Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2320 | KDB | |
ΔcH°liquid | -1095.80 ± 8.40 | kJ/mol | NIST |
μ | 0.00 | debye | KDB |
ΔfG° | 26.60 | kJ/mol | KDB |
ΔfH°gas | [-1.00; 4.19] | kJ/mol | |
ΔfH°gas | 4.19 | kJ/mol | KDB |
ΔfH°gas | -1.00 ± 2.00 | kJ/mol | NIST |
ΔfH°gas | 1.70 | kJ/mol | NIST |
ΔfH°liquid | [-30.00; -14.34] | kJ/mol | |
ΔfH°liquid | -30.00 ± 2.20 | kJ/mol | NIST |
ΔfH°liquid | -14.34 | kJ/mol | NIST |
ΔfusH° | 9.53 | kJ/mol | Joback Calculated Property |
ΔvapH° | [29.47; 30.00] | kJ/mol | |
ΔvapH° | 30.00 ± 1.00 | kJ/mol | NIST |
ΔvapH° | 29.47 | kJ/mol | NIST |
IE | [9.60; 11.92] | eV | |
IE | 9.64 ± 0.02 | eV | NIST |
IE | 9.64 | eV | NIST |
IE | 9.69 | eV | NIST |
IE | 9.60 | eV | NIST |
IE | 9.66 ± 0.03 | eV | NIST |
IE | 9.64 ± 0.02 | eV | NIST |
IE | 9.63 | eV | NIST |
IE | 9.80 | eV | NIST |
IE | 9.80 | eV | NIST |
IE | Outlier 11.92 | eV | NIST |
IE | 9.72 | eV | NIST |
log10WS | -1.81 | Crippen Calculated Property | |
logPoct/wat | 1.935 | Crippen Calculated Property | |
McVol | 59.220 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
NFPA Health | 2 | KDB | |
NFPA Safety | 2 | KDB | |
Pc | 5510.00 | kPa | KDB |
Inp | [528.00; 596.00] | ||
Inp | 558.00 | NIST | |
Inp | 559.00 | NIST | |
Inp | 557.00 | NIST | |
Inp | 555.00 | NIST | |
Inp | 559.00 | NIST | |
Inp | Outlier 528.00 | NIST | |
Inp | 551.00 | NIST | |
Inp | 551.00 | NIST | |
Inp | Outlier 596.00 | NIST | |
Inp | 567.00 | NIST | |
Inp | 558.00 | NIST | |
Inp | 551.00 | NIST | |
I | [863.21; 870.00] | ||
I | 867.61 | NIST | |
I | 866.47 | NIST | |
I | 863.21 | NIST | |
I | 870.00 | NIST | |
I | 870.00 | NIST | |
Tboil | [320.45; 322.70] | K | |
Tboil | 321.88 | K | KDB |
Tboil | 320.70 | K | NIST |
Tboil | 320.45 ± 0.25 | K | NIST |
Tboil | 320.50 ± 0.40 | K | NIST |
Tboil | 321.40 ± 0.60 | K | NIST |
Tboil | 321.40 ± 0.70 | K | NIST |
Tboil | 322.70 ± 2.00 | K | NIST |
Tc | 516.50 | K | KDB |
Tfus | [223.00; 223.30] | K | |
Tfus | 223.30 | K | KDB |
Tfus | 223.00 ± 0.10 | K | NIST |
Vc | 0.226 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [67.02; 84.99] | J/mol×K | [324.18; 517.06] | |
T(K) Ideal gas heat capacity (J/mol×K) 70 75 80 85 350 400 450 500 | ||||
Cp,gas | 67.02 | J/mol×K | 324.18 | Joback Calculated Property |
Cp,gas | 70.61 | J/mol×K | 356.33 | Joback Calculated Property |
Cp,gas | 73.95 | J/mol×K | 388.47 | Joback Calculated Property |
Cp,gas | 77.04 | J/mol×K | 420.62 | Joback Calculated Property |
Cp,gas | 79.90 | J/mol×K | 452.76 | Joback Calculated Property |
Cp,gas | 82.55 | J/mol×K | 484.91 | Joback Calculated Property |
Cp,gas | 84.99 | J/mol×K | 517.06 | Joback Calculated Property |
Cp,liquid | [112.08; 115.07] | J/mol×K | [268.30; 309.14] | |
T(K) Liquid phase heat capacity (J/mol×K) 112 112.5 113 113.5 114 114.5 115 280 300 | ||||
Cp,liquid | 113.08 | J/mol×K | 268.30 | Heat ca... |
Cp,liquid | 112.74 | J/mol×K | 268.30 | Heat ca... |
Cp,liquid | 112.41 | J/mol×K | 268.30 | Heat ca... |
Cp,liquid | 112.08 | J/mol×K | 268.30 | Heat ca... |
Cp,liquid | 112.99 | J/mol×K | 278.51 | Heat ca... |
Cp,liquid | 112.83 | J/mol×K | 278.51 | Heat ca... |
Cp,liquid | 112.41 | J/mol×K | 278.51 | Heat ca... |
Cp,liquid | 112.08 | J/mol×K | 278.51 | Heat ca... |
Cp,liquid | 113.00 | J/mol×K | 288.00 | NIST |
Cp,liquid | 113.41 | J/mol×K | 288.72 | Heat ca... |
Cp,liquid | 113.49 | J/mol×K | 288.72 | Heat ca... |
Cp,liquid | 112.58 | J/mol×K | 288.72 | Heat ca... |
Cp,liquid | 112.91 | J/mol×K | 288.72 | Heat ca... |
Cp,liquid | 114.24 | J/mol×K | 298.93 | Heat ca... |
Cp,liquid | 113.99 | J/mol×K | 298.93 | Heat ca... |
Cp,liquid | 113.41 | J/mol×K | 298.93 | Heat ca... |
Cp,liquid | 113.82 | J/mol×K | 298.93 | Heat ca... |
Cp,liquid | 115.07 | J/mol×K | 309.14 | Heat ca... |
Cp,liquid | 114.49 | J/mol×K | 309.14 | Heat ca... |
Cp,liquid | 114.16 | J/mol×K | 309.14 | Heat ca... |
Cp,liquid | 113.66 | J/mol×K | 309.14 | Heat ca... |
η | [0.0002698; 0.0028927] | Pa×s | [167.06; 324.18] | |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 200 250 300 | ||||
η | 0.0028927 | Pa×s | 167.06 | Joback Calculated Property |
η | 0.0014903 | Pa×s | 193.25 | Joback Calculated Property |
η | 0.0008995 | Pa×s | 219.43 | Joback Calculated Property |
η | 0.0006046 | Pa×s | 245.62 | Joback Calculated Property |
η | 0.0004387 | Pa×s | 271.81 | Joback Calculated Property |
η | 0.0003368 | Pa×s | 297.99 | Joback Calculated Property |
η | 0.0002698 | Pa×s | 324.18 | Joback Calculated Property |
ΔvapH | [29.00; 31.40] | kJ/mol | [293.00; 397.00] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 29 29.5 30 30.5 31 31.5 300 350 | ||||
ΔvapH | 30.40 | kJ/mol | 293.00 | NIST |
ΔvapH | 30.10 | kJ/mol | 296.00 | NIST |
ΔvapH | 31.40 | kJ/mol | 296.50 | NIST |
ΔvapH | 30.30 | kJ/mol | 321.50 | KDB |
ΔvapH | 29.00 | kJ/mol | 397.00 | NIST |
Pvap | [53.33; 269.90] | kPa | [303.15; 353.15] | |
Pvap | 53.33 | kPa | 303.15 | Phase E... |
Pvap | 269.90 | kPa | 353.15 | Phase E... |
ρl | 1255.00 | kg/m3 | 293.00 | KDB |
γ | 0.02 | N/m | 293.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.52; 6698.23] | kPa | [223.35; 516.50] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.50408e+01 | |||
Coefficient B | -3.02933e+03 | |||
Coefficient C | -3.03460e+01 | |||
Temperature range, min. | 223.35 | |||
Temperature range, max. | 516.50 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 7000 300 400 500 | ||||
Pvap | 0.52 | kPa | 223.35 | Calculated Property |
Pvap | 5.01 | kPa | 255.92 | Calculated Property |
Pvap | 27.28 | kPa | 288.49 | Calculated Property |
Pvap | 101.57 | kPa | 321.07 | Calculated Property |
Pvap | 290.20 | kPa | 353.64 | Calculated Property |
Pvap | 684.19 | kPa | 386.21 | Calculated Property |
Pvap | 1396.96 | kPa | 418.78 | Calculated Property |
Pvap | 2554.01 | kPa | 451.36 | Calculated Property |
Pvap | 4281.80 | kPa | 483.93 | Calculated Property |
Pvap | 6698.23 | kPa | 516.50 | Calculated Property |
Pvap | [0.62; 5421.34] | kPa | [223.35; 513.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.76830e+01 | |||
Coefficient B | -6.29447e+03 | |||
Coefficient C | -1.11957e+01 | |||
Coefficient D | 1.15854e-05 | |||
Temperature range, min. | 223.35 | |||
Temperature range, max. | 513.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 | ||||
Pvap | 0.62 | kPa | 223.35 | Calculated Property |
Pvap | 5.73 | kPa | 255.53 | Calculated Property |
Pvap | 29.23 | kPa | 287.72 | Calculated Property |
Pvap | 101.06 | kPa | 319.90 | Calculated Property |
Pvap | 268.16 | kPa | 352.08 | Calculated Property |
Pvap | 592.41 | kPa | 384.27 | Calculated Property |
Pvap | 1150.75 | kPa | 416.45 | Calculated Property |
Pvap | 2041.81 | kPa | 448.63 | Calculated Property |
Pvap | 3400.32 | kPa | 480.82 | Calculated Property |
Pvap | 5421.34 | kPa | 513.00 | Calculated Property |
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