Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -4590.00 ± 2.80 | kJ/mol | NIST |
ΔfG° | -192.99 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -507.20 ± 3.00 | kJ/mol | NIST |
ΔfH°liquid | -558.90 ± 3.00 | kJ/mol | NIST |
ΔfusH° | 11.10 | kJ/mol | Joback Calculated Property |
ΔvapH° | 42.99 | kJ/mol | Joback Calculated Property |
log10WS | -1.67 | Aq. Sol... | |
logPoct/wat | 1.882 | Crippen Calculated Property | |
McVol | 120.160 | ml/mol | McGowan Calculated Property |
Pc | 3322.01 | kPa | Joback Calculated Property |
Inp | [999.00; 1043.00] |
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|
Inp | Outlier 999.00 | NIST | |
Inp | 1023.00 | NIST | |
Inp | 1010.00 | NIST | |
Inp | 1024.00 | NIST | |
Inp | 1043.00 | NIST | |
Inp | 1042.00 | NIST | |
Inp | 1043.00 | NIST | |
Inp | 1043.00 | NIST | |
Inp | 1043.00 | NIST | |
Inp | 1043.00 | NIST | |
Inp | 1043.00 | NIST | |
Inp | 1043.00 | NIST | |
Inp | 1017.00 | NIST | |
Inp | 1024.00 | NIST | |
Inp | 1010.00 | NIST | |
Inp | 1027.00 | NIST | |
Inp | 1043.00 | NIST | |
Inp | 1027.00 | NIST | |
Inp | 1024.00 | NIST | |
I | [1343.00; 1379.00] |
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|
I | 1379.00 | NIST | |
I | 1343.00 | NIST | |
Tboil | [446.20; 450.20] | K |
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Tboil | 446.26 ± 0.20 | K | NIST |
Tboil | 446.20 | K | NIST |
Tboil | 447.00 | K | NIST |
Tboil | 450.20 ± 1.00 | K | NIST |
Tc | 689.84 | K | Joback Calculated Property |
Tfus | 259.46 | K | Joback Calculated Property |
Ttriple | 224.64 ± 0.15 | K | NIST |
Vc | 0.441 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [263.26; 348.27] | J/mol×K | [478.28; 689.84] | ![]() |
Cp,gas | 263.26 | J/mol×K | 478.28 | Joback Calculated Property |
Cp,gas | 279.37 | J/mol×K | 513.54 | Joback Calculated Property |
Cp,gas | 294.69 | J/mol×K | 548.80 | Joback Calculated Property |
Cp,gas | 309.24 | J/mol×K | 584.06 | Joback Calculated Property |
Cp,gas | 323.01 | J/mol×K | 619.32 | Joback Calculated Property |
Cp,gas | 336.02 | J/mol×K | 654.58 | Joback Calculated Property |
Cp,gas | 348.27 | J/mol×K | 689.84 | Joback Calculated Property |
η | [0.0010100; 0.0019500] | Pa×s | [300.00; 340.00] | ![]() |
η | 0.0019500 | Pa×s | 300.00 | Tempera... |
η | 0.0016100 | Pa×s | 310.00 | Tempera... |
η | 0.0013600 | Pa×s | 320.00 | Tempera... |
η | 0.0011600 | Pa×s | 330.00 | Tempera... |
η | 0.0010100 | Pa×s | 340.00 | Tempera... |
ΔfusH | 8.00 | kJ/mol | 224.60 | NIST |
ΔvapH | [46.70; 52.16] | kJ/mol | [300.11; 407.00] | ![]() |
ΔvapH | 52.16 | kJ/mol | 300.11 | Compreh... |
ΔvapH | 46.70 | kJ/mol | 407.00 | NIST |
n0 | [1.43980; 1.44340] | [293.00; 293.20] | ![]() |
|
n0 | 1.43980 | 293.00 | Quatern... | |
n0 | 1.44220 | 293.15 | Phase e... | |
n0 | 1.44340 | 293.15 | (Liquid... | |
n0 | 1.44250 | 293.15 | Liquid-... | |
n0 | 1.44100 | 293.20 | Phase E... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [333.96; 474.11] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.44507e+01 | |||
Coefficient B | -3.61094e+03 | |||
Coefficient C | -7.90080e+01 | |||
Temperature range, min. | 333.96 | |||
Temperature range, max. | 474.11 | |||
Pvap | 1.33 | kPa | 333.96 | Calculated Property |
Pvap | 3.01 | kPa | 349.53 | Calculated Property |
Pvap | 6.23 | kPa | 365.10 | Calculated Property |
Pvap | 11.95 | kPa | 380.68 | Calculated Property |
Pvap | 21.51 | kPa | 396.25 | Calculated Property |
Pvap | 36.63 | kPa | 411.82 | Calculated Property |
Pvap | 59.49 | kPa | 427.39 | Calculated Property |
Pvap | 92.70 | kPa | 442.97 | Calculated Property |
Pvap | 139.27 | kPa | 458.54 | Calculated Property |
Pvap | 202.64 | kPa | 474.11 | Calculated Property |
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