Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2920 | KDB | |
PAff | 899.00 | kJ/mol | NIST |
Tig | 703.15 | K | KDB |
BasG | 864.50 | kJ/mol | NIST |
ΔcH°liquid | [-1094.00; -1060.80] | kJ/mol |
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ΔcH°liquid | -1060.80 ± 0.40 | kJ/mol | NIST |
ΔcH°liquid | -1060.80 ± 0.40 | kJ/mol | NIST |
ΔcH°liquid | -1094.00 | kJ/mol | NIST |
ΔcH°liquid | -1075.00 | kJ/mol | NIST |
μ | 1.30 | debye | KDB |
LFL | 4.30 | % in Air | KDB |
UFL | 21.00 | % in Air | KDB |
ΔfG° | 32.28 | kJ/mol | KDB |
ΔfH°gas | [-23.50; -12.20] | kJ/mol |
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ΔfH°gas | -23.03 | kJ/mol | KDB |
ΔfH°gas | -23.50 | kJ/mol | NIST |
ΔfH°gas | -12.20 | kJ/mol | NIST |
ΔfH°liquid | [-47.30; -36.00] | kJ/mol |
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ΔfH°liquid | -47.30 ± 0.46 | kJ/mol | NIST |
ΔfH°liquid | -47.30 ± 0.46 | kJ/mol | NIST |
ΔfH°liquid | -36.00 | kJ/mol | NIST |
ΔfusH° | 3.54 | kJ/mol | Joback Calculated Property |
ΔvapH° | 23.85 | kJ/mol | NIST |
IE | [8.80; 9.65] | eV |
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IE | 8.90 ± 0.10 | eV | NIST |
IE | 8.90 | eV | NIST |
IE | 9.45 | eV | NIST |
IE | 8.90 ± 0.10 | eV | NIST |
IE | 9.08 | eV | NIST |
IE | 8.80 ± 0.02 | eV | NIST |
IE | 9.65 | eV | NIST |
IE | 9.00 | eV | NIST |
IE | 9.58 | eV | NIST |
IE | 9.58 | eV | NIST |
IE | 9.64 | eV | NIST |
IE | 9.64 | eV | NIST |
IE | 9.65 | eV | NIST |
log10WS | 0.32 | Crippen Calculated Property | |
logPoct/wat | -0.425 | Crippen Calculated Property | |
McVol | 34.930 | ml/mol | McGowan Calculated Property |
NFPA Fire | 4 | KDB | |
NFPA Health | 3 | KDB | |
Pc | [7457.52; 7650.00] | kPa |
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Pc | 7614.00 | kPa | KDB |
Pc | 7650.00 ± 100.00 | kPa | NIST |
Pc | 7614.00 ± 4.00 | kPa | NIST |
Pc | 7457.52 ± 60.79 | kPa | NIST |
Inp | [305.00; 380.00] |
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|
Inp | 305.00 | NIST | |
Inp | 380.00 | NIST | |
Inp | 328.00 | NIST | |
S°liquid | 150.20 | J/mol×K | NIST |
Tboil | [266.65; 267.05] | K |
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Tboil | 266.83 | K | KDB |
Tboil | 266.80 | K | NIST |
Tboil | 266.65 ± 0.50 | K | NIST |
Tboil | 266.65 ± 1.00 | K | NIST |
Tboil | 266.65 ± 1.00 | K | NIST |
Tboil | 266.95 ± 0.20 | K | NIST |
Tboil | 267.05 ± 0.20 | K | NIST |
Tboil | 266.70 ± 0.30 | K | NIST |
Tboil | 266.65 ± 1.00 | K | NIST |
Tc | [430.05; 430.85] | K |
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Tc | 430.70 | K | KDB |
Tc | 430.85 ± 0.50 | K | NIST |
Tc | 430.70 ± 0.20 | K | NIST |
Tc | 430.05 ± 0.70 | K | NIST |
Tfus | [179.70; 180.05] | K |
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Tfus | 179.71 | K | KDB |
Tfus | 180.05 ± 0.40 | K | NIST |
Tfus | 180.05 ± 0.30 | K | NIST |
Tfus | 179.70 ± 0.07 | K | NIST |
Ttriple | 179.70 ± 0.07 | K | NIST |
Vc | [0.139; 0.154] | m3/kmol |
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Vc | 0.154 | m3/kmol | KDB |
Vc | 0.139 ± 0.001 | m3/kmol | NIST |
Zc | 0.3284960 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [49.72; 69.45] | J/mol×K | [294.81; 475.82] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 50 55 60 65 70 300 350 400 450 | ||||
Cp,gas | 49.72 | J/mol×K | 294.81 | Joback Calculated Property |
Cp,gas | 53.29 | J/mol×K | 324.98 | Joback Calculated Property |
Cp,gas | 56.74 | J/mol×K | 355.15 | Joback Calculated Property |
Cp,gas | 60.08 | J/mol×K | 385.32 | Joback Calculated Property |
Cp,gas | 63.31 | J/mol×K | 415.48 | Joback Calculated Property |
Cp,gas | 66.43 | J/mol×K | 445.65 | Joback Calculated Property |
Cp,gas | 69.45 | J/mol×K | 475.82 | Joback Calculated Property |
Cp,liquid | 101.80 | J/mol×K | 259.28 | NIST |
ΔfusH | [6.13; 6.13] | kJ/mol | [179.70; 179.70] | ![]() |
ΔfusH | 6.13 | kJ/mol | 179.70 | NIST |
ΔfusH | 6.13 | kJ/mol | 179.70 | NIST |
ΔvapH | [23.50; 27.40] | kJ/mol | [228.50; 401.50] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 24 25 26 27 250 300 350 400 | ||||
ΔvapH | 27.40 | kJ/mol | 228.50 | NIST |
ΔvapH | 27.20 | kJ/mol | 248.00 | NIST |
ΔvapH | 25.98 | kJ/mol | 266.80 | KDB |
ΔvapH | 25.60 | kJ/mol | 266.80 | NIST |
ΔvapH | 25.81 | kJ/mol | 266.84 | NIST |
ΔvapH | 25.81 ± 0.13 | kJ/mol | 266.84 | NIST |
ΔvapH | 26.10 | kJ/mol | 296.00 | NIST |
ΔvapH | 24.80 | kJ/mol | 350.00 | NIST |
ΔvapH | 23.50 | kJ/mol | 401.50 | NIST |
ρl | 703.00 | kg/m3 | 260.00 | KDB |
ΔfusS | 34.13 | J/mol×K | 179.70 | NIST |
γ | 0.02 | N/m | 293.20 | KDB |
ΔvapS | 96.73 | J/mol×K | 266.84 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.18; 3767.28] | kPa | [179.69; 390.05] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.49438e+01 | |||
Coefficient B | -2.36156e+03 | |||
Coefficient C | -3.80880e+01 | |||
Temperature range, min. | 179.69 | |||
Temperature range, max. | 390.05 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 250 300 350 | ||||
Pvap | 0.18 | kPa | 179.69 | Calculated Property |
Pvap | 1.88 | kPa | 203.06 | Calculated Property |
Pvap | 11.08 | kPa | 226.44 | Calculated Property |
Pvap | 44.25 | kPa | 249.81 | Calculated Property |
Pvap | 134.11 | kPa | 273.18 | Calculated Property |
Pvap | 332.64 | kPa | 296.56 | Calculated Property |
Pvap | 709.66 | kPa | 319.93 | Calculated Property |
Pvap | 1348.10 | kPa | 343.30 | Calculated Property |
Pvap | 2337.48 | kPa | 366.68 | Calculated Property |
Pvap | 3767.28 | kPa | 390.05 | Calculated Property |
Pvap | [0.18; 7441.23] | kPa | [179.69; 430.05] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.39982e+01 | |||
Coefficient B | -5.25016e+03 | |||
Coefficient C | -9.02366e+00 | |||
Coefficient D | 9.96726e-06 | |||
Temperature range, min. | 179.69 | |||
Temperature range, max. | 430.05 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 7000 8000 200 300 400 | ||||
Pvap | 0.18 | kPa | 179.69 | Calculated Property |
Pvap | 2.67 | kPa | 207.51 | Calculated Property |
Pvap | 19.34 | kPa | 235.33 | Calculated Property |
Pvap | 85.68 | kPa | 263.14 | Calculated Property |
Pvap | 271.76 | kPa | 290.96 | Calculated Property |
Pvap | 681.75 | kPa | 318.78 | Calculated Property |
Pvap | 1445.25 | kPa | 346.60 | Calculated Property |
Pvap | 2710.10 | kPa | 374.41 | Calculated Property |
Pvap | 4643.16 | kPa | 402.23 | Calculated Property |
Pvap | 7441.23 | kPa | 430.05 | Calculated Property |
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