Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2440 | KDB | |
PAff | 755.90 | kJ/mol | NIST |
BasG | 726.60 | kJ/mol | NIST |
ΔcH°liquid | [-3126.00; -3103.90] | kJ/mol | |
ΔcH°liquid | -3103.90 ± 1.20 | kJ/mol | NIST |
ΔcH°liquid | -3126.00 | kJ/mol | NIST |
μ | 1.40 | debye | KDB |
ΔfG° | -69.08 | kJ/mol | KDB |
ΔfH°gas | -116.60 | kJ/mol | KDB |
ΔfH°liquid | -150.80 ± 1.40 | kJ/mol | NIST |
ΔfusH° | 8.42 | kJ/mol | Joback Calculated Property |
ΔvapH° | [34.50; 34.68] | kJ/mol | |
ΔvapH° | 34.68 | kJ/mol | NIST |
ΔvapH° | 34.50 | kJ/mol | NIST |
ΔvapH° | 34.53 | kJ/mol | NIST |
ΔvapH° | 34.60 | kJ/mol | NIST |
IE | [9.11; 9.75] | eV | |
IE | 9.20 ± 0.01 | eV | NIST |
IE | 9.20 | eV | NIST |
IE | 9.20 | eV | NIST |
IE | 9.22 | eV | NIST |
IE | 9.17 | eV | NIST |
IE | Outlier 9.75 | eV | NIST |
IE | 9.11 | eV | NIST |
IE | 9.20 | eV | NIST |
IE | 9.20 | eV | NIST |
IE | 9.18 | eV | NIST |
IE | 9.21 ± 0.04 | eV | NIST |
IE | 9.20 ± 0.01 | eV | NIST |
IE | 9.20 | eV | NIST |
IE | 9.20 ± 0.01 | eV | NIST |
IE | 9.22 | eV | NIST |
IE | 9.37 | eV | NIST |
IE | 9.19 | eV | NIST |
IE | 9.35 ± 0.03 | eV | NIST |
log10WS | [-1.80; -1.80] | ||
log10WS | -1.80 | Aq. Sol... | |
log10WS | -1.80 | Estimat... | |
logPoct/wat | 1.826 | Crippen Calculated Property | |
McVol | 73.410 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
NFPA Health | 2 | KDB | |
NFPA Safety | 3 | KDB | |
Pc | [4521.23; 4551.00] | kPa | |
Pc | 4551.00 | kPa | KDB |
Pc | 4550.50 ± 5.06 | kPa | NIST |
Pc | 4521.23 ± 39.99 | kPa | NIST |
Inp | [643.00; 684.00] | ||
Inp | 664.90 | NIST | |
Inp | 671.50 | NIST | |
Inp | 672.60 | NIST | |
Inp | 663.20 | NIST | |
Inp | 668.00 | NIST | |
Inp | 673.90 | NIST | |
Inp | 664.60 | NIST | |
Inp | 666.00 | NIST | |
Inp | 680.00 | NIST | |
Inp | 680.00 | NIST | |
Inp | 671.00 | NIST | |
Inp | 651.30 | NIST | |
Inp | Outlier 643.00 | NIST | |
Inp | 681.00 | NIST | |
Inp | 664.10 | NIST | |
Inp | 674.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 659.40 | NIST | |
Inp | 654.40 | NIST | |
Inp | 664.00 | NIST | |
Inp | 664.00 | NIST | |
Inp | 663.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 681.00 | NIST | |
Inp | 684.00 | NIST | |
I | [992.00; 996.00] | ||
I | 996.00 | NIST | |
I | 992.00 | NIST | |
S°liquid | [195.00; 205.94] | J/mol×K | |
S°liquid | 205.94 | J/mol×K | NIST |
S°liquid | 195.00 | J/mol×K | NIST |
Tboil | 357.88 | K | KDB |
Tc | [557.30; 560.10] | K | |
Tc | 560.09 | K | KDB |
Tc | Outlier 557.30 | K | The Cri... |
Tc | 560.10 | K | NIST |
Tc | 560.10 ± 0.20 | K | NIST |
Tc | 560.07 ± 0.07 | K | NIST |
Tc | 559.70 ± 0.60 | K | NIST |
Tfus | [230.94; 231.75] | K | |
Tfus | 230.94 | K | KDB |
Tfus | 231.75 | K | Aq. Sol... |
Tfus | 230.96 ± 0.06 | K | NIST |
Tfus | 231.25 ± 0.50 | K | NIST |
Tfus | 231.30 ± 1.00 | K | NIST |
Tfus | 231.25 ± 0.40 | K | NIST |
Ttriple | [230.92; 231.10] | K | |
Ttriple | 230.92 ± 0.08 | K | NIST |
Ttriple | 230.94 ± 0.05 | K | NIST |
Ttriple | 231.10 ± 0.20 | K | NIST |
Vc | [0.269; 0.462] | m3/kmol | |
Vc | 0.269 | m3/kmol | KDB |
Vc | 0.269 ± 0.008 | m3/kmol | NIST |
Vc | 0.462 ± 0.004 | m3/kmol | NIST |
Zc | 0.2628840 | KDB | |
Zra | 0.27 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [111.67; 160.26] | J/mol×K | [362.63; 563.38] | |
T(K) Ideal gas heat capacity (J/mol×K) 110 120 130 140 150 160 400 450 500 550 | ||||
Cp,gas | 111.67 | J/mol×K | 362.63 | Joback Calculated Property |
Cp,gas | 121.05 | J/mol×K | 396.09 | Joback Calculated Property |
Cp,gas | 129.89 | J/mol×K | 429.55 | Joback Calculated Property |
Cp,gas | 138.21 | J/mol×K | 463.01 | Joback Calculated Property |
Cp,gas | 146.03 | J/mol×K | 496.46 | Joback Calculated Property |
Cp,gas | 153.38 | J/mol×K | 529.92 | Joback Calculated Property |
Cp,gas | 160.26 | J/mol×K | 563.38 | Joback Calculated Property |
Cp,liquid | [146.29; 146.57] | J/mol×K | [298.10; 298.15] | |
Cp,liquid | 146.57 | J/mol×K | 298.10 | NIST |
Cp,liquid | 146.29 | J/mol×K | 298.15 | NIST |
Cp,liquid | 146.36 | J/mol×K | 298.15 | NIST |
ΔfusH | [10.40; 11.31] | kJ/mol | [230.90; 231.10] | |
ΔfusH | 11.31 | kJ/mol | 230.90 | NIST |
ΔfusH | 11.31 | kJ/mol | 230.90 | NIST |
ΔfusH | 11.30 | kJ/mol | 230.94 | NIST |
ΔfusH | 10.40 | kJ/mol | 231.10 | NIST |
ΔvapH | [29.70; 33.60] | kJ/mol | [318.00; 529.00] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 30 31 32 33 350 400 450 500 | ||||
ΔvapH | 33.50 ± 0.10 | kJ/mol | 318.00 | NIST |
ΔvapH | 32.40 ± 0.10 | kJ/mol | 337.00 | NIST |
ΔvapH | 33.60 | kJ/mol | 353.00 | NIST |
ΔvapH | 31.19 | kJ/mol | 357.90 | NIST |
ΔvapH | 31.20 ± 0.10 | kJ/mol | 358.00 | NIST |
ΔvapH | 33.39 | kJ/mol | 358.10 | KDB |
ΔvapH | 29.70 ± 0.10 | kJ/mol | 382.00 | NIST |
ΔvapH | 31.80 | kJ/mol | 396.00 | NIST |
ΔvapH | 31.90 | kJ/mol | 444.00 | NIST |
ΔvapH | 31.00 | kJ/mol | 457.50 | NIST |
ΔvapH | 30.90 | kJ/mol | 529.00 | NIST |
Pvap | [2.98; 12.77] | kPa | [274.20; 303.20] | |
T(K) Vapor pressure (kPa) 4 6 8 10 12 280 290 300 | ||||
Pvap | 2.98 | kPa | 274.20 | Vaporiz... |
Pvap | 3.64 | kPa | 278.20 | Vaporiz... |
Pvap | 4.84 | kPa | 283.20 | Vaporiz... |
Pvap | 6.26 | kPa | 288.20 | Vaporiz... |
Pvap | 8.02 | kPa | 293.20 | Vaporiz... |
Pvap | 10.29 | kPa | 298.20 | Vaporiz... |
Pvap | 12.77 | kPa | 303.20 | Vaporiz... |
n0 | [1.45630; 1.46300] | [298.15; 313.15] | ||
n0 | 1.46290 | 298.15 | Thermop... | |
n0 | 1.46300 | 303.15 | Refract... | |
n0 | 1.45940 | 308.15 | Refract... | |
n0 | 1.45630 | 313.15 | Refract... | |
ρl | [985.00; 1036.89] | kg/m3 | [283.15; 330.10] | |
T(K) Liquid Density (kg/m3) 980 990 1000 1010 1020 1030 1040 300 320 | ||||
ρl | 1036.89 | kg/m3 | 283.15 | The den... |
ρl | 1030.93 | kg/m3 | 288.15 | The den... |
ρl | 1024.00 | kg/m3 | 293.00 | KDB |
ρl | 1024.96 | kg/m3 | 293.15 | The den... |
ρl | 1022.27 | kg/m3 | 293.20 | Isobari... |
ρl | 1022.27 | kg/m3 | 293.20 | Isobari... |
ρl | 1022.00 | kg/m3 | 296.20 | Liquid-... |
ρl | 1019.07 | kg/m3 | 298.15 | The den... |
ρl | 1013.03 | kg/m3 | 303.15 | The den... |
ρl | 985.00 | kg/m3 | 330.10 | Liquid-... |
ΔfusS | [44.99; 48.95] | J/mol×K | [230.94; 231.10] | |
ΔfusS | 48.95 | J/mol×K | 230.94 | NIST |
ΔfusS | 44.99 | J/mol×K | 231.10 | NIST |
γ | 0.03 | N/m | 293.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.15; 202.67] | kPa | [230.94; 382.28] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43937e+01 | |||
Coefficient B | -3.10933e+03 | |||
Coefficient C | -3.99230e+01 | |||
Temperature range, min. | 230.94 | |||
Temperature range, max. | 382.28 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 | ||||
Pvap | 0.15 | kPa | 230.94 | Calculated Property |
Pvap | 0.57 | kPa | 247.76 | Calculated Property |
Pvap | 1.74 | kPa | 264.57 | Calculated Property |
Pvap | 4.56 | kPa | 281.39 | Calculated Property |
Pvap | 10.54 | kPa | 298.20 | Calculated Property |
Pvap | 22.00 | kPa | 315.02 | Calculated Property |
Pvap | 42.19 | kPa | 331.83 | Calculated Property |
Pvap | 75.36 | kPa | 348.65 | Calculated Property |
Pvap | 126.78 | kPa | 365.46 | Calculated Property |
Pvap | 202.67 | kPa | 382.28 | Calculated Property |
Pvap | [0.15; 4492.60] | kPa | [230.94; 560.09] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.12733e+01 | |||
Coefficient B | -5.96836e+03 | |||
Coefficient C | -6.90360e+00 | |||
Coefficient D | 4.71669e-06 | |||
Temperature range, min. | 230.94 | |||
Temperature range, max. | 560.09 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400 500 | ||||
Pvap | 0.15 | kPa | 230.94 | Calculated Property |
Pvap | 2.04 | kPa | 267.51 | Calculated Property |
Pvap | 13.63 | kPa | 304.08 | Calculated Property |
Pvap | 57.19 | kPa | 340.66 | Calculated Property |
Pvap | 175.01 | kPa | 377.23 | Calculated Property |
Pvap | 428.73 | kPa | 413.80 | Calculated Property |
Pvap | 894.66 | kPa | 450.37 | Calculated Property |
Pvap | 1659.76 | kPa | 486.95 | Calculated Property |
Pvap | 2821.49 | kPa | 523.52 | Calculated Property |
Pvap | 4492.60 | kPa | 560.09 | Calculated Property |
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