Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3350 | KDB | |
AP | 317.650 | K | KDB |
ΔcH°liquid | [-5245.98; -5245.60] | kJ/mol | |
ΔcH°liquid | -5245.98 ± 0.75 | kJ/mol | NIST |
ΔcH°liquid | -5245.60 ± 1.20 | kJ/mol | NIST |
ΔfG° | 52.63 | kJ/mol | KDB |
Δc,grossH | 5245.65 | kJ/mol | KDB |
Δc,netH | 4893.565 | kJ/mol | KDB |
ΔfH°gas | [-148.20; -147.60] | kJ/mol | |
ΔfH°gas | -148.20 | kJ/mol | KDB |
ΔfH°gas | -147.60 | kJ/mol | NIST |
ΔfH°gas | -148.10 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | [-189.20; -188.70] | kJ/mol | |
ΔfH°liquid | -188.70 ± 0.92 | kJ/mol | NIST |
ΔfH°liquid | -189.20 ± 1.30 | kJ/mol | NIST |
ΔfusH° | 10.41 | kJ/mol | Joback Calculated Property |
ΔvapH° | [41.08; 41.12] | kJ/mol | |
ΔvapH° | 41.12 | kJ/mol | NIST |
ΔvapH° | 41.10 | kJ/mol | NIST |
ΔvapH° | 41.10 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 41.08 | kJ/mol | NIST |
ΔvapH° | 41.10 | kJ/mol | NIST |
IE | [9.34; 10.00] | eV | |
IE | 9.34 ± 0.05 | eV | NIST |
IE | 10.00 ± 0.04 | eV | NIST |
log10WS | [-4.74; -4.74] | ||
log10WS | -4.74 | Aq. Sol... | |
log10WS | -4.74 | Estimat... | |
logPoct/wat | 2.977 | Crippen Calculated Property | |
McVol | 112.720 | ml/mol | McGowan Calculated Property |
Pc | 3000.00 | kPa | KDB |
Inp | [808.20; 857.00] | ||
Inp | 826.00 | NIST | |
Inp | 827.20 | NIST | |
Inp | 831.60 | NIST | |
Inp | 829.40 | NIST | |
Inp | 833.40 | NIST | |
Inp | 829.90 | NIST | |
Inp | 839.20 | NIST | |
Inp | 830.10 | NIST | |
Inp | 830.40 | NIST | |
Inp | 833.80 | NIST | |
Inp | 837.10 | NIST | |
Inp | 837.30 | NIST | |
Inp | 839.00 | NIST | |
Inp | 840.00 | NIST | |
Inp | 832.00 | NIST | |
Inp | 836.00 | NIST | |
Inp | 848.00 | NIST | |
Inp | Outlier 851.00 | NIST | |
Inp | Outlier 853.00 | NIST | |
Inp | Outlier 857.00 | NIST | |
Inp | 830.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 848.00 | NIST | |
Inp | Outlier 849.00 | NIST | |
Inp | 830.00 | NIST | |
Inp | 833.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 836.00 | NIST | |
Inp | 839.00 | NIST | |
Inp | 830.30 | NIST | |
Inp | 830.00 | NIST | |
Inp | Outlier 851.00 | NIST | |
Inp | 826.00 | NIST | |
Inp | 830.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 838.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 845.00 | NIST | |
Inp | Outlier 808.20 | NIST | |
Inp | 841.73 | NIST | |
Inp | 832.00 | NIST | |
Inp | 831.30 | NIST | |
Inp | 836.50 | NIST | |
Inp | 832.70 | NIST | |
Inp | 827.12 | NIST | |
Inp | 827.00 | NIST | |
Inp | 830.60 | NIST | |
Inp | 825.30 | NIST | |
Inp | 825.60 | NIST | |
Inp | 834.00 | NIST | |
Inp | 830.00 | NIST | |
Inp | 839.00 | NIST | |
Inp | 828.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 828.00 | NIST | |
Inp | 831.00 | NIST | |
Inp | 832.00 | NIST | |
Inp | 830.00 | NIST | |
Inp | 833.00 | NIST | |
Inp | 832.00 | NIST | |
Inp | 830.70 | NIST | |
Inp | 832.30 | NIST | |
Inp | 834.50 | NIST | |
Inp | 836.20 | NIST | |
Inp | 837.60 | NIST | |
Inp | 838.80 | NIST | |
Inp | 830.00 | NIST | |
Inp | 832.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 836.00 | NIST | |
Inp | 837.00 | NIST | |
Inp | 838.00 | NIST | |
Inp | Outlier 817.00 | NIST | |
Inp | 826.00 | NIST | |
Inp | 830.00 | NIST | |
Inp | 832.00 | NIST | |
Inp | 827.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 832.30 | NIST | |
Inp | 830.00 | NIST | |
Inp | 838.00 | NIST | |
I | [890.60; 912.00] | ||
I | 912.00 | NIST | |
I | 895.00 | NIST | |
I | 900.00 | NIST | |
I | 904.00 | NIST | |
I | 898.00 | NIST | |
I | 903.00 | NIST | |
I | 907.00 | NIST | |
I | 891.00 | NIST | |
I | 894.00 | NIST | |
I | 898.00 | NIST | |
I | 903.00 | NIST | |
I | 907.10 | NIST | |
I | 890.60 | NIST | |
I | 894.00 | NIST | |
I | 912.00 | NIST | |
I | 912.00 | NIST | |
I | 903.00 | NIST | |
S°gas | 414.47 | J/mol×K | NIST |
S°liquid | 310.83 | J/mol×K | NIST |
Tboil | 404.10 | K | KDB |
Tc | 603.00 | K | KDB |
Tfus | [155.80; 156.00] | K | |
Tfus | 155.80 | K | KDB |
Tfus | 156.00 | K | Aq. Sol... |
Ttriple | [155.79; 155.80] | K | |
Ttriple | 155.79 ± 0.01 | K | NIST |
Ttriple | 155.80 ± 0.60 | K | NIST |
Vc | 0.425 | m3/kmol | KDB |
Zc | 0.2543060 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [213.84; 301.46] | J/mol×K | [397.72; 590.42] | |
T(K) Ideal gas heat capacity (J/mol×K) 220 240 260 280 300 400 450 500 550 | ||||
Cp,gas | 213.84 | J/mol×K | 397.72 | Joback Calculated Property |
Cp,gas | 230.32 | J/mol×K | 429.84 | Joback Calculated Property |
Cp,gas | 246.02 | J/mol×K | 461.95 | Joback Calculated Property |
Cp,gas | 260.95 | J/mol×K | 494.07 | Joback Calculated Property |
Cp,gas | 275.16 | J/mol×K | 526.19 | Joback Calculated Property |
Cp,gas | 288.65 | J/mol×K | 558.31 | Joback Calculated Property |
Cp,gas | 301.46 | J/mol×K | 590.42 | Joback Calculated Property |
Cp,liquid | 216.27 | J/mol×K | 298.15 | NIST |
η | [0.0003069; 0.0043742] | Pa×s | [190.82; 397.72] | |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 200 300 400 | ||||
η | 0.0043742 | Pa×s | 190.82 | Joback Calculated Property |
η | 0.0020017 | Pa×s | 225.30 | Joback Calculated Property |
η | 0.0011273 | Pa×s | 259.79 | Joback Calculated Property |
η | 0.0007263 | Pa×s | 294.27 | Joback Calculated Property |
η | 0.0005131 | Pa×s | 328.75 | Joback Calculated Property |
η | 0.0003873 | Pa×s | 363.24 | Joback Calculated Property |
η | 0.0003069 | Pa×s | 397.72 | Joback Calculated Property |
ΔfusH | [10.03; 10.04] | kJ/mol | [155.79; 155.80] | |
ΔfusH | 10.03 | kJ/mol | 155.79 | NIST |
ΔfusH | 10.04 | kJ/mol | 155.80 | NIST |
ΔfusH | 10.04 | kJ/mol | 155.80 | NIST |
ΔvapH | [34.11; 39.20] | kJ/mol | [364.50; 404.10] | |
ΔvapH | 39.20 | kJ/mol | 364.50 | NIST |
ΔvapH | 34.11 | kJ/mol | 404.10 | KDB |
ΔvapH | 34.70 | kJ/mol | 404.10 | NIST |
n0 | 1.42389 | 298.15 | KDB | |
ρl | 781.00 | kg/m3 | 289.00 | KDB |
ΔfusS | 64.44 | J/mol×K | 155.79 | NIST |
γ | 0.02 | N/m | 293.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [291.64; 432.35] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41315e+01 | |||
Coefficient B | -3.42008e+03 | |||
Coefficient C | -4.45910e+01 | |||
Temperature range, min. | 291.64 | |||
Temperature range, max. | 432.35 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 291.64 | Calculated Property |
Pvap | 3.04 | kPa | 307.27 | Calculated Property |
Pvap | 6.32 | kPa | 322.91 | Calculated Property |
Pvap | 12.14 | kPa | 338.54 | Calculated Property |
Pvap | 21.85 | kPa | 354.18 | Calculated Property |
Pvap | 37.16 | kPa | 369.81 | Calculated Property |
Pvap | 60.20 | kPa | 385.45 | Calculated Property |
Pvap | 93.48 | kPa | 401.08 | Calculated Property |
Pvap | 139.89 | kPa | 416.72 | Calculated Property |
Pvap | 202.64 | kPa | 432.35 | Calculated Property |
Pvap | [6.03e-08; 2951.13] | kPa | [155.81; 603.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.66656e+01 | |||
Coefficient B | -7.41133e+03 | |||
Coefficient C | -9.07967e+00 | |||
Coefficient D | 4.79197e-06 | |||
Temperature range, min. | 155.81 | |||
Temperature range, max. | 603.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 400 600 | ||||
Pvap | 6.03e-08 | kPa | 155.81 | Calculated Property |
Pvap | 5.26e-04 | kPa | 205.50 | Calculated Property |
Pvap | 0.09 | kPa | 255.19 | Calculated Property |
Pvap | 2.38 | kPa | 304.87 | Calculated Property |
Pvap | 21.32 | kPa | 354.56 | Calculated Property |
Pvap | 101.36 | kPa | 404.25 | Calculated Property |
Pvap | 322.85 | kPa | 453.94 | Calculated Property |
Pvap | 790.66 | kPa | 503.62 | Calculated Property |
Pvap | 1622.48 | kPa | 553.31 | Calculated Property |
Pvap | 2951.13 | kPa | 603.00 | Calculated Property |
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