Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -4286.90 ± 2.10 | kJ/mol | NIST |
ΔfG° | -90.74 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -247.83 | kJ/mol | Joback Calculated Property |
ΔfusH° | 12.50 | kJ/mol | Joback Calculated Property |
ΔvapH° | [66.90; 68.10] | kJ/mol |
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ΔvapH° | 68.10 ± 1.40 | kJ/mol | NIST |
ΔvapH° | 66.90 | kJ/mol | NIST |
IE | [7.80; 8.17] | eV |
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IE | 7.80 | eV | NIST |
IE | 7.80 | eV | NIST |
IE | 7.80 ± 0.15 | eV | NIST |
IE | 8.17 | eV | NIST |
IE | 7.80 | eV | NIST |
log10WS | -1.31 | Aq. Sol... | |
logPoct/wat | 1.704 | Crippen Calculated Property | |
McVol | 111.560 | ml/mol | McGowan Calculated Property |
Pc | 3443.98 | kPa | Joback Calculated Property |
Inp | [200.73; 1155.00] |
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|
Inp | 1131.00 | NIST | |
Inp | 1114.00 | NIST | |
Inp | 1121.00 | NIST | |
Inp | 1128.00 | NIST | |
Inp | 1114.00 | NIST | |
Inp | 1127.00 | NIST | |
Inp | 1149.00 | NIST | |
Inp | 1148.00 | NIST | |
Inp | 1149.00 | NIST | |
Inp | 1148.00 | NIST | |
Inp | 1142.00 | NIST | |
Inp | 1111.20 | NIST | |
Inp | 1126.00 | NIST | |
Inp | 1117.00 | NIST | |
Inp | 1114.00 | NIST | |
Inp | 1153.80 | NIST | |
Inp | 1147.00 | NIST | |
Inp | 1147.00 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1143.00 | NIST | |
Inp | 1153.00 | NIST | |
Inp | 1110.00 | NIST | |
Inp | 1146.00 | NIST | |
Inp | 1143.00 | NIST | |
Inp | 1153.00 | NIST | |
Inp | 1153.00 | NIST | |
Inp | 1110.00 | NIST | |
Inp | 1111.00 | NIST | |
Inp | 1155.00 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1111.00 | NIST | |
Inp | 1111.00 | NIST | |
Inp | 1111.00 | NIST | |
Inp | 1112.00 | NIST | |
Inp | 1110.00 | NIST | |
Inp | 1150.00 | NIST | |
Inp | 1111.00 | NIST | |
Inp | 1151.00 | NIST | |
Inp | 1154.00 | NIST | |
Inp | 1150.00 | NIST | |
Inp | 1150.00 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1147.00 | NIST | |
Inp | 1146.00 | NIST | |
Inp | 1152.00 | NIST | |
Inp | 1151.00 | NIST | |
Inp | Outlier 200.73 | NIST | |
Inp | 1149.00 | NIST | |
Inp | 1111.20 | NIST | |
Inp | 1109.00 | NIST | |
Inp | 1151.00 | NIST | |
Inp | 1147.00 | NIST | |
Inp | 1131.00 | NIST | |
Inp | 1127.00 | NIST | |
I | [1699.00; 1753.00] |
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|
I | 1699.00 | NIST | |
I | 1703.00 | NIST | |
I | 1718.00 | NIST | |
I | Outlier 1752.00 | NIST | |
I | Outlier 1753.00 | NIST | |
I | 1699.00 | NIST | |
I | 1706.00 | NIST | |
I | 1741.00 | NIST | |
I | 1731.00 | NIST | |
I | 1731.00 | NIST | |
I | 1704.00 | NIST | |
I | 1704.00 | NIST | |
I | 1721.00 | NIST | |
I | 1727.00 | NIST | |
I | 1716.00 | NIST | |
I | 1732.00 | NIST | |
I | 1699.00 | NIST | |
I | 1720.00 | NIST | |
I | 1737.00 | NIST | |
I | 1701.00 | NIST | |
I | 1717.00 | NIST | |
I | 1721.00 | NIST | |
I | 1740.00 | NIST | |
I | 1703.00 | NIST | |
I | 1715.00 | NIST | |
I | 1715.00 | NIST | |
I | 1731.00 | NIST | |
I | 1727.00 | NIST | |
I | 1706.00 | NIST | |
Tboil | [299.95; 480.25] | K |
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Tboil | 479.20 | K | NIST |
Tboil | 480.00 | K | NIST |
Tboil | 299.95 ± 0.40 | K | NIST |
Tboil | 478.70 ± 0.50 | K | NIST |
Tboil | 480.25 ± 1.00 | K | NIST |
Tc | 667.35 | K | Joback Calculated Property |
Tfus | [288.00; 296.00] | K |
![]() |
Tfus | 292.98 | K | Aq. Sol... |
Tfus | 288.00 | K | NIST |
Tfus | 295.65 ± 0.30 | K | NIST |
Tfus | 295.65 ± 0.50 | K | NIST |
Tfus | 296.00 ± 0.50 | K | NIST |
Vc | 0.411 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [221.28; 284.22] | J/mol×K | [458.94; 667.35] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 220 230 240 250 260 270 280 290 500 550 600 650 | ||||
Cp,gas | 221.28 | J/mol×K | 458.94 | Joback Calculated Property |
Cp,gas | 232.94 | J/mol×K | 493.67 | Joback Calculated Property |
Cp,gas | 244.14 | J/mol×K | 528.41 | Joback Calculated Property |
Cp,gas | 254.88 | J/mol×K | 563.14 | Joback Calculated Property |
Cp,gas | 265.14 | J/mol×K | 597.88 | Joback Calculated Property |
Cp,gas | 274.92 | J/mol×K | 632.61 | Joback Calculated Property |
Cp,gas | 284.22 | J/mol×K | 667.35 | Joback Calculated Property |
η | [0.0001740; 0.0014041] | Pa×s | [263.32; 458.94] | ![]() |
T(K) Dynamic viscosity (Pa×s) 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 300 350 400 450 | ||||
η | 0.0014041 | Pa×s | 263.32 | Joback Calculated Property |
η | 0.0008184 | Pa×s | 295.92 | Joback Calculated Property |
η | 0.0005310 | Pa×s | 328.53 | Joback Calculated Property |
η | 0.0003725 | Pa×s | 361.13 | Joback Calculated Property |
η | 0.0002771 | Pa×s | 393.73 | Joback Calculated Property |
η | 0.0002157 | Pa×s | 426.34 | Joback Calculated Property |
η | 0.0001740 | Pa×s | 458.94 | Joback Calculated Property |
ΔvapH | 52.70 | kJ/mol | 420.50 | NIST |
Pvap | [2.66; 37.20] | kPa | [373.15; 443.15] | ![]() |
T(K) Vapor pressure (kPa) 0 5 10 15 20 25 30 35 40 380 400 420 440 | ||||
Pvap | 2.66 | kPa | 373.15 | Isother... |
Pvap | 4.15 | kPa | 383.15 | Isother... |
Pvap | 6.40 | kPa | 393.15 | Isother... |
Pvap | 13.70 | kPa | 413.15 | Isother... |
Pvap | 23.10 | kPa | 428.15 | Isother... |
Pvap | 37.20 | kPa | 443.15 | Isother... |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 363.20 | K | 1.30 | NIST |
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