Property | Value | Unit | Source |
---|---|---|---|
ΔcH°solid | -7927.40 ± 4.20 | kJ/mol | NIST |
ΔfG° | 204.55 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -255.00 ± 4.20 | kJ/mol | NIST |
ΔfH°solid | -333.00 ± 4.20 | kJ/mol | NIST |
ΔfusH° | 3.91 | kJ/mol | Joback Calculated Property |
ΔsubH° | [77.80; 78.00] | kJ/mol |
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ΔsubH° | 78.00 ± 1.00 | kJ/mol | NIST |
ΔsubH° | 78.00 | kJ/mol | NIST |
ΔsubH° | 77.80 ± 1.30 | kJ/mol | NIST |
ΔvapH° | 51.70 ± 0.20 | kJ/mol | NIST |
log10WS | -3.98 | Crippen Calculated Property | |
logPoct/wat | 4.003 | Crippen Calculated Property | |
McVol | 161.450 | ml/mol | McGowan Calculated Property |
Pc | 2632.55 | kPa | Joback Calculated Property |
Inp | [1128.00; 1204.00] |
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|
Inp | 1194.00 | NIST | |
Inp | 1143.00 | NIST | |
Inp | 1148.00 | NIST | |
Inp | 1152.00 | NIST | |
Inp | 1157.00 | NIST | |
Inp | 1163.00 | NIST | |
Inp | 1153.00 | NIST | |
Inp | 1161.00 | NIST | |
Inp | 1170.00 | NIST | |
Inp | 1148.00 | NIST | |
Inp | 1152.00 | NIST | |
Inp | 1157.00 | NIST | |
Inp | 1147.00 | NIST | |
Inp | Outlier 1204.00 | NIST | |
Inp | 1153.00 | NIST | |
Inp | 1161.00 | NIST | |
Inp | 1170.00 | NIST | |
Inp | 1163.00 | NIST | |
Inp | 1173.00 | NIST | |
Inp | 1185.00 | NIST | |
Inp | 1194.00 | NIST | |
Inp | 1128.00 | NIST | |
Inp | 1163.00 | NIST | |
Inp | 1163.00 | NIST | |
Inp | 1128.00 | NIST | |
I | [1274.00; 1310.00] |
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|
I | 1274.00 | NIST | |
I | 1292.00 | NIST | |
I | 1310.00 | NIST | |
Tboil | 517.38 | K | Joback Calculated Property |
Tc | 749.29 | K | Joback Calculated Property |
Tfus | 253.60 ± 0.20 | K | NIST |
Vc | 0.620 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [417.44; 530.62] | J/mol×K | [517.38; 749.29] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 420 440 460 480 500 520 540 600 700 | ||||
Cp,gas | 417.44 | J/mol×K | 517.38 | Joback Calculated Property |
Cp,gas | 440.13 | J/mol×K | 556.03 | Joback Calculated Property |
Cp,gas | 460.69 | J/mol×K | 594.68 | Joback Calculated Property |
Cp,gas | 479.58 | J/mol×K | 633.33 | Joback Calculated Property |
Cp,gas | 497.24 | J/mol×K | 671.98 | Joback Calculated Property |
Cp,gas | 514.10 | J/mol×K | 710.64 | Joback Calculated Property |
Cp,gas | 530.62 | J/mol×K | 749.29 | Joback Calculated Property |
ΔfusH | [1.73; 6.30] | kJ/mol | [228.20; 253.60] | ![]() |
ΔfusH | 6.30 | kJ/mol | 228.20 | NIST |
ΔfusH | 1.73 | kJ/mol | 253.60 | NIST |
ΔfusH | 1.73 | kJ/mol | 253.60 | NIST |
ρl | [859.20; 887.48] | kg/m3 | [293.15; 333.15] | ![]() |
T(K) Liquid Density (kg/m3) 860 865 870 875 880 885 890 300 310 320 330 | ||||
ρl | 887.48 | kg/m3 | 293.15 | Density... |
ρl | 883.99 | kg/m3 | 298.15 | Density... |
ρl | 880.47 | kg/m3 | 303.15 | Density... |
ρl | 876.94 | kg/m3 | 308.15 | Density... |
ρl | 873.40 | kg/m3 | 313.15 | Density... |
ρl | 869.86 | kg/m3 | 318.15 | Density... |
ρl | 866.31 | kg/m3 | 323.15 | Density... |
ρl | 862.76 | kg/m3 | 328.15 | Density... |
ρl | 859.20 | kg/m3 | 333.15 | Density... |
ΔfusS | [6.82; 27.61] | J/mol×K | [228.20; 253.60] | ![]() |
ΔfusS | 27.61 | J/mol×K | 228.20 | NIST |
ΔfusS | 6.82 | J/mol×K | 253.60 | NIST |
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