas | 1648.56 | J/mol×K | 1590.85 | Joback Calculated Property |
Cp,gas | 1698.97 | J/mol×K | 1643.42 | Joback Calculated Property |
Cp,gas | 1755.33 | J/mol×K | 1695.98 | Joback Calculated Property |
η | [0.0000771; 0.0003065] | Pa×s | [868.42; 1380.58] | ![]() |
T(K) Dynamic viscosity (Pa×s) 1.00e-4 1.50e-4 2.00e-4 2.50e-4 3.00e-4 1000 1200 | ||||
η | 0.0003065 | Pa×s | 868.42 | Joback Calculated Property |
η | 0.0002197 | Pa×s | 953.78 | Joback Calculated Property |
η | 0.0001663 | Pa×s | 1039.14 | Joback Calculated Property |
η | 0.0001313 | Pa×s | 1124.50 | Joback Calculated Property |
η | 0.0001072 | Pa×s | 1209.86 | Joback Calculated Property |
η | 0.0000899 | Pa×s | 1295.22 | Joback Calculated Property |
η | 0.0000771 | Pa×s | 1380.58 | Joback Calculated Property |
ΔsubH | [160.60; 162.80] | kJ/mol | [453.00; 488.00] | ![]() |
ΔsubH | 162.80 ± 4.20 | kJ/mol | 453.00 | NIST |
ΔsubH | 160.60 ± 4.20 | kJ/mol | 488.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [660.66; 852.18] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 2.26410e+01 | |||
Coefficient B | -1.47679e+04 | |||
Temperature range, min. | 660.66 | |||
Temperature range, max. | 852.18 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 700 750 800 850 | ||||
Pvap | 1.33 | kPa | 660.66 | Calculated Property |
Pvap | 2.68 | kPa | 681.94 | Calculated Property |
Pvap | 5.16 | kPa | 703.22 | Calculated Property |
Pvap | 9.56 | kPa | 724.50 | Calculated Property |
Pvap | 17.10 | kPa | 745.78 | Calculated Property |
Pvap | 29.62 | kPa | 767.06 | Calculated Property |
Pvap | 49.80 | kPa | 788.34 | Calculated Property |
Pvap | 81.49 | kPa | 809.62 | Calculated Property |
Pvap | 130.01 | kPa | 830.90 | Calculated Property |
Pvap | 202.64 | kPa | 852.18 | Calculated Property |
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