Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -5108.20 ± 6.70 | kJ/mol | NIST |
ΔfG° | -101.67 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -78.70 ± 6.70 | kJ/mol | NIST |
ΔfH°liquid | -149.00 ± 6.70 | kJ/mol | NIST |
ΔfH°solid | -192.00 | kJ/mol | NIST |
ΔfusH° | 10.97 | kJ/mol | Joback Calculated Property |
ΔvapH° | [69.90; 70.30] | kJ/mol |
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ΔvapH° | 69.90 | kJ/mol | NIST |
ΔvapH° | 69.90 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 70.30 | kJ/mol | NIST |
log10WS | -2.26 | Crippen Calculated Property | |
logPoct/wat | 2.411 | Crippen Calculated Property | |
McVol | 125.650 | ml/mol | McGowan Calculated Property |
Pc | 3642.13 | kPa | Joback Calculated Property |
Tboil | 543.37 | K | Joback Calculated Property |
Tc | 748.48 | K | Joback Calculated Property |
Tfus | 303.08 | K | Joback Calculated Property |
Vc | 0.458 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [293.53; 355.85] | J/mol×K | [543.37; 748.48] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 290 300 310 320 330 340 350 360 600 700 | ||||
Cp,gas | 293.53 | J/mol×K | 543.37 | Joback Calculated Property |
Cp,gas | 305.74 | J/mol×K | 577.56 | Joback Calculated Property |
Cp,gas | 317.17 | J/mol×K | 611.74 | Joback Calculated Property |
Cp,gas | 327.86 | J/mol×K | 645.93 | Joback Calculated Property |
Cp,gas | 337.84 | J/mol×K | 680.11 | Joback Calculated Property |
Cp,gas | 347.17 | J/mol×K | 714.30 | Joback Calculated Property |
Cp,gas | 355.85 | J/mol×K | 748.48 | Joback Calculated Property |
η | [0.0000892; 0.0105883] | Pa×s | [303.08; 543.37] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 300 400 500 | ||||
η | 0.0105883 | Pa×s | 303.08 | Joback Calculated Property |
η | 0.0030015 | Pa×s | 343.13 | Joback Calculated Property |
η | 0.0011074 | Pa×s | 383.18 | Joback Calculated Property |
η | 0.0004934 | Pa×s | 423.23 | Joback Calculated Property |
η | 0.0002528 | Pa×s | 463.27 | Joback Calculated Property |
η | 0.0001441 | Pa×s | 503.32 | Joback Calculated Property |
η | 0.0000892 | Pa×s | 543.37 | Joback Calculated Property |
ΔvapH | 74.00 | kJ/mol | 368.50 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 373.70 | K | 1.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [356.29; 528.17] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.07891e+01 | |||
Coefficient B | -1.96802e+03 | |||
Coefficient C | -1.68886e+02 | |||
Temperature range, min. | 356.29 | |||
Temperature range, max. | 528.17 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 356.29 | Calculated Property |
Pvap | 3.52 | kPa | 375.39 | Calculated Property |
Pvap | 7.89 | kPa | 394.49 | Calculated Property |
Pvap | 15.59 | kPa | 413.58 | Calculated Property |
Pvap | 27.90 | kPa | 432.68 | Calculated Property |
Pvap | 46.17 | kPa | 451.78 | Calculated Property |
Pvap | 71.68 | kPa | 470.88 | Calculated Property |
Pvap | 105.62 | kPa | 489.97 | Calculated Property |
Pvap | 149.00 | kPa | 509.07 | Calculated Property |
Pvap | 202.64 | kPa | 528.17 | Calculated Property |
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