Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 108.54 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 19.00 ± 3.00 | kJ/mol | NIST |
ΔfH°liquid | -33.00 ± 3.00 | kJ/mol | NIST |
ΔfusH° | 12.12 | kJ/mol | Joback Calculated Property |
ΔvapH° | [49.90; 51.00] | kJ/mol | |
ΔvapH° | 50.10 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 49.90 | kJ/mol | NIST |
ΔvapH° | 50.10 ± 0.50 | kJ/mol | NIST |
ΔvapH° | 51.00 ± 2.00 | kJ/mol | NIST |
IE | [9.10; 9.30] | eV | |
IE | 9.10 ± 0.02 | eV | NIST |
IE | 9.14 ± 0.01 | eV | NIST |
IE | 9.14 ± 0.01 | eV | NIST |
IE | 9.10 ± 0.05 | eV | NIST |
IE | 9.30 | eV | NIST |
IE | 9.29 | eV | NIST |
IE | 9.30 | eV | NIST |
log10WS | [-2.39; -2.39] | ||
log10WS | -2.39 | Aq. Sol... | |
log10WS | -2.39 | Estimat... | |
logPoct/wat | 2.425 | Crippen Calculated Property | |
McVol | 97.970 | ml/mol | McGowan Calculated Property |
NFPA Fire | 2 | KDB | |
NFPA Health | 2 | KDB | |
NFPA Safety | 1 | KDB | |
Pc | 3925.85 | kPa | Joback Calculated Property |
Inp | [977.90; 1023.00] | ||
Inp | 1015.00 | NIST | |
Inp | 977.90 | NIST | |
Inp | Outlier 1023.00 | NIST | |
Inp | 985.60 | NIST | |
Inp | 1002.00 | NIST | |
Inp | 1008.00 | NIST | |
Inp | 986.00 | NIST | |
Inp | 996.00 | NIST | |
Inp | 997.00 | NIST | |
Inp | 986.00 | NIST | |
Inp | 986.00 | NIST | |
Inp | 986.00 | NIST | |
Inp | 986.00 | NIST | |
Inp | 983.00 | NIST | |
I | [1478.00; 1497.00] | ||
I | 1478.00 | NIST | |
I | 1497.00 | NIST | |
I | 1478.00 | NIST | |
Tboil | 452.15 | K | KDB |
Tc | 643.33 | K | Joback Calculated Property |
Tfus | [225.30; 233.95] | K | |
Tfus | 233.95 | K | KDB |
Tfus | 229.48 | K | Aq. Sol... |
Tfus | 233.95 ± 0.30 | K | NIST |
Tfus | 233.45 ± 0.40 | K | NIST |
Tfus | 225.30 ± 0.50 | K | NIST |
Vc | 0.368 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [163.08; 218.66] | J/mol×K | [423.67; 643.33] | |
T(K) Ideal gas heat capacity (J/mol×K) 160 170 180 190 200 210 220 450 500 550 600 | ||||
Cp,gas | 163.08 | J/mol×K | 423.67 | Joback Calculated Property |
Cp,gas | 173.99 | J/mol×K | 460.28 | Joback Calculated Property |
Cp,gas | 184.20 | J/mol×K | 496.89 | Joback Calculated Property |
Cp,gas | 193.74 | J/mol×K | 533.50 | Joback Calculated Property |
Cp,gas | 202.64 | J/mol×K | 570.11 | Joback Calculated Property |
Cp,gas | 210.94 | J/mol×K | 606.72 | Joback Calculated Property |
Cp,gas | 218.66 | J/mol×K | 643.33 | Joback Calculated Property |
Cp,liquid | 182.40 | J/mol×K | 298.50 | NIST |
η | [0.0002746; 0.0031741] | Pa×s | [224.99; 423.67] | |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 250 300 350 400 | ||||
η | 0.0031741 | Pa×s | 224.99 | Joback Calculated Property |
η | 0.0016248 | Pa×s | 258.10 | Joback Calculated Property |
η | 0.0009686 | Pa×s | 291.22 | Joback Calculated Property |
η | 0.0006417 | Pa×s | 324.33 | Joback Calculated Property |
η | 0.0004588 | Pa×s | 357.44 | Joback Calculated Property |
η | 0.0003473 | Pa×s | 390.56 | Joback Calculated Property |
η | 0.0002746 | Pa×s | 423.67 | Joback Calculated Property |
ΔfusH | 8.74 | kJ/mol | 230.00 | NIST |
ΔvapH | [48.60; 48.60] | kJ/mol | [355.00; 374.00] | |
ΔvapH | 48.60 | kJ/mol | 355.00 | NIST |
ΔvapH | 48.60 | kJ/mol | 374.00 | NIST |
ρl | 1094.82 | kg/m3 | 298.15 | Excess ... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [332.04; 482.07] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41881e+01 | |||
Coefficient B | -3.68477e+03 | |||
Coefficient C | -6.69590e+01 | |||
Temperature range, min. | 332.04 | |||
Temperature range, max. | 482.07 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 332.04 | Calculated Property |
Pvap | 3.03 | kPa | 348.71 | Calculated Property |
Pvap | 6.30 | kPa | 365.38 | Calculated Property |
Pvap | 12.11 | kPa | 382.05 | Calculated Property |
Pvap | 21.79 | kPa | 398.72 | Calculated Property |
Pvap | 37.07 | kPa | 415.39 | Calculated Property |
Pvap | 60.08 | kPa | 432.06 | Calculated Property |
Pvap | 93.35 | kPa | 448.73 | Calculated Property |
Pvap | 139.79 | kPa | 465.40 | Calculated Property |
Pvap | 202.66 | kPa | 482.07 | Calculated Property |
Pvap | [7.17e-04; 3776.09] | kPa | [234.15; 686.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 4.79326e+01 | |||
Coefficient B | -7.14622e+03 | |||
Coefficient C | -4.52442e+00 | |||
Coefficient D | 5.72779e-07 | |||
Temperature range, min. | 234.15 | |||
Temperature range, max. | 686.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 600 | ||||
Pvap | 7.17e-04 | kPa | 234.15 | Calculated Property |
Pvap | 0.07 | kPa | 284.36 | Calculated Property |
Pvap | 1.40 | kPa | 334.56 | Calculated Property |
Pvap | 12.33 | kPa | 384.77 | Calculated Property |
Pvap | 61.85 | kPa | 434.97 | Calculated Property |
Pvap | 212.08 | kPa | 485.18 | Calculated Property |
Pvap | 556.70 | kPa | 535.38 | Calculated Property |
Pvap | 1203.63 | kPa | 585.59 | Calculated Property |
Pvap | 2252.29 | kPa | 635.79 | Calculated Property |
Pvap | 3776.09 | kPa | 686.00 | Calculated Property |
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