Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -322.44 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -585.47 | kJ/mol | Joback Calculated Property |
ΔfusH° | 20.45 | kJ/mol | Joback Calculated Property |
ΔvapH° | [59.50; 59.54] | kJ/mol |
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ΔvapH° | 59.54 ± 0.04 | kJ/mol | NIST |
ΔvapH° | 59.50 ± 0.10 | kJ/mol | NIST |
log10WS | -1.12 | Crippen Calculated Property | |
logPoct/wat | 1.366 | Crippen Calculated Property | |
McVol | 136.890 | ml/mol | McGowan Calculated Property |
Pc | 2694.00 ± 40.00 | kPa | NIST |
ρc | 291.58 ± 6.41 | kg/m3 | NIST |
Inp | [1053.00; 1120.20] |
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|
Inp | 1096.00 | NIST | |
Inp | 1120.20 | NIST | |
Inp | 1090.00 | NIST | |
Inp | 1090.00 | NIST | |
Inp | 1053.00 | NIST | |
Inp | 1061.00 | NIST | |
Inp | 1089.80 | NIST | |
Inp | 1087.00 | NIST | |
Inp | 1053.00 | NIST | |
Tboil | [465.20; 466.20] | K |
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Tboil | 465.20 | K | NIST |
Tboil | 466.20 ± 1.50 | K | NIST |
Tc | [640.20; 641.20] | K |
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Tc | 641.20 ± 1.60 | K | NIST |
Tc | 640.20 ± 0.80 | K | NIST |
Tfus | 209.70 ± 0.60 | K | NIST |
Vc | 0.525 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [303.83; 370.44] | J/mol×K | [481.15; 655.74] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 300 310 320 330 340 350 360 370 500 550 600 650 | ||||
Cp,gas | 303.83 | J/mol×K | 481.15 | Joback Calculated Property |
Cp,gas | 315.90 | J/mol×K | 510.25 | Joback Calculated Property |
Cp,gas | 327.58 | J/mol×K | 539.35 | Joback Calculated Property |
Cp,gas | 338.89 | J/mol×K | 568.45 | Joback Calculated Property |
Cp,gas | 349.80 | J/mol×K | 597.55 | Joback Calculated Property |
Cp,gas | 360.32 | J/mol×K | 626.64 | Joback Calculated Property |
Cp,gas | 370.44 | J/mol×K | 655.74 | Joback Calculated Property |
η | [0.0002138; 0.0024417] | Pa×s | [274.31; 481.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 300 350 400 450 | ||||
η | 0.0024417 | Pa×s | 274.31 | Joback Calculated Property |
η | 0.0012972 | Pa×s | 308.78 | Joback Calculated Property |
η | 0.0007825 | Pa×s | 343.26 | Joback Calculated Property |
η | 0.0005177 | Pa×s | 377.73 | Joback Calculated Property |
η | 0.0003669 | Pa×s | 412.20 | Joback Calculated Property |
η | 0.0002743 | Pa×s | 446.68 | Joback Calculated Property |
η | 0.0002138 | Pa×s | 481.15 | Joback Calculated Property |
ΔvapH | 51.90 | kJ/mol | 379.00 | NIST |
Pvap | [2.92; 98.36] | kPa | [363.15; 464.20] | ![]() |
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 400 450 | ||||
Pvap | 2.92 | kPa | 363.15 | Vapor P... |
Pvap | 4.57 | kPa | 373.15 | Vapor P... |
Pvap | 6.72 | kPa | 383.15 | Vapor P... |
Pvap | 9.96 | kPa | 393.15 | Vapor P... |
Pvap | 14.42 | kPa | 403.15 | Vapor P... |
Pvap | 20.44 | kPa | 413.15 | Vapor P... |
Pvap | 28.85 | kPa | 423.15 | Vapor P... |
Pvap | 33.94 | kPa | 428.15 | Vapor P... |
Pvap | 39.87 | kPa | 433.15 | Vapor P... |
Pvap | 46.80 | kPa | 438.15 | Vapor P... |
Pvap | 54.64 | kPa | 443.15 | Vapor P... |
Pvap | 63.48 | kPa | 448.15 | Vapor P... |
Pvap | 85.24 | kPa | 458.15 | Vapor P... |
Pvap | 93.70 | kPa | 463.00 | Estimat... |
Pvap | 98.36 | kPa | 463.15 | Vapor P... |
Pvap | 93.60 | kPa | 463.30 | Estimat... |
Pvap | 93.90 | kPa | 464.20 | Estimat... |
n0 | 1.41183 | 298.15 | Excess ... | |
ρl | [901.29; 960.40] | kg/m3 | [273.15; 333.15] | ![]() |
T(K) Liquid Density (kg/m3) 900 910 920 930 940 950 960 280 300 320 | ||||
ρl | 960.40 | kg/m3 | 273.15 | Below t... |
ρl | 950.40 | kg/m3 | 283.15 | Below t... |
ρl | 940.70 | kg/m3 | 293.15 | Solubil... |
ρl | 930.89 | kg/m3 | 303.15 | Solubil... |
ρl | 921.05 | kg/m3 | 313.15 | Solubil... |
ρl | 911.18 | kg/m3 | 323.15 | Solubil... |
ρl | 901.29 | kg/m3 | 333.15 | Solubil... |
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