Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 353.28 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -1034.05 | kJ/mol | Joback Calculated Property |
ΔfusH° | 120.08 | kJ/mol | Joback Calculated Property |
ΔvapH° | 243.00 ± 0.20 | kJ/mol | NIST |
log10WS | -19.91 | Crippen Calculated Property | |
logPoct/wat | 18.971 | Crippen Calculated Property | |
McVol | 687.180 | ml/mol | McGowan Calculated Property |
Pc | 294.62 | kPa | Joback Calculated Property |
Tboil | 1297.64 | K | Joback Calculated Property |
Tc | 2013.41 | K | Joback Calculated Property |
Tfus | 361.40 ± 3.00 | K | NIST |
Vc | 2.724 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [2748.26; 3230.01] | J/mol×K | [1297.64; 2013.41] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 2800 2900 3000 3100 3200 1400 1600 1800 2000 | ||||
Cp,gas | 2748.26 | J/mol×K | 1297.64 | Joback Calculated Property |
Cp,gas | 2824.27 | J/mol×K | 1416.94 | Joback Calculated Property |
Cp,gas | 2894.38 | J/mol×K | 1536.23 | Joback Calculated Property |
Cp,gas | 2964.30 | J/mol×K | 1655.53 | Joback Calculated Property |
Cp,gas | 3039.75 | J/mol×K | 1774.82 | Joback Calculated Property |
Cp,gas | 3126.41 | J/mol×K | 1894.12 | Joback Calculated Property |
Cp,gas | 3230.01 | J/mol×K | 2013.41 | Joback Calculated Property |
Cp,liquid | 1595.00 | J/mol×K | 353.00 | NIST |
η | [0.0000013; 0.0000663] | Pa×s | [630.72; 1297.64] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-5 2.00e-5 3.00e-5 4.00e-5 5.00e-5 6.00e-5 7.00e-5 800 1000 1200 | ||||
η | 0.0000663 | Pa×s | 630.72 | Joback Calculated Property |
η | 0.0000211 | Pa×s | 741.87 | Joback Calculated Property |
η | 0.0000090 | Pa×s | 853.03 | Joback Calculated Property |
η | 0.0000047 | Pa×s | 964.18 | Joback Calculated Property |
η | 0.0000028 | Pa×s | 1075.33 | Joback Calculated Property |
η | 0.0000018 | Pa×s | 1186.49 | Joback Calculated Property |
η | 0.0000013 | Pa×s | 1297.64 | Joback Calculated Property |
ΔvapH | [145.90; 243.00] | kJ/mol | [298.15; 719.00] | ![]() |
ΔvapH | 243.00 | kJ/mol | 298.15 | Hypothe... |
ΔvapH | 145.90 | kJ/mol | 719.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [665.69; 890.36] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43954e+01 | |||
Coefficient B | -5.73112e+03 | |||
Coefficient C | -2.59450e+02 | |||
Temperature range, min. | 665.69 | |||
Temperature range, max. | 890.36 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 700 750 800 850 | ||||
Pvap | 1.33 | kPa | 665.69 | Calculated Property |
Pvap | 3.02 | kPa | 690.65 | Calculated Property |
Pvap | 6.24 | kPa | 715.62 | Calculated Property |
Pvap | 11.98 | kPa | 740.58 | Calculated Property |
Pvap | 21.57 | kPa | 765.54 | Calculated Property |
Pvap | 36.73 | kPa | 790.51 | Calculated Property |
Pvap | 59.62 | kPa | 815.47 | Calculated Property |
Pvap | 92.84 | kPa | 840.43 | Calculated Property |
Pvap | 139.39 | kPa | 865.40 | Calculated Property |
Pvap | 202.65 | kPa | 890.36 | Calculated Property |
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