Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 487.50 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 340.97 | kJ/mol | Joback Calculated Property |
ΔfusH° | 24.98 | kJ/mol | Joback Calculated Property |
ΔvapH° | 97.50 ± 3.90 | kJ/mol | NIST |
log10WS | -8.04 | Aq. Sol... | |
logPoct/wat | 4.411 | Crippen Calculated Property | |
McVol | 172.550 | ml/mol | McGowan Calculated Property |
Pc | 2844.44 | kPa | Joback Calculated Property |
Tboil | [674.20; 674.50] | K |
![]() |
Tboil | 674.20 | K | NIST |
Tboil | 674.50 ± 0.50 | K | NIST |
Tc | 937.21 | K | Joback Calculated Property |
Tfus | [481.50; 489.70] | K |
![]() |
Tfus | 481.50 ± 0.50 | K | NIST |
Tfus | 489.70 ± 0.40 | K | NIST |
Tfus | 483.45 ± 1.00 | K | NIST |
Vc | 0.667 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [438.86; 513.42] | J/mol×K | [678.51; 937.21] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 440 460 480 500 520 700 800 900 | ||||
Cp,gas | 438.86 | J/mol×K | 678.51 | Joback Calculated Property |
Cp,gas | 453.60 | J/mol×K | 721.63 | Joback Calculated Property |
Cp,gas | 467.14 | J/mol×K | 764.74 | Joback Calculated Property |
Cp,gas | 479.68 | J/mol×K | 807.86 | Joback Calculated Property |
Cp,gas | 491.43 | J/mol×K | 850.98 | Joback Calculated Property |
Cp,gas | 502.61 | J/mol×K | 894.10 | Joback Calculated Property |
Cp,gas | 513.42 | J/mol×K | 937.21 | Joback Calculated Property |
η | [0.0009629; 0.0019238] | Pa×s | [433.67; 678.51] | ![]() |
T(K) Dynamic viscosity (Pa×s) 1.00e-3 1.20e-3 1.40e-3 1.60e-3 1.80e-3 2.00e-3 500 600 | ||||
η | 0.0019238 | Pa×s | 433.67 | Joback Calculated Property |
η | 0.0016313 | Pa×s | 474.48 | Joback Calculated Property |
η | 0.0014198 | Pa×s | 515.28 | Joback Calculated Property |
η | 0.0012612 | Pa×s | 556.09 | Joback Calculated Property |
η | 0.0011386 | Pa×s | 596.90 | Joback Calculated Property |
η | 0.0010415 | Pa×s | 637.70 | Joback Calculated Property |
η | 0.0009629 | Pa×s | 678.51 | Joback Calculated Property |
ΔfusH | [23.40; 23.40] | kJ/mol | [489.70; 489.70] | ![]() |
ΔfusH | 23.40 | kJ/mol | 489.70 | NIST |
ΔfusH | 23.40 | kJ/mol | 489.70 | NIST |
ΔfusH | 23.40 | kJ/mol | 489.70 | NIST |
ΔsubH | [111.20; 119.30] | kJ/mol | [371.00; 383.00] | ![]() |
ΔsubH | 119.30 ± 1.30 | kJ/mol | 371.00 | NIST |
ΔsubH | 111.20 | kJ/mol | 383.00 | NIST |
ΔvapH | 84.70 | kJ/mol | 398.00 | NIST |
Pvap | [1.03e-06; 2.00] | kPa | [298.15; 510.00] | ![]() |
T(K) Vapor pressure (kPa) 0 0.5 1 1.5 2 300 400 500 | ||||
Pvap | 1.03e-06 | kPa | 298.15 | Hypothe... |
Pvap | 1.31e-06 | kPa | 300.00 | Hypothe... |
Pvap | 4.60e-06 | kPa | 310.00 | Hypothe... |
Pvap | 1.47e-05 | kPa | 320.00 | Hypothe... |
Pvap | 4.30e-05 | kPa | 330.00 | Hypothe... |
Pvap | 1.16e-04 | kPa | 340.00 | Hypothe... |
Pvap | 2.94e-04 | kPa | 350.00 | Hypothe... |
Pvap | 6.97e-04 | kPa | 360.00 | Hypothe... |
Pvap | 1.56e-03 | kPa | 370.00 | Hypothe... |
Pvap | 3.29e-03 | kPa | 380.00 | Hypothe... |
Pvap | 6.63e-03 | kPa | 390.00 | Hypothe... |
Pvap | 0.01 | kPa | 400.00 | Hypothe... |
Pvap | 0.02 | kPa | 410.00 | Hypothe... |
Pvap | 0.04 | kPa | 420.00 | Hypothe... |
Pvap | 0.07 | kPa | 430.00 | Hypothe... |
Pvap | 0.12 | kPa | 440.00 | Hypothe... |
Pvap | 0.19 | kPa | 450.00 | Hypothe... |
Pvap | 0.30 | kPa | 460.00 | Hypothe... |
Pvap | 0.46 | kPa | 470.00 | Hypothe... |
Pvap | 0.69 | kPa | 480.00 | Hypothe... |
Pvap | 1.00 | kPa | 490.00 | Hypothe... |
Pvap | 1.43 | kPa | 500.00 | Hypothe... |
Pvap | 2.00 | kPa | 510.00 | Hypothe... |
ΔfusS | 47.80 | J/mol×K | 489.70 | NIST |
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