Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2590 | KDB | |
AP | 291.450 | K | KDB |
ΔcH°liquid | [-3338.71; -3335.90] | kJ/mol |
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ΔcH°liquid | -3338.71 ± 0.70 | kJ/mol | NIST |
ΔcH°liquid | -3335.90 ± 0.42 | kJ/mol | NIST |
ΔfG° | 69.96 | kJ/mol | KDB |
Δc,grossH | 3338.04 | kJ/mol | KDB |
Δc,netH | 3118.000 | kJ/mol | KDB |
ΔfH°gas | [-34.00; -31.20] | kJ/mol |
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ΔfH°gas | -31.78 | kJ/mol | KDB |
ΔfH°gas | -32.10 | kJ/mol | NIST |
ΔfH°gas | -31.40 ± 0.50 | kJ/mol | NIST |
ΔfH°gas | -31.80 | kJ/mol | NIST |
ΔfH°gas | -31.20 ± 0.80 | kJ/mol | NIST |
ΔfH°gas | -32.90 ± 1.00 | kJ/mol | NIST |
ΔfH°gas | -33.10 ± 1.30 | kJ/mol | NIST |
ΔfH°gas | -34.00 ± 0.50 | kJ/mol | NIST |
ΔfH°liquid | [-60.80; -57.98] | kJ/mol |
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ΔfH°liquid | -58.24 ± 0.42 | kJ/mol | NIST |
ΔfH°liquid | -57.98 ± 0.76 | kJ/mol | NIST |
ΔfH°liquid | -59.70 ± 1.00 | kJ/mol | NIST |
ΔfH°liquid | -60.80 ± 0.40 | kJ/mol | NIST |
ΔfusH° | 8.91 | kJ/mol | Joback Calculated Property |
ΔvapH° | 26.70 | kJ/mol | NIST |
IE | [8.92; 9.32] | eV |
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IE | 9.04 ± 0.01 | eV | NIST |
IE | 9.04 ± 0.02 | eV | NIST |
IE | 9.04 ± 0.01 | eV | NIST |
IE | 8.92 | eV | NIST |
IE | 9.32 ± 0.03 | eV | NIST |
IE | 9.06 | eV | NIST |
IE | 9.23 ± 0.01 | eV | NIST |
log10WS | -1.77 | Crippen Calculated Property | |
logPoct/wat | 1.973 | Crippen Calculated Property | |
McVol | 77.010 | ml/mol | McGowan Calculated Property |
Pc | 3520.00 | kPa | KDB |
Inp | [499.00; 518.00] |
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|
Inp | 507.60 | NIST | |
Inp | 500.70 | NIST | |
Inp | 500.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 506.00 | NIST | |
Inp | 500.20 | NIST | |
Inp | 507.00 | NIST | |
Inp | 506.80 | NIST | |
Inp | 500.20 | NIST | |
Inp | 500.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 508.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 506.00 | NIST | |
Inp | 511.30 | NIST | |
Inp | 511.10 | NIST | |
Inp | 510.80 | NIST | |
Inp | 510.50 | NIST | |
Inp | 510.20 | NIST | |
Inp | 509.90 | NIST | |
Inp | 507.00 | NIST | |
Inp | 505.90 | NIST | |
Inp | 505.90 | NIST | |
Inp | 505.80 | NIST | |
Inp | 505.80 | NIST | |
Inp | 505.80 | NIST | |
Inp | 505.80 | NIST | |
Inp | Outlier 516.70 | NIST | |
Inp | 511.20 | NIST | |
Inp | 508.40 | NIST | |
Inp | 506.20 | NIST | |
Inp | 504.20 | NIST | |
Inp | 502.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 499.50 | NIST | |
Inp | 499.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 501.00 | NIST | |
Inp | 501.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 502.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 503.00 | NIST | |
Inp | Outlier 516.00 | NIST | |
Inp | 504.00 | NIST | |
Inp | 510.80 | NIST | |
Inp | 510.00 | NIST | |
Inp | 506.60 | NIST | |
Inp | 509.00 | NIST | |
Inp | 504.91 | NIST | |
Inp | 505.09 | NIST | |
Inp | 505.00 | NIST | |
Inp | 510.00 | NIST | |
Inp | 500.70 | NIST | |
Inp | 500.00 | NIST | |
Inp | 503.00 | NIST | |
Inp | Outlier 518.00 | NIST | |
Inp | 509.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 505.00 | NIST | |
Inp | 505.00 | NIST | |
Inp | 508.00 | NIST | |
Inp | 506.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 511.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 506.00 | NIST | |
Inp | 509.00 | NIST | |
Inp | 506.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 509.00 | NIST | |
Inp | 511.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 505.00 | NIST | |
Inp | 512.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 510.00 | NIST | |
Inp | 506.60 | NIST | |
Inp | 507.60 | NIST | |
Inp | 506.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 507.00 | NIST | |
Inp | 511.10 | NIST | |
Inp | 505.80 | NIST | |
Inp | 506.20 | NIST | |
Inp | 499.00 | NIST | |
I | [551.00; 565.00] |
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|
I | 565.00 | NIST | |
I | 551.00 | NIST | |
S°liquid | [256.52; 256.60] | J/mol×K |
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S°liquid | 256.60 | J/mol×K | NIST |
S°liquid | 256.52 | J/mol×K | NIST |
Tboil | [308.95; 310.00] | K |
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Tboil | 309.49 | K | KDB |
Tboil | Outlier 310.00 | K | NIST |
Tboil | 309.50 | K | NIST |
Tboil | 309.00 ± 0.40 | K | NIST |
Tboil | 309.51 ± 0.15 | K | NIST |
Tboil | 309.50 ± 0.15 | K | NIST |
Tboil | 309.51 ± 0.20 | K | NIST |
Tboil | 309.74 ± 0.60 | K | NIST |
Tboil | 309.50 ± 0.20 | K | NIST |
Tboil | 309.50 ± 0.20 | K | NIST |
Tboil | 309.00 ± 0.50 | K | NIST |
Tboil | 308.95 ± 0.30 | K | NIST |
Tboil | 309.45 ± 0.60 | K | NIST |
Tboil | 309.40 ± 0.20 | K | NIST |
Tboil | 309.35 ± 0.40 | K | NIST |
Tboil | 309.40 ± 0.50 | K | NIST |
Tboil | 309.40 ± 0.40 | K | NIST |
Tboil | 309.55 ± 0.30 | K | NIST |
Tboil | 309.00 ± 0.40 | K | NIST |
Tboil | 309.30 ± 0.40 | K | NIST |
Tboil | 309.45 ± 0.15 | K | NIST |
Tboil | 309.54 ± 0.15 | K | NIST |
Tc | 471.00 | K | KDB |
Tfus | [123.90; 132.91] | K |
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Tfus | 132.90 | K | KDB |
Tfus | 132.90 ± 0.01 | K | NIST |
Tfus | 132.90 ± 0.01 | K | NIST |
Tfus | 131.90 ± 1.00 | K | NIST |
Tfus | 132.90 ± 0.06 | K | NIST |
Tfus | 132.90 ± 0.04 | K | NIST |
Tfus | 132.91 ± 0.03 | K | NIST |
Tfus | 132.89 ± 0.20 | K | NIST |
Tfus | 132.89 ± 2.00 | K | NIST |
Tfus | 132.89 ± 0.30 | K | NIST |
Tfus | 132.89 ± 0.30 | K | NIST |
Tfus | Outlier 123.90 ± 2.00 | K | NIST |
Ttriple | [132.93; 132.95] | K |
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Ttriple | 132.93 ± 0.02 | K | NIST |
Ttriple | 132.95 ± 0.02 | K | NIST |
Ttriple | 132.95 ± 0.60 | K | NIST |
Vc | 0.295 | m3/kmol | Joback Calculated Property |
Zra | 0.27 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [112.28; 160.11] | J/mol×K | [317.96; 489.90] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 110 120 130 140 150 160 350 400 450 | ||||
Cp,gas | 112.28 | J/mol×K | 317.96 | Joback Calculated Property |
Cp,gas | 121.16 | J/mol×K | 346.62 | Joback Calculated Property |
Cp,gas | 129.66 | J/mol×K | 375.27 | Joback Calculated Property |
Cp,gas | 137.80 | J/mol×K | 403.93 | Joback Calculated Property |
Cp,gas | 145.57 | J/mol×K | 432.58 | Joback Calculated Property |
Cp,gas | 153.01 | J/mol×K | 461.24 | Joback Calculated Property |
Cp,gas | 160.11 | J/mol×K | 489.90 | Joback Calculated Property |
Cp,liquid | [156.98; 157.00] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 157.00 | J/mol×K | 298.15 | NIST |
Cp,liquid | 156.98 | J/mol×K | 298.15 | NIST |
η | [0.0001682; 0.0033409] | Pa×s | [141.03; 317.96] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 150 200 250 300 | ||||
η | 0.0033409 | Pa×s | 141.03 | Joback Calculated Property |
η | 0.0013197 | Pa×s | 170.52 | Joback Calculated Property |
η | 0.0006855 | Pa×s | 200.01 | Joback Calculated Property |
η | 0.0004214 | Pa×s | 229.50 | Joback Calculated Property |
η | 0.0002894 | Pa×s | 258.98 | Joback Calculated Property |
η | 0.0002146 | Pa×s | 288.47 | Joback Calculated Property |
η | 0.0001682 | Pa×s | 317.96 | Joback Calculated Property |
ΔfusH | [8.35; 8.35] | kJ/mol | [132.93; 133.00] | ![]() |
ΔfusH | 8.35 | kJ/mol | 132.93 | NIST |
ΔfusH | 8.35 | kJ/mol | 132.95 | NIST |
ΔfusH | 8.35 | kJ/mol | 133.00 | NIST |
ΔfusH | 8.35 | kJ/mol | 133.00 | NIST |
ΔvapH | [26.07; 28.80] | kJ/mol | [296.00; 309.50] | ![]() |
ΔvapH | 28.80 | kJ/mol | 296.00 | NIST |
ΔvapH | 28.00 | kJ/mol | 307.50 | NIST |
ΔvapH | 26.07 | kJ/mol | 309.50 | KDB |
n0 | 1.37610 | 298.15 | KDB | |
ρl | 649.00 | kg/m3 | 293.00 | KDB |
ΔfusS | [62.81; 62.83] | J/mol×K | [132.93; 132.95] | ![]() |
ΔfusS | 62.83 | J/mol×K | 132.93 | NIST |
ΔfusS | 62.81 | J/mol×K | 132.95 | NIST |
γ | 0.02 | N/m | 298.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [222.94; 331.03] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42324e+01 | |||
Coefficient B | -2.67642e+03 | |||
Coefficient C | -3.10150e+01 | |||
Temperature range, min. | 222.94 | |||
Temperature range, max. | 331.03 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 | ||||
Pvap | 1.33 | kPa | 222.94 | Calculated Property |
Pvap | 3.03 | kPa | 234.95 | Calculated Property |
Pvap | 6.29 | kPa | 246.96 | Calculated Property |
Pvap | 12.08 | kPa | 258.97 | Calculated Property |
Pvap | 21.74 | kPa | 270.98 | Calculated Property |
Pvap | 36.99 | kPa | 282.99 | Calculated Property |
Pvap | 59.97 | kPa | 295.00 | Calculated Property |
Pvap | 93.23 | kPa | 307.01 | Calculated Property |
Pvap | 139.69 | kPa | 319.02 | Calculated Property |
Pvap | 202.65 | kPa | 331.03 | Calculated Property |
Pvap | [5.97e-06; 3694.47] | kPa | [132.89; 475.37] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.66647e+01 | |||
Coefficient B | -5.30654e+03 | |||
Coefficient C | -7.95545e+00 | |||
Coefficient D | 7.74821e-06 | |||
Temperature range, min. | 132.89 | |||
Temperature range, max. | 475.37 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 300 400 | ||||
Pvap | 5.97e-06 | kPa | 132.89 | Calculated Property |
Pvap | 6.39e-03 | kPa | 170.94 | Calculated Property |
Pvap | 0.41 | kPa | 209.00 | Calculated Property |
Pvap | 6.21 | kPa | 247.05 | Calculated Property |
Pvap | 40.89 | kPa | 285.10 | Calculated Property |
Pvap | 161.63 | kPa | 323.16 | Calculated Property |
Pvap | 460.08 | kPa | 361.21 | Calculated Property |
Pvap | 1052.55 | kPa | 399.26 | Calculated Property |
Pvap | 2075.40 | kPa | 437.32 | Calculated Property |
Pvap | 3694.47 | kPa | 475.37 | Calculated Property |
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