Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -13895.00 ± 1.00 | kJ/mol | NIST |
ΔfG° | -99.56 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -742.21 | kJ/mol | Joback Calculated Property |
ΔfusH° | 55.52 | kJ/mol | Joback Calculated Property |
ΔvapH° | 73.72 | kJ/mol | Joback Calculated Property |
log10WS | -7.89 | Crippen Calculated Property | |
logPoct/wat | 7.591 | Crippen Calculated Property | |
McVol | 328.280 | ml/mol | McGowan Calculated Property |
Pc | 927.24 | kPa | Joback Calculated Property |
Inp | [2373.00; 2400.00] |
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|
Inp | 2378.00 | NIST | |
Inp | 2383.00 | NIST | |
Inp | 2379.00 | NIST | |
Inp | 2394.20 | NIST | |
Inp | 2400.00 | NIST | |
Inp | 2373.00 | NIST | |
Inp | 2379.00 | NIST | |
Inp | 2394.20 | NIST | |
I | [2649.00; 2670.00] |
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I | 2649.00 | NIST | |
I | 2649.00 | NIST | |
I | 2662.00 | NIST | |
I | 2660.00 | NIST | |
I | 2664.00 | NIST | |
I | 2657.00 | NIST | |
I | 2670.00 | NIST | |
I | 2649.00 | NIST | |
Tboil | 779.05 | K | Joback Calculated Property |
Tc | 955.69 | K | Joback Calculated Property |
Tfus | 314.52 ± 1.00 | K | NIST |
Vc | 1.292 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [1031.01; 1139.78] | J/mol×K | [779.05; 955.69] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 1040 1060 1080 1100 1120 1140 800 850 900 950 | ||||
Cp,gas | 1031.01 | J/mol×K | 779.05 | Joback Calculated Property |
Cp,gas | 1051.60 | J/mol×K | 808.49 | Joback Calculated Property |
Cp,gas | 1071.17 | J/mol×K | 837.93 | Joback Calculated Property |
Cp,gas | 1089.74 | J/mol×K | 867.37 | Joback Calculated Property |
Cp,gas | 1107.35 | J/mol×K | 896.81 | Joback Calculated Property |
Cp,gas | 1124.02 | J/mol×K | 926.25 | Joback Calculated Property |
Cp,gas | 1139.78 | J/mol×K | 955.69 | Joback Calculated Property |
η | [0.0020395; 0.0056573] | Pa×s | [318.15; 373.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 320 340 360 | ||||
η | 0.0056573 | Pa×s | 318.15 | Densiti... |
η | 0.0049733 | Pa×s | 323.15 | Densiti... |
η | 0.0045070 | Pa×s | 328.15 | Densiti... |
η | 0.0040577 | Pa×s | 333.15 | Densiti... |
η | 0.0036714 | Pa×s | 338.15 | Densiti... |
η | 0.0033373 | Pa×s | 343.15 | Densiti... |
η | 0.0030462 | Pa×s | 348.15 | Densiti... |
η | 0.0027799 | Pa×s | 353.15 | Densiti... |
η | 0.0025690 | Pa×s | 358.15 | Densiti... |
η | 0.0023716 | Pa×s | 363.15 | Densiti... |
η | 0.0021961 | Pa×s | 368.15 | Densiti... |
η | 0.0020395 | Pa×s | 373.15 | Densiti... |
ΔfusH | 68.62 | kJ/mol | 315.00 | NIST |
ΔsubH | 171.50 | kJ/mol | 310.00 | NIST |
ΔvapH | 113.70 | kJ/mol | 389.00 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [459.70; 569.20] | K | [0.30; 13.30] |
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Tboilr | 459.70 | K | 0.30 | NIST |
Tboilr | 569.20 | K | 13.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [550.12; 670.06] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 2.24916e+01 | |||
Coefficient B | -9.10717e+03 | |||
Coefficient C | -1.39962e+02 | |||
Temperature range, min. | 550.12 | |||
Temperature range, max. | 670.06 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 550 600 650 | ||||
Pvap | 1.33 | kPa | 550.12 | Calculated Property |
Pvap | 2.68 | kPa | 563.45 | Calculated Property |
Pvap | 5.17 | kPa | 576.77 | Calculated Property |
Pvap | 9.58 | kPa | 590.10 | Calculated Property |
Pvap | 17.14 | kPa | 603.43 | Calculated Property |
Pvap | 29.69 | kPa | 616.75 | Calculated Property |
Pvap | 49.90 | kPa | 630.08 | Calculated Property |
Pvap | 81.61 | kPa | 643.41 | Calculated Property |
Pvap | 130.12 | kPa | 656.73 | Calculated Property |
Pvap | 202.65 | kPa | 670.06 | Calculated Property |
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