Property | Value | Unit | Source |
---|---|---|---|
PAff | 846.40 | kJ/mol | NIST |
BasG | 816.20 | kJ/mol | NIST |
IE | [9.59; 9.88] | eV |
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IE | 9.60 ± 1.00 | eV | NIST |
IE | 9.64 ± 0.01 | eV | NIST |
IE | 9.59 ± 0.04 | eV | NIST |
IE | 9.88 | eV | NIST |
log10WS | 2.48 | Crippen Calculated Property | |
logPoct/wat | 2.673 | Crippen Calculated Property | |
Pc | 1925.00 ± 10.00 | kPa | NIST |
Inp | [597.40; 646.00] |
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|
Inp | 597.40 | NIST | |
Inp | 597.40 | NIST | |
Inp | 598.00 | NIST | |
Inp | 645.00 | NIST | |
Inp | 646.00 | NIST | |
S°liquid | [433.80; 433.84] | J/mol×K |
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S°liquid | 433.80 | J/mol×K | NIST |
S°liquid | 433.84 | J/mol×K | NIST |
Tboil | [372.00; 375.00] | K |
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Tboil | 374.12 | K | Isobari... |
Tboil | 374.00 | K | NIST |
Tboil | 372.50 ± 0.50 | K | NIST |
Tboil | 374.14 ± 0.30 | K | NIST |
Tboil | 373.20 ± 1.50 | K | NIST |
Tboil | 375.00 ± 3.00 | K | NIST |
Tboil | 373.00 ± 3.00 | K | NIST |
Tboil | 372.00 ± 3.00 | K | NIST |
Tc | 518.70 ± 0.51 | K | NIST |
Ttriple | 204.93 ± 0.02 | K | NIST |
Vm | 2.14e-04 | m3/mol | Thermod... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,liquid | [311.37; 311.40] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 311.40 | J/mol×K | 298.15 | NIST |
Cp,liquid | 311.37 | J/mol×K | 298.15 | NIST |
ΔfusH | [11.92; 11.92] | kJ/mol | [204.90; 204.93] | ![]() |
ΔfusH | 11.92 | kJ/mol | 204.90 | NIST |
ΔfusH | 11.92 | kJ/mol | 204.90 | NIST |
ΔfusH | 11.92 | kJ/mol | 204.93 | NIST |
ΔfusH | 11.92 | kJ/mol | 204.93 | NIST |
ΔvapH | [31.30; 36.90] | kJ/mol | [327.00; 373.00] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 31 32 33 34 35 36 37 340 360 | ||||
ΔvapH | 33.10 | kJ/mol | 327.00 | NIST |
ΔvapH | 34.60 ± 0.10 | kJ/mol | 332.00 | NIST |
ΔvapH | 36.90 | kJ/mol | 341.50 | NIST |
ΔvapH | 33.10 ± 0.10 | kJ/mol | 351.00 | NIST |
ΔvapH | 36.00 | kJ/mol | 360.00 | NIST |
ΔvapH | 31.30 ± 0.10 | kJ/mol | 373.00 | NIST |
Pvap | 101.30 | kPa | 374.12 | Isobari... |
n0 | 1.37370 | 298.15 | Determi... | |
ρl | [726.05; 763.87] | kg/m3 | [293.15; 328.15] | ![]() |
T(K) Liquid Density (kg/m3) 730 740 750 760 300 310 320 | ||||
ρl | 763.87 | kg/m3 | 293.15 | The mix... |
ρl | 747.95 | kg/m3 | 308.15 | The mix... |
ρl | 742.53 | kg/m3 | 313.15 | The mix... |
ρl | 737.07 | kg/m3 | 318.15 | The mix... |
ρl | 731.57 | kg/m3 | 323.15 | The mix... |
ρl | 726.05 | kg/m3 | 328.15 | The mix... |
ΔfusS | 58.18 | J/mol×K | 204.93 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [273.82; 398.55] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40019e+01 | |||
Coefficient B | -2.95909e+03 | |||
Coefficient C | -5.80520e+01 | |||
Temperature range, min. | 273.82 | |||
Temperature range, max. | 398.55 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 273.82 | Calculated Property |
Pvap | 3.05 | kPa | 287.68 | Calculated Property |
Pvap | 6.35 | kPa | 301.54 | Calculated Property |
Pvap | 12.22 | kPa | 315.40 | Calculated Property |
Pvap | 22.00 | kPa | 329.26 | Calculated Property |
Pvap | 37.39 | kPa | 343.11 | Calculated Property |
Pvap | 60.50 | kPa | 356.97 | Calculated Property |
Pvap | 93.81 | kPa | 370.83 | Calculated Property |
Pvap | 140.15 | kPa | 384.69 | Calculated Property |
Pvap | 202.64 | kPa | 398.55 | Calculated Property |
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