Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2440 | KDB | |
PAff | 808.60 | kJ/mol | NIST |
BasG | 781.20 | kJ/mol | NIST |
ΔcH°gas | -2107.40 ± 0.63 | kJ/mol | NIST |
μ | 1.20 | debye | KDB |
ΔfG° | -117.70 | kJ/mol | KDB |
ΔfH°gas | [-216.60; -216.40] | kJ/mol |
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ΔfH°gas | -216.60 | kJ/mol | KDB |
ΔfH°gas | -216.40 ± 0.67 | kJ/mol | NIST |
ΔfusH° | 4.71 | kJ/mol | Joback Calculated Property |
ΔvapH° | 24.68 | kJ/mol | Joback Calculated Property |
IE | [9.50; 9.86] | eV |
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IE | 9.72 ± 0.07 | eV | NIST |
IE | 9.72 ± 0.07 | eV | NIST |
IE | 9.86 | eV | NIST |
IE | 9.72 | eV | NIST |
IE | 9.50 | eV | NIST |
IE | 9.60 ± 0.10 | eV | NIST |
IE | 9.72 | eV | NIST |
IE | 9.81 | eV | NIST |
log10WS | -0.17 | Crippen Calculated Property | |
logPoct/wat | 0.653 | Crippen Calculated Property | |
McVol | 59.000 | ml/mol | McGowan Calculated Property |
NFPA Fire | 4 | KDB | |
NFPA Health | 2 | KDB | |
Pc | [4361.00; 4688.00] | kPa |
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Pc | 4400.00 | kPa | KDB |
Pc | 4361.00 ± 50.66 | kPa | NIST |
Pc | 4400.00 ± 40.53 | kPa | NIST |
Pc | 4688.00 ± 303.98 | kPa | NIST |
ρc | [272.17; 307.03] | kg/m3 |
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ρc | 272.17 ± 1.80 | kg/m3 | NIST |
ρc | 307.03 ± 19.83 | kg/m3 | NIST |
Inp | [419.00; 421.00] |
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|
Inp | 421.00 | NIST | |
Inp | 421.00 | NIST | |
Inp | 419.00 | NIST | |
Inp | 421.00 | NIST | |
Tboil | [279.75; 312.10] | K |
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Tboil | 280.60 | K | KDB |
Tboil | 283.20 | K | NIST |
Tboil | 312.10 ± 0.40 | K | NIST |
Tboil | 279.75 ± 0.60 | K | NIST |
Tc | [437.80; 441.60] | K |
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Tc | 437.80 | K | KDB |
Tc | 438.03 ± 1.00 | K | NIST |
Tc | 437.80 ± 0.30 | K | NIST |
Tc | 437.90 ± 0.30 | K | NIST |
Tc | 441.60 ± 4.00 | K | NIST |
Tc | 440.90 ± 3.00 | K | NIST |
Tfus | 160.00 | K | KDB |
Vc | [0.221; 0.222] | m3/kmol |
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Vc | 0.221 | m3/kmol | KDB |
Vc | 0.222 ± 0.003 | m3/kmol | NIST |
Zc | 0.2671360 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [88.06; 119.18] | J/mol×K | [290.46; 452.73] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 85 90 95 100 105 110 115 120 300 350 400 450 | ||||
Cp,gas | 88.06 | J/mol×K | 290.46 | Joback Calculated Property |
Cp,gas | 93.47 | J/mol×K | 317.50 | Joback Calculated Property |
Cp,gas | 98.79 | J/mol×K | 344.55 | Joback Calculated Property |
Cp,gas | 104.03 | J/mol×K | 371.59 | Joback Calculated Property |
Cp,gas | 109.18 | J/mol×K | 398.64 | Joback Calculated Property |
Cp,gas | 114.23 | J/mol×K | 425.68 | Joback Calculated Property |
Cp,gas | 119.18 | J/mol×K | 452.73 | Joback Calculated Property |
η | [0.0001721; 0.0019793] | Pa×s | [145.80; 290.46] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 150 200 250 | ||||
η | 0.0019793 | Pa×s | 145.80 | Joback Calculated Property |
η | 0.0009870 | Pa×s | 169.91 | Joback Calculated Property |
η | 0.0005850 | Pa×s | 194.02 | Joback Calculated Property |
η | 0.0003893 | Pa×s | 218.13 | Joback Calculated Property |
η | 0.0002809 | Pa×s | 242.24 | Joback Calculated Property |
η | 0.0002151 | Pa×s | 266.35 | Joback Calculated Property |
η | 0.0001721 | Pa×s | 290.46 | Joback Calculated Property |
ΔvapH | [24.69; 37.10] | kJ/mol | [231.00; 359.50] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 24 26 28 30 32 34 36 38 250 300 350 | ||||
ΔvapH | 26.30 | kJ/mol | 231.00 | NIST |
ΔvapH | 37.00 | kJ/mol | 257.50 | NIST |
ΔvapH | 24.69 | kJ/mol | 280.80 | KDB |
ΔvapH | 30.10 | kJ/mol | 357.00 | NIST |
ΔvapH | 37.10 | kJ/mol | 359.50 | NIST |
ρl | 700.00 | kg/m3 | 293.00 | KDB |
γ | 0.02 | N/m | 298.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 3537.71] | kPa | [217.94; 437.80] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.23480e+01 | |||
Coefficient B | -1.40486e+03 | |||
Coefficient C | -1.01451e+02 | |||
Temperature range, min. | 217.94 | |||
Temperature range, max. | 437.80 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 250 300 350 400 | ||||
Pvap | 1.33 | kPa | 217.94 | Calculated Property |
Pvap | 10.79 | kPa | 242.37 | Calculated Property |
Pvap | 47.07 | kPa | 266.80 | Calculated Property |
Pvap | 140.51 | kPa | 291.23 | Calculated Property |
Pvap | 326.86 | kPa | 315.66 | Calculated Property |
Pvap | 639.65 | kPa | 340.08 | Calculated Property |
Pvap | 1105.02 | kPa | 364.51 | Calculated Property |
Pvap | 1739.59 | kPa | 388.94 | Calculated Property |
Pvap | 2550.68 | kPa | 413.37 | Calculated Property |
Pvap | 3537.71 | kPa | 437.80 | Calculated Property |
Pvap | [3.35e-04; 4647.74] | kPa | [160.00; 437.80] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.43488e+02 | |||
Coefficient B | -1.12818e+04 | |||
Coefficient C | -3.58975e+01 | |||
Coefficient D | 4.71928e-05 | |||
Temperature range, min. | 160.00 | |||
Temperature range, max. | 437.80 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 200 300 400 | ||||
Pvap | 3.35e-04 | kPa | 160.00 | Calculated Property |
Pvap | 0.09 | kPa | 190.87 | Calculated Property |
Pvap | 2.80 | kPa | 221.73 | Calculated Property |
Pvap | 26.01 | kPa | 252.60 | Calculated Property |
Pvap | 117.24 | kPa | 283.47 | Calculated Property |
Pvap | 341.34 | kPa | 314.33 | Calculated Property |
Pvap | 765.38 | kPa | 345.20 | Calculated Property |
Pvap | 1479.02 | kPa | 376.07 | Calculated Property |
Pvap | 2653.25 | kPa | 406.93 | Calculated Property |
Pvap | 4647.74 | kPa | 437.80 | Calculated Property |
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