Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | [-4139.90; -4139.50] | kJ/mol |
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ΔcH°liquid | -4139.90 ± 0.59 | kJ/mol | NIST |
ΔcH°liquid | -4139.50 ± 0.59 | kJ/mol | NIST |
ΔfG° | 24.34 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-104.70; -104.50] | kJ/mol |
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ΔfH°gas | -104.70 ± 0.79 | kJ/mol | NIST |
ΔfH°gas | -104.50 | kJ/mol | NIST |
ΔfH°liquid | [-144.80; -144.60] | kJ/mol |
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ΔfH°liquid | -144.80 ± 0.79 | kJ/mol | NIST |
ΔfH°liquid | -144.60 ± 0.75 | kJ/mol | NIST |
ΔfusH° | 12.84 | kJ/mol | Joback Calculated Property |
ΔvapH° | [39.50; 40.10] | kJ/mol |
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ΔvapH° | 40.01 | kJ/mol | NIST |
ΔvapH° | Outlier 39.50 | kJ/mol | NIST |
ΔvapH° | 40.00 | kJ/mol | NIST |
ΔvapH° | 40.10 ± 0.04 | kJ/mol | NIST |
ΔvapH° | 40.10 | kJ/mol | NIST |
ΔvapH° | 40.08 | kJ/mol | NIST |
IE | [8.37; 8.50] | eV |
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IE | 8.37 | eV | NIST |
IE | 8.50 ± 0.05 | eV | NIST |
log10WS | -1.80 | Crippen Calculated Property | |
logPoct/wat | 2.150 | Crippen Calculated Property | |
McVol | 97.660 | ml/mol | McGowan Calculated Property |
Pc | 3538.87 | kPa | Joback Calculated Property |
Inp | [782.00; 801.00] |
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|
Inp | 794.00 | NIST | |
Inp | 794.00 | NIST | |
Inp | 801.00 | NIST | |
Inp | 785.00 | NIST | |
Inp | 785.00 | NIST | |
Inp | 782.00 | NIST | |
Inp | 783.00 | NIST | |
Inp | 785.00 | NIST | |
Inp | 794.00 | NIST | |
I | [1017.00; 1017.00] |
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|
I | 1017.00 | NIST | |
I | 1017.00 | NIST | |
S°liquid | 309.53 | J/mol×K | NIST |
Tboil | [389.00; 391.70] | K |
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Tboil | 391.70 | K | NIST |
Tboil | 391.70 | K | NIST |
Tboil | 391.70 ± 0.30 | K | NIST |
Tboil | 389.00 ± 3.00 | K | NIST |
Tc | 572.69 | K | Joback Calculated Property |
Tfus | 156.11 ± 0.10 | K | NIST |
Ttriple | [156.10; 156.10] | K |
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Ttriple | 156.10 ± 0.04 | K | NIST |
Ttriple | 156.10 ± 0.03 | K | NIST |
Vc | 0.369 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [169.71; 224.63] | J/mol×K | [382.58; 572.69] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 170 180 190 200 210 220 230 400 450 500 550 | ||||
Cp,gas | 169.71 | J/mol×K | 382.58 | Joback Calculated Property |
Cp,gas | 179.76 | J/mol×K | 414.26 | Joback Calculated Property |
Cp,gas | 189.45 | J/mol×K | 445.95 | Joback Calculated Property |
Cp,gas | 198.78 | J/mol×K | 477.63 | Joback Calculated Property |
Cp,gas | 207.75 | J/mol×K | 509.32 | Joback Calculated Property |
Cp,gas | 216.36 | J/mol×K | 541.00 | Joback Calculated Property |
Cp,gas | 224.63 | J/mol×K | 572.69 | Joback Calculated Property |
Cp,liquid | 198.41 | J/mol×K | 298.15 | NIST |
ΔfusH | [10.58; 10.58] | kJ/mol | [156.10; 156.10] | ![]() |
ΔfusH | 10.58 | kJ/mol | 156.10 | NIST |
ΔfusH | 10.58 | kJ/mol | 156.10 | NIST |
ΔfusH | 10.58 | kJ/mol | 156.10 | NIST |
ΔvapH | [34.24; 39.80] | kJ/mol | [355.50; 391.70] | ![]() |
ΔvapH | 39.80 | kJ/mol | 355.50 | NIST |
ΔvapH | 37.80 | kJ/mol | 364.50 | NIST |
ΔvapH | 34.24 | kJ/mol | 391.70 | NIST |
ΔfusS | 67.78 | J/mol×K | 156.10 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [287.68; 417.73] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42227e+01 | |||
Coefficient B | -3.21450e+03 | |||
Coefficient C | -5.70070e+01 | |||
Temperature range, min. | 287.68 | |||
Temperature range, max. | 417.73 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 287.68 | Calculated Property |
Pvap | 3.03 | kPa | 302.13 | Calculated Property |
Pvap | 6.29 | kPa | 316.58 | Calculated Property |
Pvap | 12.08 | kPa | 331.03 | Calculated Property |
Pvap | 21.75 | kPa | 345.48 | Calculated Property |
Pvap | 37.00 | kPa | 359.93 | Calculated Property |
Pvap | 59.99 | kPa | 374.38 | Calculated Property |
Pvap | 93.25 | kPa | 388.83 | Calculated Property |
Pvap | 139.70 | kPa | 403.28 | Calculated Property |
Pvap | 202.63 | kPa | 417.73 | Calculated Property |
Pvap | [1.37; 3391.50] | kPa | [287.15; 584.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.12345e+01 | |||
Coefficient B | -7.82974e+03 | |||
Coefficient C | -1.13601e+01 | |||
Coefficient D | 7.81191e-06 | |||
Temperature range, min. | 287.15 | |||
Temperature range, max. | 584.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 | ||||
Pvap | 1.37 | kPa | 287.15 | Calculated Property |
Pvap | 7.72 | kPa | 320.13 | Calculated Property |
Pvap | 29.60 | kPa | 353.12 | Calculated Property |
Pvap | 86.33 | kPa | 386.10 | Calculated Property |
Pvap | 206.53 | kPa | 419.08 | Calculated Property |
Pvap | 427.27 | kPa | 452.07 | Calculated Property |
Pvap | 793.63 | kPa | 485.05 | Calculated Property |
Pvap | 1360.34 | kPa | 518.03 | Calculated Property |
Pvap | 2196.17 | kPa | 551.02 | Calculated Property |
Pvap | 3391.50 | kPa | 584.00 | Calculated Property |
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