Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -5006.20 ± 2.20 | kJ/mol | NIST |
ΔfG° | 3.33 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -153.54 | kJ/mol | Joback Calculated Property |
ΔfH°solid | -250.40 ± 2.30 | kJ/mol | NIST |
ΔfusH° | 9.78 | kJ/mol | Joback Calculated Property |
ΔsubH° | 82.30 ± 0.70 | kJ/mol | NIST |
ΔvapH° | 65.00 ± 0.50 | kJ/mol | NIST |
log10WS | -2.13 | Crippen Calculated Property | |
logPoct/wat | 1.914 | Crippen Calculated Property | |
McVol | 119.780 | ml/mol | McGowan Calculated Property |
Pc | 3718.02 | kPa | Joback Calculated Property |
Inp | [1057.00; 1102.00] |
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|
Inp | 1076.00 | NIST | |
Inp | 1080.00 | NIST | |
Inp | 1089.60 | NIST | |
Inp | 1098.00 | NIST | |
Inp | 1089.00 | NIST | |
Inp | 1090.00 | NIST | |
Inp | 1090.00 | NIST | |
Inp | 1098.00 | NIST | |
Inp | Outlier 1057.00 | NIST | |
Inp | 1102.00 | NIST | |
Inp | 1095.00 | NIST | |
Inp | 1076.00 | NIST | |
Inp | 1098.00 | NIST | |
Inp | Outlier 1057.00 | NIST | |
I | [1759.00; 1782.00] |
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|
I | 1776.00 | NIST | |
I | 1782.00 | NIST | |
I | 1770.00 | NIST | |
I | 1759.00 | NIST | |
I | 1779.00 | NIST | |
I | 1770.00 | NIST | |
I | 1770.00 | NIST | |
Tboil | 475.20 | K | NIST |
Tc | 728.04 | K | Joback Calculated Property |
Tfus | [310.00; 346.00] | K |
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Tfus | 310.00 ± 1.00 | K | NIST |
Tfus | 346.00 ± 3.00 | K | NIST |
Vc | 0.440 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [270.14; 333.56] | J/mol×K | [520.95; 728.04] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 270 280 290 300 310 320 330 550 600 650 700 | ||||
Cp,gas | 270.14 | J/mol×K | 520.95 | Joback Calculated Property |
Cp,gas | 282.69 | J/mol×K | 555.46 | Joback Calculated Property |
Cp,gas | 294.38 | J/mol×K | 589.98 | Joback Calculated Property |
Cp,gas | 305.26 | J/mol×K | 624.49 | Joback Calculated Property |
Cp,gas | 315.39 | J/mol×K | 659.01 | Joback Calculated Property |
Cp,gas | 324.80 | J/mol×K | 693.52 | Joback Calculated Property |
Cp,gas | 333.56 | J/mol×K | 728.04 | Joback Calculated Property |
η | [0.0001204; 0.0212186] | Pa×s | [280.85; 520.95] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-3 0.01 0.02 0.02 300 400 500 | ||||
η | 0.0212186 | Pa×s | 280.85 | Joback Calculated Property |
η | 0.0052355 | Pa×s | 320.87 | Joback Calculated Property |
η | 0.0017619 | Pa×s | 360.88 | Joback Calculated Property |
η | 0.0007369 | Pa×s | 400.90 | Joback Calculated Property |
η | 0.0003611 | Pa×s | 440.92 | Joback Calculated Property |
η | 0.0001992 | Pa×s | 480.93 | Joback Calculated Property |
η | 0.0001204 | Pa×s | 520.95 | Joback Calculated Property |
ΔsubH | [82.80; 87.50] | kJ/mol | [289.00; 294.00] | ![]() |
ΔsubH | 82.80 ± 0.70 | kJ/mol | 289.00 | NIST |
ΔsubH | 87.50 ± 2.60 | kJ/mol | 294.00 | NIST |
ΔvapH | [52.90; 63.40] | kJ/mol | [324.50; 407.00] | ![]() |
ΔvapH | 63.40 ± 0.50 | kJ/mol | 324.50 | NIST |
ΔvapH | 52.90 | kJ/mol | 407.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [358.80; 502.14] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.64941e+01 | |||
Coefficient B | -5.17060e+03 | |||
Coefficient C | -3.97590e+01 | |||
Temperature range, min. | 358.80 | |||
Temperature range, max. | 502.14 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 358.80 | Calculated Property |
Pvap | 2.88 | kPa | 374.73 | Calculated Property |
Pvap | 5.80 | kPa | 390.65 | Calculated Property |
Pvap | 11.01 | kPa | 406.58 | Calculated Property |
Pvap | 19.78 | kPa | 422.51 | Calculated Property |
Pvap | 33.94 | kPa | 438.43 | Calculated Property |
Pvap | 55.86 | kPa | 454.36 | Calculated Property |
Pvap | 88.60 | kPa | 470.29 | Calculated Property |
Pvap | 135.99 | kPa | 486.21 | Calculated Property |
Pvap | 202.66 | kPa | 502.14 | Calculated Property |
Pvap | [3.42; 27.81] | kPa | [379.15; 431.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.07927e+02 | |||
Coefficient B | -1.09574e+04 | |||
Coefficient C | -1.32851e+01 | |||
Coefficient D | 7.56204e-06 | |||
Temperature range, min. | 379.15 | |||
Temperature range, max. | 431.15 | |||
T(K) Vapor pressure (kPa) 5 10 15 20 25 30 380 400 420 | ||||
Pvap | 3.42 | kPa | 379.15 | Calculated Property |
Pvap | 4.46 | kPa | 384.93 | Calculated Property |
Pvap | 5.77 | kPa | 390.71 | Calculated Property |
Pvap | 7.39 | kPa | 396.48 | Calculated Property |
Pvap | 9.39 | kPa | 402.26 | Calculated Property |
Pvap | 11.84 | kPa | 408.04 | Calculated Property |
Pvap | 14.81 | kPa | 413.82 | Calculated Property |
Pvap | 18.40 | kPa | 419.59 | Calculated Property |
Pvap | 22.69 | kPa | 425.37 | Calculated Property |
Pvap | 27.81 | kPa | 431.15 | Calculated Property |
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