Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -761.60 ± 3.20 | kJ/mol | NIST |
ΔfG° | -615.68 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -699.90 ± 3.80 | kJ/mol | NIST |
ΔfH°liquid | -720.00 ± 4.90 | kJ/mol | NIST |
ΔfusH° | 8.72 | kJ/mol | Joback Calculated Property |
ΔvapH° | [29.56; 29.80] | kJ/mol |
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ΔvapH° | 29.80 | kJ/mol | NIST |
ΔvapH° | 29.80 ± 0.40 | kJ/mol | NIST |
ΔvapH° | 29.56 ± 0.33 | kJ/mol | NIST |
ΔvapH° | 29.60 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 29.60 ± 0.10 | kJ/mol | NIST |
IE | [11.00; 11.20] | eV |
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IE | 11.00 | eV | NIST |
IE | 11.20 | eV | NIST |
log10WS | [-1.71; -1.53] |
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|
log10WS | -1.53 | Aq. Sol... | |
log10WS | -1.71 | Estimat... | |
logPoct/wat | 2.509 | Crippen Calculated Property | |
McVol | 74.090 | ml/mol | McGowan Calculated Property |
Pc | 4528.58 | kPa | Joback Calculated Property |
Inp | [533.00; 555.00] |
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|
Inp | 541.00 | NIST | |
Inp | 543.00 | NIST | |
Inp | 543.00 | NIST | |
Inp | 533.00 | NIST | |
Inp | 555.00 | NIST | |
Inp | 533.00 | NIST | |
Inp | 543.00 | NIST | |
I | 858.00 | NIST | |
Tboil | [323.00; 596.40] | K |
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Tboil | 323.40 | K | NIST |
Tboil | 596.40 ± 0.40 | K | NIST |
Tboil | 323.00 | K | NIST |
Tboil | 323.30 | K | NIST |
Tboil | 323.42 ± 0.01 | K | NIST |
Tc | 496.30 | K | NIST |
Tfus | 157.40 ± 0.20 | K | NIST |
Vc | 0.295 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [112.10; 137.51] | J/mol×K | [342.89; 523.53] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 110 115 120 125 130 135 140 350 400 450 500 | ||||
Cp,gas | 112.10 | J/mol×K | 342.89 | Joback Calculated Property |
Cp,gas | 117.35 | J/mol×K | 373.00 | Joback Calculated Property |
Cp,gas | 122.16 | J/mol×K | 403.10 | Joback Calculated Property |
Cp,gas | 126.55 | J/mol×K | 433.21 | Joback Calculated Property |
Cp,gas | 130.56 | J/mol×K | 463.31 | Joback Calculated Property |
Cp,gas | 134.21 | J/mol×K | 493.42 | Joback Calculated Property |
Cp,gas | 137.51 | J/mol×K | 523.53 | Joback Calculated Property |
Cp,liquid | 156.60 | J/mol×K | 298.15 | NIST |
ΔfusH | [4.84; 4.84] | kJ/mol | [154.70; 157.40] | ![]() |
ΔfusH | 4.84 | kJ/mol | 154.70 | NIST |
ΔfusH | 4.84 | kJ/mol | 154.70 | NIST |
ΔfusH | 4.84 | kJ/mol | 157.40 | NIST |
ΔvapH | [26.80; 34.30] | kJ/mol | [272.50; 343.00] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 28 30 32 34 280 300 320 340 | ||||
ΔvapH | 34.30 | kJ/mol | 272.50 | NIST |
ΔvapH | 33.20 | kJ/mol | 275.50 | NIST |
ΔvapH | 30.00 | kJ/mol | 310.50 | NIST |
ΔvapH | 28.70 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 28.08 | kJ/mol | 323.30 | NIST |
ΔvapH | 27.80 ± 0.10 | kJ/mol | 328.00 | NIST |
ΔvapH | 26.80 ± 0.10 | kJ/mol | 343.00 | NIST |
ΔfusS | 30.70 | J/mol×K | 157.40 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.49; 202.67] | kPa | [223.15; 346.52] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.30696e+01 | |||
Coefficient B | -2.19144e+03 | |||
Coefficient C | -6.40470e+01 | |||
Temperature range, min. | 223.15 | |||
Temperature range, max. | 346.52 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 | ||||
Pvap | 0.49 | kPa | 223.15 | Calculated Property |
Pvap | 1.47 | kPa | 236.86 | Calculated Property |
Pvap | 3.75 | kPa | 250.57 | Calculated Property |
Pvap | 8.37 | kPa | 264.27 | Calculated Property |
Pvap | 16.88 | kPa | 277.98 | Calculated Property |
Pvap | 31.28 | kPa | 291.69 | Calculated Property |
Pvap | 54.04 | kPa | 305.40 | Calculated Property |
Pvap | 88.03 | kPa | 319.10 | Calculated Property |
Pvap | 136.44 | kPa | 332.81 | Calculated Property |
Pvap | 202.67 | kPa | 346.52 | Calculated Property |
Pvap | [0.46; 118.43] | kPa | [222.00; 328.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.11666e+02 | |||
Coefficient B | -7.03230e+03 | |||
Coefficient C | -1.51373e+01 | |||
Coefficient D | 2.08113e-05 | |||
Temperature range, min. | 222.00 | |||
Temperature range, max. | 328.00 | |||
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 120 250 300 | ||||
Pvap | 0.46 | kPa | 222.00 | Calculated Property |
Pvap | 1.17 | kPa | 233.78 | Calculated Property |
Pvap | 2.65 | kPa | 245.56 | Calculated Property |
Pvap | 5.47 | kPa | 257.33 | Calculated Property |
Pvap | 10.45 | kPa | 269.11 | Calculated Property |
Pvap | 18.70 | kPa | 280.89 | Calculated Property |
Pvap | 31.65 | kPa | 292.67 | Calculated Property |
Pvap | 51.09 | kPa | 304.44 | Calculated Property |
Pvap | 79.16 | kPa | 316.22 | Calculated Property |
Pvap | 118.43 | kPa | 328.00 | Calculated Property |
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