Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | [-6309.00; -6304.00] | kJ/mol | |
ΔcH°solid | -6304.00 ± 3.00 | kJ/mol | NIST |
ΔcH°solid | -6309.00 ± 15.00 | kJ/mol | NIST |
ΔfG° | 49.48 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-152.00; -142.00] | kJ/mol | |
ΔfH°gas | -142.00 ± 3.00 | kJ/mol | NIST |
ΔfH°gas | -152.00 ± 4.70 | kJ/mol | NIST |
ΔfH°gas | -150.00 | kJ/mol | NIST |
ΔfH°solid | [-241.00; -238.00] | kJ/mol | |
ΔfH°solid | -241.00 ± 2.00 | kJ/mol | NIST |
ΔfH°solid | -241.00 ± 3.00 | kJ/mol | NIST |
ΔfH°solid | -238.00 ± 15.00 | kJ/mol | NIST |
ΔfusH° | 20.30 | kJ/mol | Joback Calculated Property |
ΔsubH° | [99.00; 99.00] | kJ/mol | |
ΔsubH° | 99.00 ± 0.40 | kJ/mol | NIST |
ΔsubH° | 99.00 ± 0.40 | kJ/mol | NIST |
ΔvapH° | 58.24 | kJ/mol | Joback Calculated Property |
IE | [8.63; 9.00] | eV | |
IE | 8.80 ± 0.15 | eV | NIST |
IE | 8.76 | eV | NIST |
IE | 8.63 | eV | NIST |
IE | 9.00 | eV | NIST |
IE | 8.98 ± 0.05 | eV | NIST |
log10WS | -2.85 | Aq. Sol... | |
logPoct/wat | 2.906 | Crippen Calculated Property | |
McVol | 153.950 | ml/mol | McGowan Calculated Property |
Pc | 3235.66 | kPa | Joback Calculated Property |
Inp | 1604.00 | NIST | |
I | [2514.00; 2514.00] | ||
I | 2514.00 | NIST | |
I | 2514.00 | NIST | |
Tboil | 571.70 | K | NIST |
Tc | 874.68 | K | Joback Calculated Property |
Tfus | [341.00; 344.15] | K | |
Tfus | 342.35 | K | Aq. Sol... |
Tfus | 344.15 ± 1.50 | K | NIST |
Tfus | 341.00 ± 3.00 | K | NIST |
Vc | 0.572 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [366.53; 437.96] | J/mol×K | [626.49; 874.68] | |
T(K) Ideal gas heat capacity (J/mol×K) 360 380 400 420 440 700 800 | ||||
Cp,gas | 366.53 | J/mol×K | 626.49 | Joback Calculated Property |
Cp,gas | 381.28 | J/mol×K | 667.85 | Joback Calculated Property |
Cp,gas | 394.82 | J/mol×K | 709.22 | Joback Calculated Property |
Cp,gas | 407.20 | J/mol×K | 750.58 | Joback Calculated Property |
Cp,gas | 418.48 | J/mol×K | 791.95 | Joback Calculated Property |
Cp,gas | 428.71 | J/mol×K | 833.31 | Joback Calculated Property |
Cp,gas | 437.96 | J/mol×K | 874.68 | Joback Calculated Property |
η | [0.0001665; 0.0016739] | Pa×s | [361.27; 626.49] | |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 400 500 600 | ||||
η | 0.0016739 | Pa×s | 361.27 | Joback Calculated Property |
η | 0.0009238 | Pa×s | 405.47 | Joback Calculated Property |
η | 0.0005731 | Pa×s | 449.68 | Joback Calculated Property |
η | 0.0003872 | Pa×s | 493.88 | Joback Calculated Property |
η | 0.0002790 | Pa×s | 538.08 | Joback Calculated Property |
η | 0.0002113 | Pa×s | 582.29 | Joback Calculated Property |
η | 0.0001665 | Pa×s | 626.49 | Joback Calculated Property |
ΔvapH | 62.40 | kJ/mol | 483.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [431.70; 624.56] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.52259e+01 | |||
Coefficient B | -5.68560e+03 | |||
Coefficient C | -5.10940e+01 | |||
Temperature range, min. | 431.70 | |||
Temperature range, max. | 624.56 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
Pvap | 1.33 | kPa | 431.70 | Calculated Property |
Pvap | 2.96 | kPa | 453.13 | Calculated Property |
Pvap | 6.05 | kPa | 474.56 | Calculated Property |
Pvap | 11.54 | kPa | 495.99 | Calculated Property |
Pvap | 20.77 | kPa | 517.42 | Calculated Property |
Pvap | 35.48 | kPa | 538.84 | Calculated Property |
Pvap | 57.95 | kPa | 560.27 | Calculated Property |
Pvap | 90.98 | kPa | 581.70 | Calculated Property |
Pvap | 137.90 | kPa | 603.13 | Calculated Property |
Pvap | 202.64 | kPa | 624.56 | Calculated Property |
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