Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | [-4467.70; -4455.50] | kJ/mol |
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ΔcH°solid | -4459.00 ± 0.90 | kJ/mol | NIST |
ΔcH°solid | -4460.80 ± 1.60 | kJ/mol | NIST |
ΔcH°solid | -4467.70 | kJ/mol | NIST |
ΔcH°solid | -4455.50 ± 0.80 | kJ/mol | NIST |
ΔcH°solid | -4457.20 ± 8.40 | kJ/mol | NIST |
ΔfH°gas | [6.50; 27.60] | kJ/mol |
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ΔfH°gas | 6.50 ± 1.70 | kJ/mol | NIST |
ΔfH°gas | 27.60 ± 2.60 | kJ/mol | NIST |
ΔfH°solid | [-83.00; -81.20] | kJ/mol |
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ΔfH°solid | -83.00 ± 1.50 | kJ/mol | NIST |
ΔfH°solid | -81.20 ± 2.00 | kJ/mol | NIST |
ΔsubH° | [87.90; 109.00] | kJ/mol |
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ΔsubH° | 89.50 ± 0.90 | kJ/mol | NIST |
ΔsubH° | 89.50 ± 0.90 | kJ/mol | NIST |
ΔsubH° | 89.00 ± 1.40 | kJ/mol | NIST |
ΔsubH° | 108.80 ± 1.70 | kJ/mol | NIST |
ΔsubH° | 109.00 ± 0.80 | kJ/mol | NIST |
ΔsubH° | 87.90 ± 0.80 | kJ/mol | NIST |
log10WS | [-2.42; -2.42] |
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|
log10WS | -2.42 | Aq. Sol... | |
log10WS | -2.42 | Estimat... | |
logPoct/wat | 1.940 | Crippen Calculated Property | |
McVol | 110.300 | ml/mol | McGowan Calculated Property |
Inp | [232.24; 1362.00] |
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|
Inp | 1326.30 | NIST | |
Inp | 1348.90 | NIST | |
Inp | 1358.00 | NIST | |
Inp | 1339.00 | NIST | |
Inp | 1362.00 | NIST | |
Inp | 1312.00 | NIST | |
Inp | Outlier 232.24 | NIST | |
I | 2153.00 | NIST | |
Tfus | [347.65; 348.32] | K |
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Tfus | 348.32 | K | Aq. Sol... |
Tfus | 347.65 ± 2.00 | K | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
ΔfusH | [22.10; 40.30] | kJ/mol | [345.70; 346.80] | ![]() |
ΔfusH | 40.30 | kJ/mol | 345.70 | NIST |
ΔfusH | 22.10 | kJ/mol | 346.80 | NIST |
ΔsubH | 108.80 ± 1.70 | kJ/mol | 318.00 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 540.20 | K | 100.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.04; 4298.96] | kPa | [346.00; 788.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.01590e+02 | |||
Coefficient B | -1.21996e+04 | |||
Coefficient C | -1.19913e+01 | |||
Coefficient D | 3.59759e-06 | |||
Temperature range, min. | 346.00 | |||
Temperature range, max. | 788.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 400 500 600 700 | ||||
Pvap | 0.04 | kPa | 346.00 | Calculated Property |
Pvap | 0.66 | kPa | 395.11 | Calculated Property |
Pvap | 5.66 | kPa | 444.22 | Calculated Property |
Pvap | 29.26 | kPa | 493.33 | Calculated Property |
Pvap | 105.65 | kPa | 542.44 | Calculated Property |
Pvap | 295.42 | kPa | 591.56 | Calculated Property |
Pvap | 685.82 | kPa | 640.67 | Calculated Property |
Pvap | 1388.21 | kPa | 689.78 | Calculated Property |
Pvap | 2537.64 | kPa | 738.89 | Calculated Property |
Pvap | 4298.96 | kPa | 788.00 | Calculated Property |
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