Property | Value | Unit | Source |
---|---|---|---|
PAff | 801.70 | kJ/mol | NIST |
BasG | 770.50 | kJ/mol | NIST |
ΔfG° | 12.19 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -87.41 | kJ/mol | Joback Calculated Property |
ΔfusH° | 10.16 | kJ/mol | Joback Calculated Property |
ΔvapH° | [36.50; 36.70] | kJ/mol |
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ΔvapH° | 36.70 | kJ/mol | NIST |
ΔvapH° | 36.50 | kJ/mol | NIST |
ΔvapH° | 36.60 ± 0.40 | kJ/mol | NIST |
IE | [9.14; 9.15] | eV |
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IE | 9.14 ± 0.01 | eV | NIST |
IE | 9.15 | eV | NIST |
IE | 9.14 ± 0.02 | eV | NIST |
log10WS | [-2.18; -2.18] |
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|
log10WS | -2.18 | Aq. Sol... | |
log10WS | -2.18 | Estimat... | |
logPoct/wat | 1.716 | Crippen Calculated Property | |
McVol | 83.570 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
NFPA Health | 2 | KDB | |
Pc | 4227.54 | kPa | Joback Calculated Property |
ρc | 277.78 ± 6.31 | kg/m3 | NIST |
Inp | [673.00; 742.00] |
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|
Inp | 721.30 | NIST | |
Inp | 729.70 | NIST | |
Inp | 714.80 | NIST | |
Inp | 716.90 | NIST | |
Inp | 716.60 | NIST | |
Inp | 718.90 | NIST | |
Inp | 722.00 | NIST | |
Inp | 726.00 | NIST | |
Inp | 691.00 | NIST | |
Inp | 693.00 | NIST | |
Inp | 724.00 | NIST | |
Inp | Outlier 673.00 | NIST | |
Inp | 701.00 | NIST | |
Inp | 693.00 | NIST | |
Inp | 713.00 | NIST | |
Inp | 703.00 | NIST | |
Inp | 718.00 | NIST | |
Inp | 701.00 | NIST | |
Inp | 726.00 | NIST | |
Inp | 699.00 | NIST | |
Inp | 721.00 | NIST | |
Inp | 715.00 | NIST | |
Inp | 717.00 | NIST | |
Inp | Outlier 742.00 | NIST | |
Inp | 718.00 | NIST | |
Inp | Outlier 677.00 | NIST | |
Inp | 705.00 | NIST | |
Inp | 713.00 | NIST | |
Inp | 692.00 | NIST | |
Inp | 721.00 | NIST | |
I | [919.00; 960.00] |
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|
I | 938.00 | NIST | |
I | 960.00 | NIST | |
I | 919.00 | NIST | |
I | 944.00 | NIST | |
I | 944.00 | NIST | |
I | 938.00 | NIST | |
S°liquid | 275.98 | J/mol×K | NIST |
Tboil | [369.00; 372.00] | K |
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Tboil | 371.60 | K | KDB |
Tboil | 371.60 | K | NIST |
Tboil | 371.00 | K | NIST |
Tboil | 371.60 | K | NIST |
Tboil | 370.00 ± 2.00 | K | NIST |
Tboil | 370.00 ± 2.00 | K | NIST |
Tboil | 371.20 ± 0.40 | K | NIST |
Tboil | Outlier 369.00 ± 3.00 | K | NIST |
Tboil | Outlier 369.00 ± 4.00 | K | NIST |
Tboil | 371.73 ± 0.40 | K | NIST |
Tboil | 370.20 ± 0.30 | K | NIST |
Tboil | 372.00 ± 3.00 | K | NIST |
Tboil | 371.73 ± 0.25 | K | NIST |
Tboil | 370.70 ± 0.50 | K | NIST |
Tboil | 370.70 ± 0.70 | K | NIST |
Tboil | 371.00 ± 3.00 | K | NIST |
Tboil | 371.30 ± 1.00 | K | NIST |
Tboil | 370.40 ± 1.50 | K | NIST |
Tboil | 371.00 ± 3.00 | K | NIST |
Tboil | 371.00 ± 3.00 | K | NIST |
Tc | [569.20; 570.10] | K |
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Tc | 570.10 | K | KDB |
Tc | 570.10 ± 0.40 | K | NIST |
Tc | 569.20 | K | NIST |
Tfus | [157.03; 157.48] | K |
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Tfus | 157.23 | K | Aq. Sol... |
Tfus | 157.40 | K | KDB |
Tfus | 157.48 ± 0.07 | K | NIST |
Tfus | 157.03 ± 0.25 | K | NIST |
Tfus | 157.30 ± 0.50 | K | NIST |
Tfus | 157.30 ± 0.30 | K | NIST |
Ttriple | [157.46; 157.47] | K |
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Ttriple | 157.46 | K | KDB |
Ttriple | 157.47 ± 0.05 | K | NIST |
Vc | 0.324 | m3/kmol | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [134.39; 180.66] | J/mol×K | [353.78; 544.40] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 130 140 150 160 170 180 350 400 450 500 | ||||
Cp,gas | 134.39 | J/mol×K | 353.78 | Joback Calculated Property |
Cp,gas | 142.92 | J/mol×K | 385.55 | Joback Calculated Property |
Cp,gas | 151.11 | J/mol×K | 417.32 | Joback Calculated Property |
Cp,gas | 158.97 | J/mol×K | 449.09 | Joback Calculated Property |
Cp,gas | 166.51 | J/mol×K | 480.86 | Joback Calculated Property |
Cp,gas | 173.74 | J/mol×K | 512.63 | Joback Calculated Property |
Cp,gas | 180.66 | J/mol×K | 544.40 | Joback Calculated Property |
Cp,liquid | [171.39; 172.30] | J/mol×K | [298.15; 300.00] | ![]() |
Cp,liquid | 172.30 | J/mol×K | 298.15 | NIST |
Cp,liquid | 171.39 | J/mol×K | 300.00 | NIST |
ΔfusH | [10.46; 10.46] | kJ/mol | [157.47; 157.50] | ![]() |
ΔfusH | 10.46 | kJ/mol | 157.47 | NIST |
ΔfusH | 10.46 | kJ/mol | 157.50 | NIST |
ΔfusH | 10.46 | kJ/mol | 157.50 | NIST |
ΔvapH | [32.20; 35.00] | kJ/mol | [330.00; 371.60] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 32 32.5 33 33.5 34 34.5 35 340 360 | ||||
ΔvapH | 34.70 ± 0.10 | kJ/mol | 330.00 | NIST |
ΔvapH | 33.60 ± 0.10 | kJ/mol | 350.00 | NIST |
ΔvapH | 35.00 | kJ/mol | 366.00 | NIST |
ΔvapH | 32.20 ± 0.10 | kJ/mol | 371.00 | NIST |
ΔvapH | 32.23 | kJ/mol | 371.60 | NIST |
Pvap | [23.10; 100.50] | kPa | [328.08; 371.04] | ![]() |
T(K) Vapor pressure (kPa) 20 40 60 80 100 340 360 | ||||
Pvap | 23.10 | kPa | 328.08 | Phase e... |
Pvap | 31.40 | kPa | 336.10 | Phase e... |
Pvap | 40.90 | kPa | 343.41 | Phase e... |
Pvap | 52.10 | kPa | 350.44 | Phase e... |
Pvap | 61.90 | kPa | 355.65 | Phase e... |
Pvap | 72.60 | kPa | 360.57 | Phase e... |
Pvap | 81.90 | kPa | 364.39 | Phase e... |
Pvap | 91.60 | kPa | 368.05 | Phase e... |
Pvap | 100.50 | kPa | 371.04 | Phase e... |
ΔfusS | 66.43 | J/mol×K | 157.47 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [277.69; 393.34] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.54429e+01 | |||
Coefficient B | -3.53467e+03 | |||
Coefficient C | -4.44580e+01 | |||
Temperature range, min. | 277.69 | |||
Temperature range, max. | 393.34 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 277.69 | Calculated Property |
Pvap | 2.94 | kPa | 290.54 | Calculated Property |
Pvap | 6.00 | kPa | 303.39 | Calculated Property |
Pvap | 11.44 | kPa | 316.24 | Calculated Property |
Pvap | 20.58 | kPa | 329.09 | Calculated Property |
Pvap | 35.20 | kPa | 341.94 | Calculated Property |
Pvap | 57.56 | kPa | 354.79 | Calculated Property |
Pvap | 90.54 | kPa | 367.64 | Calculated Property |
Pvap | 137.55 | kPa | 380.49 | Calculated Property |
Pvap | 202.64 | kPa | 393.34 | Calculated Property |
Pvap | [1.65e-06; 3969.92] | kPa | [157.46; 569.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.14838e+01 | |||
Coefficient B | -7.01146e+03 | |||
Coefficient C | -9.97282e+00 | |||
Coefficient D | 7.38659e-06 | |||
Temperature range, min. | 157.46 | |||
Temperature range, max. | 569.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 300 400 500 | ||||
Pvap | 1.65e-06 | kPa | 157.46 | Calculated Property |
Pvap | 3.29e-03 | kPa | 203.19 | Calculated Property |
Pvap | 0.29 | kPa | 248.91 | Calculated Property |
Pvap | 5.08 | kPa | 294.64 | Calculated Property |
Pvap | 36.53 | kPa | 340.37 | Calculated Property |
Pvap | 152.32 | kPa | 386.09 | Calculated Property |
Pvap | 449.90 | kPa | 431.82 | Calculated Property |
Pvap | 1061.17 | kPa | 477.55 | Calculated Property |
Pvap | 2156.52 | kPa | 523.27 | Calculated Property |
Pvap | 3969.92 | kPa | 569.00 | Calculated Property |
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