Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2670 | KDB | |
AP | 343.650 | K | KDB |
ΔcH°liquid | [-4806.70; -4802.00] | kJ/mol |
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ΔcH°liquid | -4806.70 ± 0.79 | kJ/mol | NIST |
ΔcH°liquid | -4802.00 ± 1.00 | kJ/mol | NIST |
μ | 0.00 | debye | KDB |
ΔfG° | 2.64 | kJ/mol | KDB |
Δc,grossH | 4806.70 | kJ/mol | KDB |
Δc,netH | 4454.580 | kJ/mol | KDB |
ΔfH°gas | [-205.90; -201.50] | kJ/mol |
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ΔfH°gas | -201.70 | kJ/mol | KDB |
ΔfH°gas | -201.50 ± 0.92 | kJ/mol | NIST |
ΔfH°gas | -205.90 | kJ/mol | NIST |
ΔfH°liquid | [-239.00; -234.60] | kJ/mol |
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ΔfH°liquid | -234.60 ± 0.92 | kJ/mol | NIST |
ΔfH°liquid | -239.00 ± 1.00 | kJ/mol | NIST |
ΔfusH° | 6.47 | kJ/mol | Joback Calculated Property |
ΔvapH° | [33.00; 33.15] | kJ/mol |
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ΔvapH° | 33.15 | kJ/mol | NIST |
ΔvapH° | 33.00 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 33.00 | kJ/mol | NIST |
ΔvapH° | 33.00 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 33.02 | kJ/mol | NIST |
log10WS | [-4.23; -4.23] |
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|
log10WS | -4.23 | Aq. Sol... | |
log10WS | -4.23 | Estimat... | |
logPoct/wat | 2.833 | Crippen Calculated Property | |
McVol | 109.490 | ml/mol | McGowan Calculated Property |
Pc | [2945.80; 2950.00] | kPa |
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Pc | 2950.00 | kPa | KDB |
Pc | 2950.00 ± 50.00 | kPa | NIST |
Pc | 2945.80 ± 40.53 | kPa | NIST |
ρc | [242.49; 242.49] | kg/m3 |
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ρc | 242.49 ± 5.01 | kg/m3 | NIST |
ρc | 242.49 ± 5.01 | kg/m3 | NIST |
Inp | [643.00; 669.00] |
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|
Inp | 653.10 | NIST | |
Inp | 656.30 | NIST | |
Inp | 660.00 | NIST | |
Inp | 649.00 | NIST | |
Inp | 662.80 | NIST | |
Inp | 658.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | 658.10 | NIST | |
Inp | 658.00 | NIST | |
Inp | 658.10 | NIST | |
Inp | 658.00 | NIST | |
Inp | 657.90 | NIST | |
Inp | 656.20 | NIST | |
Inp | 659.00 | NIST | |
Inp | 658.90 | NIST | |
Inp | 661.50 | NIST | |
Inp | 658.50 | NIST | |
Inp | 661.20 | NIST | |
Inp | 654.70 | NIST | |
Inp | 656.10 | NIST | |
Inp | 657.60 | NIST | |
Inp | 659.20 | NIST | |
Inp | 654.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | 657.00 | NIST | |
Inp | 658.00 | NIST | |
Inp | 659.00 | NIST | |
Inp | 661.00 | NIST | |
Inp | 654.60 | NIST | |
Inp | 655.90 | NIST | |
Inp | 657.30 | NIST | |
Inp | 658.70 | NIST | |
Inp | 660.30 | NIST | |
Inp | 661.90 | NIST | |
Inp | 658.10 | NIST | |
Inp | 658.10 | NIST | |
Inp | 656.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | 658.00 | NIST | |
Inp | 658.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | 655.00 | NIST | |
Inp | 656.50 | NIST | |
Inp | 658.00 | NIST | |
Inp | 659.70 | NIST | |
Inp | 661.40 | NIST | |
Inp | 663.40 | NIST | |
Inp | 657.00 | NIST | |
Inp | 657.60 | NIST | |
Inp | 657.90 | NIST | |
Inp | 658.30 | NIST | |
Inp | 658.80 | NIST | |
Inp | 659.30 | NIST | |
Inp | 661.00 | NIST | |
Inp | 662.00 | NIST | |
Inp | 662.00 | NIST | |
Inp | 663.00 | NIST | |
Inp | 657.00 | NIST | |
Inp | 660.00 | NIST | |
Inp | Outlier 643.00 | NIST | |
Inp | 659.00 | NIST | |
Inp | 662.00 | NIST | |
Inp | 664.21 | NIST | |
Inp | 665.95 | NIST | |
Inp | Outlier 667.80 | NIST | |
Inp | 660.59 | NIST | |
Inp | 662.46 | NIST | |
Inp | 654.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | 657.00 | NIST | |
Inp | 658.00 | NIST | |
Inp | 660.00 | NIST | |
Inp | 659.10 | NIST | |
Inp | 660.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | 662.00 | NIST | |
Inp | 658.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | 659.00 | NIST | |
Inp | 661.00 | NIST | |
Inp | 664.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | 659.00 | NIST | |
Inp | 662.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | 657.00 | NIST | |
Inp | 660.00 | NIST | |
Inp | 661.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | Outlier 646.00 | NIST | |
Inp | 657.00 | NIST | |
Inp | 654.25 | NIST | |
Inp | 651.90 | NIST | |
Inp | Outlier 643.69 | NIST | |
Inp | Outlier 644.47 | NIST | |
Inp | 651.50 | NIST | |
Inp | 650.50 | NIST | |
Inp | 647.31 | NIST | |
Inp | 647.32 | NIST | |
Inp | 648.00 | NIST | |
Inp | Outlier 646.00 | NIST | |
Inp | 650.00 | NIST | |
Inp | 651.00 | NIST | |
Inp | 659.00 | NIST | |
Inp | 656.00 | NIST | |
Inp | 659.00 | NIST | |
Inp | 666.00 | NIST | |
Inp | 662.00 | NIST | |
Inp | 653.00 | NIST | |
Inp | 661.00 | NIST | |
Inp | 652.00 | NIST | |
Inp | 653.00 | NIST | |
Inp | 647.00 | NIST | |
Inp | 664.00 | NIST | |
Inp | 660.00 | NIST | |
Inp | 660.00 | NIST | |
Inp | 650.00 | NIST | |
Inp | 659.00 | NIST | |
Inp | 653.00 | NIST | |
Inp | 659.00 | NIST | |
Inp | 647.00 | NIST | |
Inp | 649.00 | NIST | |
Inp | 654.00 | NIST | |
Inp | Outlier 646.00 | NIST | |
Inp | 657.00 | NIST | |
Inp | 658.00 | NIST | |
Inp | 653.00 | NIST | |
Inp | Outlier 669.00 | NIST | |
Inp | Outlier 669.00 | NIST | |
Inp | 654.25 | NIST | |
Inp | Outlier 646.00 | NIST | |
Inp | 651.00 | NIST | |
Inp | 662.00 | NIST | |
Inp | 650.00 | NIST | |
Inp | 664.00 | NIST | |
Inp | 653.00 | NIST | |
Inp | Outlier 669.00 | NIST | |
S°gas | 398.02 | J/mol×K | NIST |
S°liquid | [293.30; 305.60] | J/mol×K |
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S°liquid | 305.60 | J/mol×K | NIST |
S°liquid | 293.30 | J/mol×K | NIST |
Tboil | [358.95; 363.15] | K |
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Tboil | 359.21 | K | KDB |
Tboil | 359.30 | K | NIST |
Tboil | 359.20 | K | NIST |
Tboil | 359.15 ± 0.40 | K | NIST |
Tboil | 359.21 ± 0.20 | K | NIST |
Tboil | 359.22 ± 0.20 | K | NIST |
Tboil | 359.20 ± 0.20 | K | NIST |
Tboil | 359.20 ± 0.20 | K | NIST |
Tboil | 359.20 ± 0.30 | K | NIST |
Tboil | 359.20 ± 0.20 | K | NIST |
Tboil | 359.21 ± 0.10 | K | NIST |
Tboil | 359.25 ± 0.50 | K | NIST |
Tboil | 358.95 ± 0.40 | K | NIST |
Tboil | 359.25 ± 0.30 | K | NIST |
Tboil | 359.20 ± 0.20 | K | NIST |
Tboil | 359.25 ± 0.30 | K | NIST |
Tboil | 359.21 ± 0.01 | K | NIST |
Tboil | 359.24 ± 0.20 | K | NIST |
Tboil | 359.25 ± 0.30 | K | NIST |
Tboil | 359.25 ± 0.30 | K | NIST |
Tboil | Outlier 363.05 ± 0.50 | K | NIST |
Tboil | Outlier 363.15 ± 0.50 | K | NIST |
Tboil | 359.23 ± 0.30 | K | NIST |
Tboil | 359.21 ± 0.06 | K | NIST |
Tboil | 359.00 ± 0.30 | K | NIST |
Tboil | 359.12 ± 0.10 | K | NIST |
Tboil | 359.00 ± 0.50 | K | NIST |
Tboil | 359.25 ± 0.50 | K | NIST |
Tboil | 359.25 ± 0.20 | K | NIST |
Tboil | 359.25 ± 0.30 | K | NIST |
Tboil | 359.15 ± 0.50 | K | NIST |
Tboil | 359.25 ± 0.20 | K | NIST |
Tboil | 359.25 ± 0.30 | K | NIST |
Tboil | 359.10 ± 0.50 | K | NIST |
Tboil | 359.15 ± 0.50 | K | NIST |
Tboil | 359.15 ± 0.50 | K | NIST |
Tboil | 359.40 ± 0.60 | K | NIST |
Tboil | 359.70 ± 2.00 | K | NIST |
Tboil | 360.00 ± 3.00 | K | NIST |
Tc | [536.30; 536.40] | K |
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Tc | 536.40 | K | KDB |
Tc | 536.40 ± 0.50 | K | NIST |
Tc | 536.30 | K | NIST |
Tc | 536.34 ± 0.40 | K | NIST |
Tfus | [137.24; 138.71] | K |
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Tfus | 138.20 | K | KDB |
Tfus | 138.52 | K | Aq. Sol... |
Tfus | 138.34 ± 0.30 | K | NIST |
Tfus | 137.54 ± 0.50 | K | NIST |
Tfus | 138.70 ± 0.05 | K | NIST |
Tfus | 138.70 ± 0.05 | K | NIST |
Tfus | 138.71 ± 0.05 | K | NIST |
Tfus | 138.17 ± 0.30 | K | NIST |
Tfus | 138.17 ± 0.20 | K | NIST |
Tfus | 137.60 ± 0.40 | K | NIST |
Tfus | 138.16 ± 0.01 | K | NIST |
Tfus | 138.64 ± 0.06 | K | NIST |
Tfus | 138.64 ± 0.05 | K | NIST |
Tfus | 138.69 ± 0.04 | K | NIST |
Tfus | 138.20 ± 0.05 | K | NIST |
Tfus | 137.59 ± 0.05 | K | NIST |
Tfus | 138.12 ± 0.50 | K | NIST |
Tfus | 137.50 ± 0.30 | K | NIST |
Tfus | 137.55 ± 0.70 | K | NIST |
Tfus | 137.24 ± 0.40 | K | NIST |
Tfus | 137.41 ± 0.20 | K | NIST |
Tfus | 137.45 ± 0.30 | K | NIST |
Tfus | 137.45 ± 0.50 | K | NIST |
Tfus | 138.15 ± 0.50 | K | NIST |
Tfus | 138.25 ± 0.50 | K | NIST |
Tfus | 138.15 ± 0.50 | K | NIST |
Tfus | 138.15 ± 0.30 | K | NIST |
Ttriple | [138.20; 138.75] | K |
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Ttriple | 138.75 ± 0.10 | K | NIST |
Ttriple | 138.20 ± 0.03 | K | NIST |
Ttriple | 138.20 ± 0.20 | K | NIST |
Vc | [0.414; 0.414] | m3/kmol |
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Vc | 0.414 | m3/kmol | KDB |
Vc | 0.414 | m3/kmol | NIST |
Zc | 0.2738400 | KDB | |
Zra | 0.27 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [187.44; 250.70] | J/mol×K | [344.13; 487.21] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 190 200 210 220 230 240 250 350 400 450 | ||||
Cp,gas | 187.44 ± 0.37 | J/mol×K | 344.13 | NIST |
Cp,gas | 197.68 ± 0.40 | J/mol×K | 366.22 | NIST |
Cp,gas | 214.51 ± 0.43 | J/mol×K | 402.31 | NIST |
Cp,gas | 235.08 ± 0.47 | J/mol×K | 449.30 | NIST |
Cp,gas | 250.70 ± 0.50 | J/mol×K | 487.21 | NIST |
Cp,liquid | [211.70; 214.80] | J/mol×K | [292.90; 298.15] | ![]() |
Cp,liquid | 211.70 | J/mol×K | 292.90 | NIST |
Cp,liquid | 214.80 | J/mol×K | 298.15 | NIST |
η | [0.0002842; 0.0112423] | Pa×s | [171.07; 356.33] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 0.01 200 250 300 350 | ||||
η | 0.0112423 | Pa×s | 171.07 | Joback Calculated Property |
η | 0.0038120 | Pa×s | 201.95 | Joback Calculated Property |
η | 0.0017220 | Pa×s | 232.82 | Joback Calculated Property |
η | 0.0009370 | Pa×s | 263.70 | Joback Calculated Property |
η | 0.0005792 | Pa×s | 294.58 | Joback Calculated Property |
η | 0.0003923 | Pa×s | 325.45 | Joback Calculated Property |
η | 0.0002842 | Pa×s | 356.33 | Joback Calculated Property |
ΔfusH | [7.07; 7.07] | kJ/mol | [138.20; 138.20] | ![]() |
ΔfusH | 7.07 | kJ/mol | 138.20 | NIST |
ΔfusH | 7.07 | kJ/mol | 138.20 | NIST |
ΔfusH | 7.07 | kJ/mol | 138.20 | NIST |
ΔvapH | [29.62; 34.80] | kJ/mol | [247.00; 359.20] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 30 31 32 33 34 35 250 300 350 | ||||
ΔvapH | 34.80 | kJ/mol | 247.00 | NIST |
ΔvapH | 33.60 | kJ/mol | 320.00 | NIST |
ΔvapH | 33.30 | kJ/mol | 322.50 | NIST |
ΔvapH | 33.20 | kJ/mol | 323.50 | NIST |
ΔvapH | 29.65 | kJ/mol | 359.20 | KDB |
ΔvapH | 29.62 | kJ/mol | 359.20 | NIST |
n0 | 1.38842 | 298.15 | KDB | |
ρl | 693.00 | kg/m3 | 293.00 | KDB |
ΔfusS | 51.14 | J/mol×K | 138.20 | NIST |
γ | 0.02 | N/m | 298.20 | KDB |
λ | [0.09; 0.11] | W/m×K | [256.11; 334.37] | ![]() |
T(K) Liquid thermal conductivity (W/m×K) 0.09 0.1 0.1 0.11 0.11 260 280 300 320 | ||||
λ | 0.11 | W/m×K | 256.11 | Thermal... |
λ | 0.11 | W/m×K | 256.71 | Thermal... |
λ | 0.11 | W/m×K | 257.04 | Thermal... |
λ | 0.11 | W/m×K | 276.17 | Thermal... |
λ | 0.11 | W/m×K | 276.50 | Thermal... |
λ | 0.11 | W/m×K | 276.78 | Thermal... |
λ | 0.10 | W/m×K | 296.01 | Thermal... |
λ | 0.10 | W/m×K | 296.03 | Thermal... |
λ | 0.10 | W/m×K | 296.39 | Thermal... |
λ | 0.10 | W/m×K | 296.63 | Thermal... |
λ | 0.10 | W/m×K | 316.38 | Thermal... |
λ | 0.09 | W/m×K | 316.67 | Thermal... |
λ | 0.09 | W/m×K | 316.93 | Thermal... |
λ | 0.09 | W/m×K | 333.75 | Thermal... |
λ | 0.09 | W/m×K | 334.10 | Thermal... |
λ | 0.09 | W/m×K | 334.37 | Thermal... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [257.53; 384.68] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42009e+01 | |||
Coefficient B | -3.13031e+03 | |||
Coefficient C | -3.25430e+01 | |||
Temperature range, min. | 257.53 | |||
Temperature range, max. | 384.68 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 257.53 | Calculated Property |
Pvap | 3.03 | kPa | 271.66 | Calculated Property |
Pvap | 6.30 | kPa | 285.79 | Calculated Property |
Pvap | 12.10 | kPa | 299.91 | Calculated Property |
Pvap | 21.77 | kPa | 314.04 | Calculated Property |
Pvap | 37.05 | kPa | 328.17 | Calculated Property |
Pvap | 60.05 | kPa | 342.30 | Calculated Property |
Pvap | 93.31 | kPa | 356.42 | Calculated Property |
Pvap | 139.75 | kPa | 370.55 | Calculated Property |
Pvap | 202.64 | kPa | 384.68 | Calculated Property |
Pvap | [2.29e-07; 2919.02] | kPa | [138.70; 536.40] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.78524e+01 | |||
Coefficient B | -6.06498e+03 | |||
Coefficient C | -8.01550e+00 | |||
Coefficient D | 6.29022e-06 | |||
Temperature range, min. | 138.70 | |||
Temperature range, max. | 536.40 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 300 400 500 | ||||
Pvap | 2.29e-07 | kPa | 138.70 | Calculated Property |
Pvap | 1.06e-03 | kPa | 182.89 | Calculated Property |
Pvap | 0.13 | kPa | 227.08 | Calculated Property |
Pvap | 2.85 | kPa | 271.27 | Calculated Property |
Pvap | 22.90 | kPa | 315.46 | Calculated Property |
Pvap | 102.52 | kPa | 359.64 | Calculated Property |
Pvap | 316.93 | kPa | 403.83 | Calculated Property |
Pvap | 768.49 | kPa | 448.02 | Calculated Property |
Pvap | 1583.06 | kPa | 492.21 | Calculated Property |
Pvap | 2919.02 | kPa | 536.40 | Calculated Property |
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