Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -4467.00 ± 9.30 | kJ/mol | NIST |
ΔfG° | -265.58 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -477.60 ± 9.30 | kJ/mol | NIST |
ΔfH°liquid | -574.20 ± 9.30 | kJ/mol | NIST |
ΔfusH° | 22.06 | kJ/mol | Joback Calculated Property |
ΔvapH° | [96.20; 96.60] | kJ/mol | |
ΔvapH° | 96.50 ± 3.20 | kJ/mol | NIST |
ΔvapH° | 96.60 ± 0.60 | kJ/mol | NIST |
ΔvapH° | 96.60 | kJ/mol | NIST |
ΔvapH° | 96.20 ± 1.20 | kJ/mol | NIST |
log10WS | -1.28 | Crippen Calculated Property | |
logPoct/wat | 0.922 | Crippen Calculated Property | |
McVol | 121.230 | ml/mol | McGowan Calculated Property |
Pc | 3435.91 | kPa | Joback Calculated Property |
Inp | [1201.00; 1201.00] | ||
Inp | 1201.00 | NIST | |
Inp | 1201.00 | NIST | |
Tboil | [532.20; 535.20] | K | |
Tboil | 532.20 | K | NIST |
Tboil | 535.20 | K | NIST |
Tc | 700.93 | K | Joback Calculated Property |
Tfus | [290.50; 337.15] | K | |
Tfus | 290.50 | K | Thermod... |
Tfus | 337.15 ± 2.00 | K | NIST |
Tfus | 293.15 ± 4.00 | K | NIST |
Ttriple | 295.00 ± 0.20 | K | NIST |
Vc | 0.466 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [299.02; 349.86] | J/mol×K | [543.92; 700.93] | |
T(K) Ideal gas heat capacity (J/mol×K) 300 310 320 330 340 350 550 600 650 700 | ||||
Cp,gas | 299.02 | J/mol×K | 543.92 | Joback Calculated Property |
Cp,gas | 308.35 | J/mol×K | 570.09 | Joback Calculated Property |
Cp,gas | 317.33 | J/mol×K | 596.26 | Joback Calculated Property |
Cp,gas | 325.96 | J/mol×K | 622.42 | Joback Calculated Property |
Cp,gas | 334.25 | J/mol×K | 648.59 | Joback Calculated Property |
Cp,gas | 342.22 | J/mol×K | 674.76 | Joback Calculated Property |
Cp,gas | 349.86 | J/mol×K | 700.93 | Joback Calculated Property |
Cp,liquid | [292.06; 354.42] | J/mol×K | [293.15; 353.15] | |
T(K) Liquid phase heat capacity (J/mol×K) 290 300 310 320 330 340 350 360 300 320 340 | ||||
Cp,liquid | 292.06 | J/mol×K | 293.15 | Heat Ca... |
Cp,liquid | 293.40 | J/mol×K | 294.65 | Heat Ca... |
Cp,liquid | 294.75 | J/mol×K | 296.15 | Heat Ca... |
Cp,liquid | 296.11 | J/mol×K | 297.65 | Heat Ca... |
Cp,liquid | 297.48 | J/mol×K | 299.15 | Heat Ca... |
Cp,liquid | 298.87 | J/mol×K | 300.65 | Heat Ca... |
Cp,liquid | 300.26 | J/mol×K | 302.15 | Heat Ca... |
Cp,liquid | 301.67 | J/mol×K | 303.65 | Heat Ca... |
Cp,liquid | 303.09 | J/mol×K | 305.15 | Heat Ca... |
Cp,liquid | 304.51 | J/mol×K | 306.65 | Heat Ca... |
Cp,liquid | 305.95 | J/mol×K | 308.15 | Heat Ca... |
Cp,liquid | 307.41 | J/mol×K | 309.65 | Heat Ca... |
Cp,liquid | 308.87 | J/mol×K | 311.15 | Heat Ca... |
Cp,liquid | 310.34 | J/mol×K | 312.65 | Heat Ca... |
Cp,liquid | 311.83 | J/mol×K | 314.15 | Heat Ca... |
Cp,liquid | 313.33 | J/mol×K | 315.65 | Heat Ca... |
Cp,liquid | 314.83 | J/mol×K | 317.15 | Heat Ca... |
Cp,liquid | 316.35 | J/mol×K | 318.65 | Heat Ca... |
Cp,liquid | 317.88 | J/mol×K | 320.15 | Heat Ca... |
Cp,liquid | 319.43 | J/mol×K | 321.65 | Heat Ca... |
Cp,liquid | 320.98 | J/mol×K | 323.15 | Heat Ca... |
Cp,liquid | 322.54 | J/mol×K | 324.65 | Heat Ca... |
Cp,liquid | 324.12 | J/mol×K | 326.15 | Heat Ca... |
Cp,liquid | 325.71 | J/mol×K | 327.65 | Heat Ca... |
Cp,liquid | 327.31 | J/mol×K | 329.15 | Heat Ca... |
Cp,liquid | 328.00 | J/mol×K | 330.65 | Heat Ca... |
Cp,liquid | 330.54 | J/mol×K | 332.15 | Heat Ca... |
Cp,liquid | 332.17 | J/mol×K | 333.65 | Heat Ca... |
Cp,liquid | 333.81 | J/mol×K | 335.15 | Heat Ca... |
Cp,liquid | 335.47 | J/mol×K | 336.65 | Heat Ca... |
Cp,liquid | 337.13 | J/mol×K | 338.15 | Heat Ca... |
Cp,liquid | 338.81 | J/mol×K | 339.65 | Heat Ca... |
Cp,liquid | 340.50 | J/mol×K | 341.15 | Heat Ca... |
Cp,liquid | 342.20 | J/mol×K | 342.65 | Heat Ca... |
Cp,liquid | 343.91 | J/mol×K | 344.15 | Heat Ca... |
Cp,liquid | 345.63 | J/mol×K | 345.65 | Heat Ca... |
Cp,liquid | 347.37 | J/mol×K | 347.15 | Heat Ca... |
Cp,liquid | 349.11 | J/mol×K | 348.65 | Heat Ca... |
Cp,liquid | 350.87 | J/mol×K | 350.15 | Heat Ca... |
Cp,liquid | 352.64 | J/mol×K | 351.65 | Heat Ca... |
Cp,liquid | 354.42 | J/mol×K | 353.15 | Heat Ca... |
η | [0.0000601; 0.0715544] | Pa×s | [290.29; 543.92] | |
T(K) Dynamic viscosity (Pa×s) 0 0.01 0.02 0.03 0.04 0.05 0.06 0.07 300 400 500 | ||||
η | 0.0715544 | Pa×s | 290.29 | Joback Calculated Property |
η | 0.0103813 | Pa×s | 332.56 | Joback Calculated Property |
η | 0.0023279 | Pa×s | 374.83 | Joback Calculated Property |
η | 0.0007068 | Pa×s | 417.11 | Joback Calculated Property |
η | 0.0002672 | Pa×s | 459.38 | Joback Calculated Property |
η | 0.0001190 | Pa×s | 501.65 | Joback Calculated Property |
η | 0.0000601 | Pa×s | 543.92 | Joback Calculated Property |
ΔfusH | [21.30; 21.30] | kJ/mol | [295.20; 295.20] | |
ΔfusH | 21.30 | kJ/mol | 295.20 | NIST |
ΔfusH | 21.30 | kJ/mol | 295.20 | NIST |
ΔvapH | [92.40; 97.90] | kJ/mol | [298.15; 341.00] | |
ΔvapH | 97.90 | kJ/mol | 298.15 | Vaporiz... |
ΔvapH | 93.80 | kJ/mol | 323.00 | NIST |
ΔvapH | 92.40 | kJ/mol | 341.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [415.12; 559.24] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.66473e+01 | |||
Coefficient B | -5.32013e+03 | |||
Coefficient C | -8.99220e+01 | |||
Temperature range, min. | 415.12 | |||
Temperature range, max. | 559.24 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
Pvap | 1.33 | kPa | 415.12 | Calculated Property |
Pvap | 2.87 | kPa | 431.13 | Calculated Property |
Pvap | 5.78 | kPa | 447.15 | Calculated Property |
Pvap | 10.95 | kPa | 463.16 | Calculated Property |
Pvap | 19.68 | kPa | 479.17 | Calculated Property |
Pvap | 33.77 | kPa | 495.19 | Calculated Property |
Pvap | 55.63 | kPa | 511.20 | Calculated Property |
Pvap | 88.34 | kPa | 527.21 | Calculated Property |
Pvap | 135.77 | kPa | 543.23 | Calculated Property |
Pvap | 202.63 | kPa | 559.24 | Calculated Property |
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