Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3310 | KDB | |
PAff | 836.30 | kJ/mol | NIST |
BasG | 804.40 | kJ/mol | NIST |
ΔcH°liquid | -3097.20 ± 0.80 | kJ/mol | NIST |
μ | 2.80 | debye | KDB |
ΔfG° | -140.14 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -262.57 ± 0.87 | kJ/mol | NIST |
ΔfH°liquid | -299.47 ± 0.86 | kJ/mol | NIST |
ΔfusH° | 6.78 | kJ/mol | Joback Calculated Property |
ΔvapH° | [36.80; 36.90] | kJ/mol | |
ΔvapH° | 36.87 | kJ/mol | NIST |
ΔvapH° | 36.81 | kJ/mol | NIST |
ΔvapH° | 36.80 | kJ/mol | NIST |
ΔvapH° | 36.90 | kJ/mol | NIST |
IE | [9.30; 9.36] | eV | |
IE | 9.31 ± 0.02 | eV | NIST |
IE | 9.30 ± 0.01 | eV | NIST |
IE | 9.30 ± 0.01 | eV | NIST |
IE | 9.30 ± 0.04 | eV | NIST |
IE | Outlier 9.36 | eV | NIST |
IE | 9.30 ± 0.01 | eV | NIST |
IE | 9.30 ± 0.02 | eV | NIST |
IE | 9.32 ± 0.02 | eV | NIST |
log10WS | [-0.12; -0.12] | ||
log10WS | -0.12 | Aq. Sol... | |
log10WS | -0.12 | Estimat... | |
logPoct/wat | 1.231 | Crippen Calculated Property | |
McVol | 82.880 | ml/mol | McGowan Calculated Property |
Pc | [3800.00; 3850.00] | kPa | |
Pc | 3850.00 | kPa | KDB |
Pc | 3800.00 ± 20.00 | kPa | NIST |
Pc | 3850.00 ± 48.30 | kPa | NIST |
ρc | 278.21 ± 24.98 | kg/m3 | NIST |
Inp | [625.00; 673.00] | ||
Inp | 640.90 | NIST | |
Inp | 642.78 | NIST | |
Inp | 639.36 | NIST | |
Inp | 639.89 | NIST | |
Inp | 640.49 | NIST | |
Inp | 641.53 | NIST | |
Inp | 643.00 | NIST | |
Inp | 640.00 | NIST | |
Inp | 640.00 | NIST | |
Inp | 642.00 | NIST | |
Inp | 646.00 | NIST | |
Inp | 627.00 | NIST | |
Inp | 650.00 | NIST | |
Inp | 647.20 | NIST | |
Inp | 636.00 | NIST | |
Inp | Outlier 673.00 | NIST | |
Inp | 640.00 | NIST | |
Inp | 625.00 | NIST | |
Inp | 641.00 | NIST | |
Inp | 657.00 | NIST | |
Inp | Outlier 666.10 | NIST | |
Inp | 628.00 | NIST | |
Inp | 638.00 | NIST | |
Inp | 659.00 | NIST | |
Inp | 654.00 | NIST | |
Inp | 628.00 | NIST | |
Inp | 639.00 | NIST | |
Inp | 637.00 | NIST | |
Inp | 658.00 | NIST | |
Inp | 641.00 | NIST | |
Inp | 653.00 | NIST | |
Inp | 640.00 | NIST | |
Inp | 640.00 | NIST | |
Inp | 641.00 | NIST | |
Inp | 642.00 | NIST | |
Inp | 641.00 | NIST | |
Inp | 635.00 | NIST | |
Inp | 636.00 | NIST | |
Inp | 642.00 | NIST | |
Inp | 650.00 | NIST | |
Inp | 647.00 | NIST | |
Inp | 651.00 | NIST | |
Inp | 650.00 | NIST | |
Inp | 640.90 | NIST | |
Inp | 641.53 | NIST | |
Inp | 646.00 | NIST | |
Inp | 641.00 | NIST | |
Inp | 659.00 | NIST | |
Inp | 640.00 | NIST | |
Inp | Outlier 673.00 | NIST | |
Inp | 658.00 | NIST | |
Inp | 642.00 | NIST | |
Inp | 650.00 | NIST | |
I | [918.00; 989.00] | ||
I | 965.00 | NIST | |
I | 949.40 | NIST | |
I | 954.40 | NIST | |
I | 959.60 | NIST | |
I | 943.20 | NIST | |
I | 929.00 | NIST | |
I | 936.00 | NIST | |
I | 929.00 | NIST | |
I | 929.00 | NIST | |
I | 918.00 | NIST | |
I | 929.00 | NIST | |
I | 925.00 | NIST | |
I | 927.00 | NIST | |
I | Outlier 989.00 | NIST | |
I | 956.00 | NIST | |
I | 929.00 | NIST | |
I | 929.00 | NIST | |
I | 970.00 | NIST | |
I | 949.00 | NIST | |
I | 936.00 | NIST | |
I | 918.00 | NIST | |
I | 929.00 | NIST | |
I | 965.00 | NIST | |
S°liquid | 268.50 | J/mol×K | NIST |
Tboil | [365.15; 389.50] | K | |
Tboil | 367.48 | K | KDB |
Tboil | 367.70 | K | NIST |
Tboil | 367.40 | K | NIST |
Tboil | Outlier 389.50 ± 0.30 | K | NIST |
Tboil | 368.30 ± 0.60 | K | NIST |
Tboil | 368.00 ± 0.40 | K | NIST |
Tboil | 366.65 ± 1.00 | K | NIST |
Tboil | 367.15 ± 1.00 | K | NIST |
Tboil | 367.65 ± 1.00 | K | NIST |
Tboil | 367.35 ± 0.50 | K | NIST |
Tboil | 367.65 ± 1.00 | K | NIST |
Tboil | 367.90 ± 0.50 | K | NIST |
Tboil | 366.15 ± 2.00 | K | NIST |
Tboil | 367.35 ± 0.50 | K | NIST |
Tboil | 368.55 ± 2.00 | K | NIST |
Tboil | 365.65 ± 2.00 | K | NIST |
Tboil | 368.60 ± 0.50 | K | NIST |
Tboil | 368.15 ± 2.00 | K | NIST |
Tboil | 366.70 ± 0.50 | K | NIST |
Tboil | 367.41 ± 0.50 | K | NIST |
Tboil | 365.15 ± 5.00 | K | NIST |
Tboil | 367.30 ± 1.00 | K | NIST |
Tboil | 366.15 ± 1.00 | K | NIST |
Tboil | 366.65 ± 2.00 | K | NIST |
Tboil | 365.65 ± 5.00 | K | NIST |
Tboil | 366.65 ± 1.00 | K | NIST |
Tboil | 366.65 ± 1.00 | K | NIST |
Tboil | 368.15 ± 2.00 | K | NIST |
Tboil | 365.15 ± 2.00 | K | NIST |
Tboil | 366.65 ± 1.00 | K | NIST |
Tboil | 368.65 ± 1.00 | K | NIST |
Tboil | 367.65 ± 2.00 | K | NIST |
Tboil | 368.30 ± 2.00 | K | NIST |
Tboil | 367.15 ± 1.00 | K | NIST |
Tboil | 367.65 ± 2.00 | K | NIST |
Tboil | 366.15 ± 1.00 | K | NIST |
Tboil | 366.65 ± 1.00 | K | NIST |
Tboil | 365.55 ± 0.30 | K | NIST |
Tboil | 367.65 ± 2.00 | K | NIST |
Tboil | 366.65 ± 1.00 | K | NIST |
Tboil | 366.65 ± 1.00 | K | NIST |
Tboil | 366.65 ± 1.00 | K | NIST |
Tc | [553.10; 553.40] | K | |
Tc | 553.40 | K | KDB |
Tc | 553.10 ± 0.40 | K | NIST |
Tc | 553.40 | K | NIST |
Tc | 553.40 ± 0.83 | K | NIST |
Tfus | [178.75; 181.15] | K | |
Tfus | 181.00 | K | KDB |
Tfus | 180.78 | K | Aq. Sol... |
Tfus | 178.75 ± 0.40 | K | NIST |
Tfus | 181.15 ± 0.60 | K | NIST |
Ttriple | 180.01 ± 0.06 | K | NIST |
Vc | 0.310 | m3/kmol | KDB |
Zc | 0.2593860 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [139.58; 172.09] | J/mol×K | [358.15; 473.15] | |
T(K) Ideal gas heat capacity (J/mol×K) 140 145 150 155 160 165 170 175 400 450 | ||||
Cp,gas | 139.58 | J/mol×K | 358.15 | NIST |
Cp,gas | 146.82 | J/mol×K | 383.15 | NIST |
Cp,gas | 154.26 | J/mol×K | 408.15 | NIST |
Cp,gas | 161.25 | J/mol×K | 433.15 | NIST |
Cp,gas | 166.77 | J/mol×K | 453.15 | NIST |
Cp,gas | 172.09 | J/mol×K | 473.15 | NIST |
Cp,liquid | [179.90; 180.00] | J/mol×K | [298.15; 298.15] | |
Cp,liquid | 180.00 | J/mol×K | 298.15 | NIST |
Cp,liquid | 179.90 | J/mol×K | 298.15 | NIST |
η | [0.0002843; 0.0056166] | Pa×s | [181.04; 367.23] | |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 200 250 300 350 | ||||
η | 0.0056166 | Pa×s | 181.04 | Joback Calculated Property |
η | 0.0023744 | Pa×s | 212.07 | Joback Calculated Property |
η | 0.0012505 | Pa×s | 243.10 | Joback Calculated Property |
η | 0.0007615 | Pa×s | 274.13 | Joback Calculated Property |
η | 0.0005129 | Pa×s | 305.17 | Joback Calculated Property |
η | 0.0003716 | Pa×s | 336.20 | Joback Calculated Property |
η | 0.0002843 | Pa×s | 367.23 | Joback Calculated Property |
ΔfusH | [9.34; 9.34] | kJ/mol | [180.00; 180.01] | |
ΔfusH | 9.34 | kJ/mol | 180.00 | NIST |
ΔfusH | 9.34 | kJ/mol | 180.00 | NIST |
ΔfusH | 9.34 | kJ/mol | 180.01 | NIST |
ΔvapH | [32.30; 35.50] | kJ/mol | [327.00; 452.50] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 32 32.5 33 33.5 34 34.5 35 35.5 350 400 450 | ||||
ΔvapH | 35.00 ± 0.10 | kJ/mol | 327.00 | NIST |
ΔvapH | 35.50 | kJ/mol | 340.00 | NIST |
ΔvapH | 33.80 ± 0.10 | kJ/mol | 346.00 | NIST |
ΔvapH | 35.00 | kJ/mol | 352.50 | NIST |
ΔvapH | 32.30 ± 0.10 | kJ/mol | 367.00 | NIST |
ΔvapH | 32.35 | kJ/mol | 367.40 | NIST |
ΔvapH | 33.80 | kJ/mol | 389.00 | NIST |
ΔvapH | 32.60 | kJ/mol | 452.50 | NIST |
n0 | [1.38620; 1.38620] | [298.15; 298.15] | ||
n0 | 1.38620 | 298.15 | Isother... | |
n0 | 1.38620 | 298.15 | Vapor-L... | |
ρl | [778.62; 808.30] | kg/m3 | [288.15; 318.15] | |
T(K) Liquid Density (kg/m3) 780 785 790 795 800 805 810 290 300 310 | ||||
ρl | 808.30 | kg/m3 | 288.15 | Thermal... |
ρl | 803.00 | kg/m3 | 293.00 | KDB |
ρl | 799.55 | kg/m3 | 298.15 | Vapour-... |
ρl | 800.63 | kg/m3 | 298.15 | Liquid-... |
ρl | 798.51 | kg/m3 | 298.15 | Thermal... |
ρl | 788.60 | kg/m3 | 308.15 | Thermal... |
ρl | 778.62 | kg/m3 | 318.15 | Thermal... |
ΔfusS | 51.90 | J/mol×K | 180.01 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [273.22; 390.44] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42556e+01 | |||
Coefficient B | -2.91500e+03 | |||
Coefficient C | -6.45290e+01 | |||
Temperature range, min. | 273.22 | |||
Temperature range, max. | 390.44 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 273.22 | Calculated Property |
Pvap | 3.03 | kPa | 286.24 | Calculated Property |
Pvap | 6.28 | kPa | 299.27 | Calculated Property |
Pvap | 12.07 | kPa | 312.29 | Calculated Property |
Pvap | 21.71 | kPa | 325.32 | Calculated Property |
Pvap | 36.95 | kPa | 338.34 | Calculated Property |
Pvap | 59.92 | kPa | 351.37 | Calculated Property |
Pvap | 93.18 | kPa | 364.39 | Calculated Property |
Pvap | 139.65 | kPa | 377.42 | Calculated Property |
Pvap | 202.64 | kPa | 390.44 | Calculated Property |
Pvap | [2.35e-05; 3934.08] | kPa | [181.15; 553.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.01851e+02 | |||
Coefficient B | -1.16914e+04 | |||
Coefficient C | -2.86327e+01 | |||
Coefficient D | 2.74487e-05 | |||
Temperature range, min. | 181.15 | |||
Temperature range, max. | 553.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 300 400 500 | ||||
Pvap | 2.35e-05 | kPa | 181.15 | Calculated Property |
Pvap | 0.02 | kPa | 222.47 | Calculated Property |
Pvap | 0.83 | kPa | 263.78 | Calculated Property |
Pvap | 9.86 | kPa | 305.10 | Calculated Property |
Pvap | 52.54 | kPa | 346.42 | Calculated Property |
Pvap | 174.91 | kPa | 387.73 | Calculated Property |
Pvap | 443.66 | kPa | 429.05 | Calculated Property |
Pvap | 968.92 | kPa | 470.37 | Calculated Property |
Pvap | 1970.91 | kPa | 511.68 | Calculated Property |
Pvap | 3934.08 | kPa | 553.00 | Calculated Property |
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