Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3030 | KDB | |
AP | 341.150 | K | KDB |
ΔcH°liquid | -6121.60 ± 1.50 | kJ/mol | NIST |
ΔfG° | 34.33 | kJ/mol | KDB |
Δc,grossH | 6121.61 | kJ/mol | KDB |
Δc,netH | 5681.496 | kJ/mol | KDB |
ΔfH°gas | -237.40 | kJ/mol | KDB |
ΔfusH° | 4.24 | kJ/mol | Joback Calculated Property |
ΔvapH° | 41.20 | kJ/mol | NIST |
log10WS | -3.11 | Crippen Calculated Property | |
logPoct/wat | 3.469 | Crippen Calculated Property | |
McVol | 137.670 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
Pc | [2740.00; 2741.00] | kPa | |
Pc | 2740.00 | kPa | KDB |
Pc | 2740.00 ± 40.00 | kPa | NIST |
Pc | 2741.00 ± 20.00 | kPa | NIST |
Inp | [844.00; 862.00] | ||
Inp | 856.00 | NIST | |
Inp | 851.70 | NIST | |
Inp | 857.10 | NIST | |
Inp | 847.70 | NIST | |
Inp | 847.80 | NIST | |
Inp | 855.00 | NIST | |
Inp | 855.80 | NIST | |
Inp | 852.00 | NIST | |
Inp | 858.00 | NIST | |
Inp | 852.70 | NIST | |
Inp | 856.00 | NIST | |
Inp | 847.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 853.00 | NIST | |
Inp | Outlier 862.00 | NIST | |
Inp | 854.00 | NIST | |
Inp | Outlier 844.00 | NIST | |
Inp | 852.00 | NIST | |
Inp | 849.00 | NIST | |
Inp | 852.00 | NIST | |
Inp | 855.00 | NIST | |
Inp | 856.00 | NIST | |
Inp | 855.00 | NIST | |
Inp | 852.00 | NIST | |
S°liquid | 334.80 | J/mol×K | NIST |
Tboil | [413.39; 413.50] | K | |
Tboil | 413.44 | K | KDB |
Tboil | Outlier 413.50 | K | NIST |
Tboil | 413.42 ± 0.20 | K | NIST |
Tboil | 413.40 ± 0.40 | K | NIST |
Tboil | 413.42 ± 0.03 | K | NIST |
Tboil | 413.41 ± 0.10 | K | NIST |
Tboil | 413.39 ± 0.20 | K | NIST |
Tc | [607.50; 607.55] | K | |
Tc | 607.50 | K | KDB |
Tc | 607.50 ± 0.50 | K | NIST |
Tc | 607.55 ± 0.20 | K | NIST |
Tfus | [261.52; 263.30] | K | |
Tfus | 263.30 | K | KDB |
Tfus | 263.15 ± 0.30 | K | NIST |
Tfus | 263.11 ± 0.10 | K | NIST |
Tfus | 263.25 ± 0.08 | K | NIST |
Tfus | 263.15 ± 0.50 | K | NIST |
Tfus | Outlier 261.52 ± 0.20 | K | NIST |
Tfus | 263.25 ± 0.10 | K | NIST |
Ttriple | 263.40 ± 0.02 | K | NIST |
Vc | 0.517 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [275.15; 365.94] | J/mol×K | [398.86; 583.86] | |
Cp,gas | 275.15 | J/mol×K | 398.86 | Joback Calculated Property |
Cp,gas | 292.52 | J/mol×K | 429.69 | Joback Calculated Property |
Cp,gas | 308.94 | J/mol×K | 460.53 | Joback Calculated Property |
Cp,gas | 324.44 | J/mol×K | 491.36 | Joback Calculated Property |
Cp,gas | 339.09 | J/mol×K | 522.19 | Joback Calculated Property |
Cp,gas | 352.90 | J/mol×K | 553.03 | Joback Calculated Property |
Cp,gas | 365.94 | J/mol×K | 583.86 | Joback Calculated Property |
Cp,liquid | 271.50 | J/mol×K | 298.15 | NIST |
η | [0.0002923; 0.0205234] | Pa×s | [196.03; 398.86] | |
η | 0.0205234 | Pa×s | 196.03 | Joback Calculated Property |
η | 0.0060005 | Pa×s | 229.84 | Joback Calculated Property |
η | 0.0024048 | Pa×s | 263.64 | Joback Calculated Property |
η | 0.0011864 | Pa×s | 297.44 | Joback Calculated Property |
η | 0.0006761 | Pa×s | 331.25 | Joback Calculated Property |
η | 0.0004276 | Pa×s | 365.06 | Joback Calculated Property |
η | 0.0002923 | Pa×s | 398.86 | Joback Calculated Property |
ΔfusH | [2.33; 7.33] | kJ/mol | [174.50; 263.40] | |
ΔfusH | 7.33 | kJ/mol | 174.50 | NIST |
ΔfusH | 2.33 | kJ/mol | 263.40 | NIST |
ΔfusH | 2.33 | kJ/mol | 263.40 | NIST |
ΔvapH | [35.27; 39.20] | kJ/mol | [371.50; 413.40] | |
ΔvapH | 39.20 | kJ/mol | 371.50 | NIST |
ΔvapH | 35.27 | kJ/mol | 413.40 | KDB |
n0 | 1.42140 | 298.15 | KDB | |
ρl | 757.00 | kg/m3 | 293.00 | KDB |
ΔfusS | [8.90; 42.00] | J/mol×K | [174.50; 263.40] | |
ΔfusS | 42.00 | J/mol×K | 174.50 | NIST |
ΔfusS | 8.90 | J/mol×K | 263.40 | NIST |
γ | 0.02 | N/m | 298.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [299.10; 442.41] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.39261e+01 | |||
Coefficient B | -3.35151e+03 | |||
Coefficient C | -5.33610e+01 | |||
Temperature range, min. | 299.10 | |||
Temperature range, max. | 442.41 | |||
Pvap | 1.33 | kPa | 299.10 | Calculated Property |
Pvap | 3.06 | kPa | 315.02 | Calculated Property |
Pvap | 6.37 | kPa | 330.95 | Calculated Property |
Pvap | 12.27 | kPa | 346.87 | Calculated Property |
Pvap | 22.08 | kPa | 362.79 | Calculated Property |
Pvap | 37.52 | kPa | 378.72 | Calculated Property |
Pvap | 60.68 | kPa | 394.64 | Calculated Property |
Pvap | 94.01 | kPa | 410.56 | Calculated Property |
Pvap | 140.30 | kPa | 426.49 | Calculated Property |
Pvap | 202.64 | kPa | 442.41 | Calculated Property |
Pvap | [0.13; 2786.82] | kPa | [263.26; 610.85] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.97422e+01 | |||
Coefficient B | -7.54526e+03 | |||
Coefficient C | -9.60312e+00 | |||
Coefficient D | 5.74899e-06 | |||
Temperature range, min. | 263.26 | |||
Temperature range, max. | 610.85 | |||
Pvap | 0.13 | kPa | 263.26 | Calculated Property |
Pvap | 1.55 | kPa | 301.88 | Calculated Property |
Pvap | 9.58 | kPa | 340.50 | Calculated Property |
Pvap | 38.27 | kPa | 379.12 | Calculated Property |
Pvap | 113.29 | kPa | 417.74 | Calculated Property |
Pvap | 271.35 | kPa | 456.37 | Calculated Property |
Pvap | 558.08 | kPa | 494.99 | Calculated Property |
Pvap | 1027.29 | kPa | 533.61 | Calculated Property |
Pvap | 1743.25 | kPa | 572.23 | Calculated Property |
Pvap | 2786.82 | kPa | 610.85 | Calculated Property |
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