Property | Value | Unit | Source |
---|---|---|---|
PAff | 731.20 | kJ/mol | NIST |
BasG | 703.50 | kJ/mol | NIST |
ΔcH°liquid | -2960.70 ± 0.54 | kJ/mol | NIST |
ΔfG° | -287.20 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -283.00 ± 0.92 | kJ/mol | NIST |
ΔfH°liquid | -319.20 ± 0.92 | kJ/mol | NIST |
ΔfusH° | 11.11 | kJ/mol | Joback Calculated Property |
ΔvapH° | [36.20; 36.24] | kJ/mol |
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ΔvapH° | 36.24 | kJ/mol | NIST |
ΔvapH° | 36.20 | kJ/mol | NIST |
ΔvapH° | 36.20 | kJ/mol | NIST |
ΔvapH° | 36.20 ± 0.08 | kJ/mol | NIST |
IE | [9.28; 9.74] | eV |
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IE | 9.29 ± 0.01 | eV | NIST |
IE | 9.28 ± 0.01 | eV | NIST |
IE | 9.30 | eV | NIST |
IE | 9.74 ± 0.02 | eV | NIST |
IE | 9.31 | eV | NIST |
IE | 9.30 | eV | NIST |
IE | 9.60 ± 0.03 | eV | NIST |
log10WS | -2.13 | Crippen Calculated Property | |
logPoct/wat | 1.965 | Crippen Calculated Property | |
McVol | 75.180 | ml/mol | McGowan Calculated Property |
Pc | 4067.32 | kPa | Joback Calculated Property |
Inp | [674.40; 681.00] |
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|
Inp | 674.40 | NIST | |
Inp | 681.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 674.40 | NIST | |
S°liquid | 222.59 | J/mol×K | NIST |
Tboil | [364.50; 367.10] | K |
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Tboil | 365.20 | K | NIST |
Tboil | 364.50 ± 0.50 | K | NIST |
Tboil | 367.10 | K | NIST |
Tc | 557.30 | K | NIST |
Tfus | 197.50 | K | Joback Calculated Property |
Ttriple | 226.01 ± 0.01 | K | NIST |
Vc | 0.299 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [121.64; 165.34] | J/mol×K | [366.88; 557.84] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 120 130 140 150 160 400 450 500 550 | ||||
Cp,gas | 121.64 | J/mol×K | 366.88 | Joback Calculated Property |
Cp,gas | 129.96 | J/mol×K | 398.71 | Joback Calculated Property |
Cp,gas | 137.84 | J/mol×K | 430.53 | Joback Calculated Property |
Cp,gas | 145.31 | J/mol×K | 462.36 | Joback Calculated Property |
Cp,gas | 152.37 | J/mol×K | 494.18 | Joback Calculated Property |
Cp,gas | 159.04 | J/mol×K | 526.01 | Joback Calculated Property |
Cp,gas | 165.34 | J/mol×K | 557.84 | Joback Calculated Property |
Cp,liquid | [159.03; 159.40] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 159.03 | J/mol×K | 298.15 | NIST |
Cp,liquid | 159.40 | J/mol×K | 298.15 | NIST |
ΔfusH | [11.05; 11.05] | kJ/mol | [226.00; 226.01] | ![]() |
ΔfusH | 11.05 | kJ/mol | 226.00 | NIST |
ΔfusH | 11.05 | kJ/mol | 226.00 | NIST |
ΔfusH | 11.05 | kJ/mol | 226.01 | NIST |
ΔvapH | [32.20; 35.50] | kJ/mol | [327.00; 367.10] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 32 32.5 33 33.5 34 34.5 35 35.5 330 340 350 360 | ||||
ΔvapH | 34.60 ± 0.10 | kJ/mol | 327.00 | NIST |
ΔvapH | 33.50 ± 0.10 | kJ/mol | 345.00 | NIST |
ΔvapH | 35.50 | kJ/mol | 353.50 | NIST |
ΔvapH | 32.20 ± 0.10 | kJ/mol | 367.00 | NIST |
ΔvapH | 32.21 | kJ/mol | 367.10 | NIST |
ρl | [1117.00; 1156.00] | kg/m3 | [296.20; 331.10] | ![]() |
ρl | 1156.00 | kg/m3 | 296.20 | Liquid-... |
ρl | 1117.00 | kg/m3 | 331.10 | Liquid-... |
ΔfusS | 48.87 | J/mol×K | 226.01 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 364.70 | K | 100.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [269.41; 389.14] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42556e+01 | |||
Coefficient B | -2.97732e+03 | |||
Coefficient C | -5.62610e+01 | |||
Temperature range, min. | 269.41 | |||
Temperature range, max. | 389.14 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 269.41 | Calculated Property |
Pvap | 3.03 | kPa | 282.71 | Calculated Property |
Pvap | 6.28 | kPa | 296.02 | Calculated Property |
Pvap | 12.06 | kPa | 309.32 | Calculated Property |
Pvap | 21.71 | kPa | 322.62 | Calculated Property |
Pvap | 36.95 | kPa | 335.93 | Calculated Property |
Pvap | 59.92 | kPa | 349.23 | Calculated Property |
Pvap | 93.17 | kPa | 362.53 | Calculated Property |
Pvap | 139.64 | kPa | 375.84 | Calculated Property |
Pvap | 202.64 | kPa | 389.14 | Calculated Property |
Pvap | [9.52; 282.03] | kPa | [304.15; 405.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.47430e+01 | |||
Coefficient B | -6.68596e+03 | |||
Coefficient C | -8.94050e+00 | |||
Coefficient D | 6.59509e-06 | |||
Temperature range, min. | 304.15 | |||
Temperature range, max. | 405.15 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 400 | ||||
Pvap | 9.52 | kPa | 304.15 | Calculated Property |
Pvap | 15.76 | kPa | 315.37 | Calculated Property |
Pvap | 25.04 | kPa | 326.59 | Calculated Property |
Pvap | 38.39 | kPa | 337.82 | Calculated Property |
Pvap | 56.99 | kPa | 349.04 | Calculated Property |
Pvap | 82.19 | kPa | 360.26 | Calculated Property |
Pvap | 115.54 | kPa | 371.48 | Calculated Property |
Pvap | 158.72 | kPa | 382.71 | Calculated Property |
Pvap | 213.56 | kPa | 393.93 | Calculated Property |
Pvap | 282.03 | kPa | 405.15 | Calculated Property |
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