Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -5742.30 ± 7.00 | kJ/mol | NIST |
ΔfG° | -248.74 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -508.90 ± 7.10 | kJ/mol | NIST |
ΔfH°liquid | -657.60 ± 7.00 | kJ/mol | NIST |
ΔfusH° | 27.24 | kJ/mol | Joback Calculated Property |
ΔvapH° | [111.40; 148.70] | kJ/mol |
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ΔvapH° | 111.40 ± 7.00 | kJ/mol | NIST |
ΔvapH° | 148.70 ± 1.10 | kJ/mol | NIST |
ΔvapH° | 148.70 | kJ/mol | NIST |
ΔvapH° | 112.80 ± 2.10 | kJ/mol | NIST |
log10WS | -2.12 | Crippen Calculated Property | |
logPoct/wat | 1.702 | Crippen Calculated Property | |
McVol | 149.410 | ml/mol | McGowan Calculated Property |
Pc | 2775.92 | kPa | Joback Calculated Property |
Inp | 1414.00 | NIST | |
Tboil | 589.68 | K | Joback Calculated Property |
Tc | 760.00 | K | Critica... |
Tfus | 318.70 | K | Thermod... |
Ttriple | 319.50 ± 0.10 | K | NIST |
Vc | 0.578 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [392.38; 451.76] | J/mol×K | [589.68; 746.58] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 390 400 410 420 430 440 450 600 650 700 750 | ||||
Cp,gas | 392.38 | J/mol×K | 589.68 | Joback Calculated Property |
Cp,gas | 403.30 | J/mol×K | 615.83 | Joback Calculated Property |
Cp,gas | 413.80 | J/mol×K | 641.98 | Joback Calculated Property |
Cp,gas | 423.89 | J/mol×K | 668.13 | Joback Calculated Property |
Cp,gas | 433.57 | J/mol×K | 694.28 | Joback Calculated Property |
Cp,gas | 442.85 | J/mol×K | 720.43 | Joback Calculated Property |
Cp,gas | 451.76 | J/mol×K | 746.58 | Joback Calculated Property |
Cp,liquid | [389.02; 436.95] | J/mol×K | [318.65; 353.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 390 400 410 420 430 440 320 330 340 350 | ||||
Cp,liquid | 389.02 | J/mol×K | 318.65 | Heat Ca... |
Cp,liquid | 391.15 | J/mol×K | 320.15 | Heat Ca... |
Cp,liquid | 393.27 | J/mol×K | 321.65 | Heat Ca... |
Cp,liquid | 395.39 | J/mol×K | 323.15 | Heat Ca... |
Cp,liquid | 397.51 | J/mol×K | 324.65 | Heat Ca... |
Cp,liquid | 399.62 | J/mol×K | 326.15 | Heat Ca... |
Cp,liquid | 401.73 | J/mol×K | 327.65 | Heat Ca... |
Cp,liquid | 403.84 | J/mol×K | 329.15 | Heat Ca... |
Cp,liquid | 405.94 | J/mol×K | 330.65 | Heat Ca... |
Cp,liquid | 408.03 | J/mol×K | 332.15 | Heat Ca... |
Cp,liquid | 410.12 | J/mol×K | 333.65 | Heat Ca... |
Cp,liquid | 412.21 | J/mol×K | 335.15 | Heat Ca... |
Cp,liquid | 414.30 | J/mol×K | 336.65 | Heat Ca... |
Cp,liquid | 416.38 | J/mol×K | 338.15 | Heat Ca... |
Cp,liquid | 418.45 | J/mol×K | 339.65 | Heat Ca... |
Cp,liquid | 420.52 | J/mol×K | 341.15 | Heat Ca... |
Cp,liquid | 422.59 | J/mol×K | 342.65 | Heat Ca... |
Cp,liquid | 424.66 | J/mol×K | 344.15 | Heat Ca... |
Cp,liquid | 426.72 | J/mol×K | 345.65 | Heat Ca... |
Cp,liquid | 428.77 | J/mol×K | 347.15 | Heat Ca... |
Cp,liquid | 430.82 | J/mol×K | 348.65 | Heat Ca... |
Cp,liquid | 432.87 | J/mol×K | 350.15 | Heat Ca... |
Cp,liquid | 434.92 | J/mol×K | 351.65 | Heat Ca... |
Cp,liquid | 436.95 | J/mol×K | 353.15 | Heat Ca... |
η | [0.0000359; 0.0356093] | Pa×s | [312.83; 589.68] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-3 0.01 0.02 0.02 0.03 0.03 0.04 400 500 | ||||
η | 0.0356093 | Pa×s | 312.83 | Joback Calculated Property |
η | 0.0053856 | Pa×s | 358.97 | Joback Calculated Property |
η | 0.0012525 | Pa×s | 405.11 | Joback Calculated Property |
η | 0.0003925 | Pa×s | 451.25 | Joback Calculated Property |
η | 0.0001526 | Pa×s | 497.40 | Joback Calculated Property |
η | 0.0000696 | Pa×s | 543.54 | Joback Calculated Property |
η | 0.0000359 | Pa×s | 589.68 | Joback Calculated Property |
ΔfusH | [36.40; 36.40] | kJ/mol | [319.60; 319.60] | ![]() |
ΔfusH | 36.40 | kJ/mol | 319.60 | NIST |
ΔfusH | 36.40 | kJ/mol | 319.60 | NIST |
ΔvapH | [104.40; 112.50] | kJ/mol | [298.15; 360.00] | ![]() |
ΔvapH | 112.50 | kJ/mol | 298.15 | Vaporiz... |
ΔvapH | 110.00 | kJ/mol | 323.00 | NIST |
ΔvapH | 104.40 | kJ/mol | 360.00 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [447.20; 450.20] | K | [2.00; 2.70] |
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Tboilr | 450.20 | K | 2.00 | NIST |
Tboilr | 447.20 | K | 2.70 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.68] | kPa | [433.52; 546.86] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 2.02589e+01 | |||
Coefficient B | -6.73440e+03 | |||
Coefficient C | -9.63160e+01 | |||
Temperature range, min. | 433.52 | |||
Temperature range, max. | 546.86 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 | ||||
Pvap | 1.33 | kPa | 433.52 | Calculated Property |
Pvap | 2.74 | kPa | 446.11 | Calculated Property |
Pvap | 5.34 | kPa | 458.71 | Calculated Property |
Pvap | 9.97 | kPa | 471.30 | Calculated Property |
Pvap | 17.87 | kPa | 483.89 | Calculated Property |
Pvap | 30.88 | kPa | 496.49 | Calculated Property |
Pvap | 51.60 | kPa | 509.08 | Calculated Property |
Pvap | 83.64 | kPa | 521.67 | Calculated Property |
Pvap | 131.87 | kPa | 534.27 | Calculated Property |
Pvap | 202.68 | kPa | 546.86 | Calculated Property |
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