Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3780 | KDB | |
AP | 347.150 | K | KDB |
ΔcH°liquid | [-5465.50; -5274.60] | kJ/mol |
![]() |
ΔcH°liquid | -5465.50 ± 1.20 | kJ/mol | NIST |
ΔcH°liquid | -5447.10 | kJ/mol | NIST |
ΔcH°liquid | -5274.60 | kJ/mol | NIST |
ΔfG° | 12.77 | kJ/mol | KDB |
Δc,grossH | 5465.48 | kJ/mol | KDB |
Δc,netH | 5069.335 | kJ/mol | KDB |
ΔfH°gas | [-215.60; -215.50] | kJ/mol |
![]() |
ΔfH°gas | -215.60 | kJ/mol | KDB |
ΔfH°gas | -215.50 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | -255.20 ± 1.30 | kJ/mol | NIST |
ΔfusH° | 12.95 | kJ/mol | Joback Calculated Property |
ΔvapH° | [33.00; 39.80] | kJ/mol |
![]() |
ΔvapH° | 39.72 | kJ/mol | NIST |
ΔvapH° | 39.70 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 39.70 | kJ/mol | NIST |
ΔvapH° | 39.80 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 39.67 | kJ/mol | NIST |
ΔvapH° | Outlier 33.00 | kJ/mol | NIST |
IE | [9.74; 9.84] | eV |
![]() |
IE | 9.84 ± 0.10 | eV | NIST |
IE | 9.76 | eV | NIST |
IE | 9.84 ± 0.10 | eV | NIST |
IE | 9.74 ± 0.15 | eV | NIST |
log10WS | [-5.08; -5.08] |
![]() |
|
log10WS | -5.08 | Aq. Sol... | |
log10WS | -5.08 | Estimat... | |
logPoct/wat | 3.223 | Crippen Calculated Property | |
McVol | 123.580 | ml/mol | McGowan Calculated Property |
Pc | [2484.20; 2500.00] | kPa |
![]() |
Pc | 2500.00 | kPa | KDB |
Pc | 2500.00 ± 20.00 | kPa | NIST |
Pc | 2500.00 ± 40.00 | kPa | NIST |
Pc | 2484.20 ± 40.53 | kPa | NIST |
ρc | [234.17; 234.17] | kg/m3 |
![]() |
ρc | 234.17 ± 2.28 | kg/m3 | NIST |
ρc | 234.17 ± 4.57 | kg/m3 | NIST |
Inp | [754.00; 778.00] |
![]() |
|
Inp | 765.50 | NIST | |
Inp | 765.80 | NIST | |
Inp | 765.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.30 | NIST | |
Inp | 765.00 | NIST | |
Inp | 767.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 764.70 | NIST | |
Inp | 765.60 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.20 | NIST | |
Inp | 766.30 | NIST | |
Inp | 766.30 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 766.50 | NIST | |
Inp | 766.40 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | Outlier 754.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 765.20 | NIST | |
Inp | 764.90 | NIST | |
Inp | 765.00 | NIST | |
Inp | 764.60 | NIST | |
Inp | 764.60 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | Outlier 772.52 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 764.80 | NIST | |
Inp | 767.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.10 | NIST | |
Inp | 764.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 764.50 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 761.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 764.10 | NIST | |
Inp | 769.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | Outlier 778.00 | NIST | |
Inp | 766.90 | NIST | |
Inp | 761.38 | NIST | |
Inp | 761.79 | NIST | |
Inp | 762.50 | NIST | |
Inp | 764.10 | NIST | |
Inp | 761.00 | NIST | |
Inp | 761.10 | NIST | |
Inp | 762.25 | NIST | |
Inp | 762.36 | NIST | |
Inp | 763.00 | NIST | |
Inp | 763.03 | NIST | |
Inp | 763.50 | NIST | |
Inp | 763.00 | NIST | |
Inp | 765.90 | NIST | |
Inp | 765.50 | NIST | |
Inp | 765.50 | NIST | |
Inp | 766.78 | NIST | |
Inp | 766.99 | NIST | |
Inp | 767.12 | NIST | |
Inp | 765.99 | NIST | |
Inp | 766.21 | NIST | |
Inp | 766.26 | NIST | |
Inp | 761.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | Outlier 776.21 | NIST | |
Inp | 764.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | Outlier 756.00 | NIST | |
Inp | 767.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 767.00 | NIST | |
Inp | 764.30 | NIST | |
Inp | 765.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | Outlier 775.00 | NIST | |
Inp | 767.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 759.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 768.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | Outlier 758.54 | NIST | |
Inp | 764.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 761.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | Outlier 775.00 | NIST | |
Inp | Outlier 772.00 | NIST | |
Inp | 770.00 | NIST | |
Inp | Outlier 772.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 766.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 764.10 | NIST | |
Inp | 759.00 | NIST | |
Inp | Outlier 772.00 | NIST | |
I | [750.00; 764.00] |
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|
I | 750.00 | NIST | |
I | 764.00 | NIST | |
I | 764.00 | NIST | |
S°gas | 459.49 ± 0.88 | J/mol×K | NIST |
S°liquid | 356.39 | J/mol×K | NIST |
Tboil | [389.15; 391.60] | K |
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Tboil | 390.81 | K | KDB |
Tboil | 390.80 | K | NIST |
Tboil | 390.80 | K | NIST |
Tboil | 391.00 ± 3.00 | K | NIST |
Tboil | 390.00 ± 3.00 | K | NIST |
Tboil | 391.00 ± 2.00 | K | NIST |
Tboil | 390.80 ± 0.20 | K | NIST |
Tboil | Outlier 391.60 ± 2.00 | K | NIST |
Tboil | 390.79 ± 0.10 | K | NIST |
Tboil | 390.40 ± 0.30 | K | NIST |
Tboil | 390.85 ± 0.20 | K | NIST |
Tboil | 390.78 ± 0.20 | K | NIST |
Tboil | 390.55 ± 0.50 | K | NIST |
Tboil | 390.85 ± 0.30 | K | NIST |
Tboil | 391.00 ± 0.30 | K | NIST |
Tboil | 390.86 ± 0.20 | K | NIST |
Tboil | 390.90 ± 0.15 | K | NIST |
Tboil | 390.90 ± 0.20 | K | NIST |
Tboil | 390.79 ± 0.01 | K | NIST |
Tboil | 390.90 ± 0.20 | K | NIST |
Tboil | 390.85 ± 0.20 | K | NIST |
Tboil | 390.75 ± 0.50 | K | NIST |
Tboil | 390.15 ± 1.00 | K | NIST |
Tboil | 390.15 ± 1.50 | K | NIST |
Tboil | 390.00 ± 3.00 | K | NIST |
Tboil | 390.85 ± 0.10 | K | NIST |
Tboil | 390.80 ± 0.30 | K | NIST |
Tboil | 390.79 ± 0.10 | K | NIST |
Tboil | 391.15 ± 0.30 | K | NIST |
Tboil | 391.25 ± 0.30 | K | NIST |
Tboil | 389.85 ± 0.50 | K | NIST |
Tboil | Outlier 389.75 ± 0.60 | K | NIST |
Tboil | 390.35 ± 0.60 | K | NIST |
Tboil | 390.35 ± 0.50 | K | NIST |
Tboil | 391.00 ± 1.00 | K | NIST |
Tboil | 390.65 ± 1.50 | K | NIST |
Tboil | Outlier 389.15 ± 0.30 | K | NIST |
Tboil | 390.90 ± 1.00 | K | NIST |
Tboil | 391.15 ± 1.00 | K | NIST |
Tc | [559.56; 559.70] | K |
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Tc | 559.70 | K | KDB |
Tc | 559.70 ± 0.10 | K | NIST |
Tc | 559.70 ± 0.20 | K | NIST |
Tc | 559.60 | K | NIST |
Tc | 559.56 ± 0.40 | K | NIST |
Tc | 559.57 ± 0.20 | K | NIST |
Tfus | [160.00; 165.52] | K |
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Tfus | 164.16 | K | KDB |
Tfus | 165.52 | K | Aq. Sol... |
Tfus | 163.59 ± 0.20 | K | NIST |
Tfus | 163.59 ± 0.30 | K | NIST |
Tfus | 163.52 ± 0.20 | K | NIST |
Tfus | 163.52 ± 0.30 | K | NIST |
Tfus | 163.90 ± 0.02 | K | NIST |
Tfus | 164.02 ± 0.09 | K | NIST |
Tfus | 164.03 ± 0.06 | K | NIST |
Tfus | 164.11 ± 0.05 | K | NIST |
Tfus | 163.32 ± 0.15 | K | NIST |
Tfus | 163.55 ± 0.50 | K | NIST |
Tfus | 163.65 ± 0.10 | K | NIST |
Tfus | Outlier 160.00 ± 0.30 | K | NIST |
Tfus | 162.15 ± 2.00 | K | NIST |
Tfus | 161.85 ± 1.50 | K | NIST |
Ttriple | [154.87; 164.19] | K |
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Ttriple | 164.18 ± 0.04 | K | NIST |
Ttriple | 164.19 ± 0.01 | K | NIST |
Ttriple | 163.15 ± 0.02 | K | NIST |
Ttriple | 164.14 ± 0.02 | K | NIST |
Ttriple | 164.14 ± 0.02 | K | NIST |
Ttriple | 164.14 ± 0.40 | K | NIST |
Ttriple | 154.91 ± 0.02 | K | NIST |
Ttriple | 154.87 ± 0.04 | K | NIST |
Ttriple | 154.91 ± 0.03 | K | NIST |
Ttriple | 154.87 ± 0.05 | K | NIST |
Vc | [0.488; 0.488] | m3/kmol |
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Vc | 0.488 | m3/kmol | KDB |
Vc | 0.488 | m3/kmol | NIST |
Zc | 0.2621610 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [186.13; 265.52] | J/mol×K | [298.15; 448.15] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 180 200 220 240 260 300 350 400 450 | ||||
Cp,gas | 186.13 | J/mol×K | 298.15 | NIST |
Cp,gas | 202.07 | J/mol×K | 323.15 | NIST |
Cp,gas | 230.06 | J/mol×K | 373.15 | NIST |
Cp,gas | 248.37 | J/mol×K | 408.15 | NIST |
Cp,gas | 265.52 | J/mol×K | 448.15 | NIST |
Cp,liquid | [251.58; 252.00] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 252.00 | J/mol×K | 298.15 | NIST |
Cp,liquid | 251.58 | J/mol×K | 298.15 | NIST |
η | [0.0002373; 0.0105616] | Pa×s | [164.92; 382.00] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 200 250 300 350 | ||||
η | 0.0105616 | Pa×s | 164.92 | Joback Calculated Property |
η | 0.0031758 | Pa×s | 201.10 | Joback Calculated Property |
η | 0.0013776 | Pa×s | 237.28 | Joback Calculated Property |
η | 0.0007454 | Pa×s | 273.46 | Joback Calculated Property |
η | 0.0004656 | Pa×s | 309.64 | Joback Calculated Property |
η | 0.0003209 | Pa×s | 345.82 | Joback Calculated Property |
η | 0.0002373 | Pa×s | 382.00 | Joback Calculated Property |
ΔfusH | [11.92; 11.92] | kJ/mol | [64.19; 164.20] | ![]() |
ΔfusH | 11.92 | kJ/mol | 64.19 | NIST |
ΔfusH | 11.92 | kJ/mol | 164.20 | NIST |
ΔfusH | 11.92 | kJ/mol | 164.20 | NIST |
ΔvapH | [33.26; 41.60] | kJ/mol | [258.00; 390.80] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 34 36 38 40 42 300 350 | ||||
ΔvapH | 41.60 | kJ/mol | 258.00 | NIST |
ΔvapH | 38.70 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 37.30 ± 0.10 | kJ/mol | 333.00 | NIST |
ΔvapH | 39.80 | kJ/mol | 338.50 | NIST |
ΔvapH | 36.00 ± 0.10 | kJ/mol | 353.00 | NIST |
ΔvapH | 38.10 | kJ/mol | 353.00 | NIST |
ΔvapH | 33.81 | kJ/mol | 390.80 | KDB |
ΔvapH | 33.26 | kJ/mol | 390.80 | NIST |
n0 | 1.39257 | 298.15 | KDB | |
ρl | 702.00 | kg/m3 | 289.00 | KDB |
ΔfusS | 72.60 | J/mol×K | 64.19 | NIST |
γ | 0.02 | N/m | 298.20 | KDB |
λ | [0.11; 0.12] | W/m×K | [259.12; 328.23] | ![]() |
T(K) Liquid thermal conductivity (W/m×K) 0.11 0.11 0.12 0.12 0.13 260 280 300 320 | ||||
λ | 0.12 | W/m×K | 259.12 | Thermal... |
λ | 0.12 | W/m×K | 259.33 | Thermal... |
λ | 0.12 | W/m×K | 259.51 | Thermal... |
λ | 0.12 | W/m×K | 277.53 | Thermal... |
λ | 0.12 | W/m×K | 277.77 | Thermal... |
λ | 0.12 | W/m×K | 277.96 | Thermal... |
λ | 0.11 | W/m×K | 295.72 | Thermal... |
λ | 0.11 | W/m×K | 295.95 | Thermal... |
λ | 0.11 | W/m×K | 296.16 | Thermal... |
λ | 0.11 | W/m×K | 313.83 | Thermal... |
λ | 0.11 | W/m×K | 314.07 | Thermal... |
λ | 0.11 | W/m×K | 314.30 | Thermal... |
λ | 0.11 | W/m×K | 327.74 | Thermal... |
λ | 0.11 | W/m×K | 328.00 | Thermal... |
λ | 0.11 | W/m×K | 328.23 | Thermal... |
Vm | [1.63e-04; 1.64e-04] | m3/mol | [288.05; 298.15] | ![]() |
Vm | 1.63e-04 | m3/mol | 288.05 | Thermod... |
Vm | 1.64e-04 | m3/mol | 298.15 | Thermod... |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 389.20 | K | 101.00 | NIST |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
293.15 | 100.00 | 236.20 |
293.15 | 5000.00 | 233.80 |
293.15 | 10000.00 | 231.70 |
293.15 | 15000.00 | 229.10 |
293.15 | 20000.00 | 228.00 |
293.15 | 25000.00 | 224.80 |
313.15 | 100.00 | 249.60 |
313.15 | 5000.00 | 246.80 |
313.15 | 10000.00 | 245.10 |
313.15 | 15000.00 | 243.20 |
313.15 | 20000.00 | 240.80 |
313.15 | 25000.00 | 235.10 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
298.15 | 100.00 | 693.9 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [284.25; 417.28] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43957e+01 | |||
Coefficient B | -3.39364e+03 | |||
Coefficient C | -4.37100e+01 | |||
Temperature range, min. | 284.25 | |||
Temperature range, max. | 417.28 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 284.25 | Calculated Property |
Pvap | 3.02 | kPa | 299.03 | Calculated Property |
Pvap | 6.24 | kPa | 313.81 | Calculated Property |
Pvap | 11.98 | kPa | 328.59 | Calculated Property |
Pvap | 21.56 | kPa | 343.37 | Calculated Property |
Pvap | 36.72 | kPa | 358.16 | Calculated Property |
Pvap | 59.61 | kPa | 372.94 | Calculated Property |
Pvap | 92.83 | kPa | 387.72 | Calculated Property |
Pvap | 139.37 | kPa | 402.50 | Calculated Property |
Pvap | 202.63 | kPa | 417.28 | Calculated Property |
Pvap | [1.04e-06; 2474.20] | kPa | [164.16; 559.64] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.36210e+01 | |||
Coefficient B | -7.47230e+03 | |||
Coefficient C | -1.02064e+01 | |||
Coefficient D | 6.78071e-06 | |||
Temperature range, min. | 164.16 | |||
Temperature range, max. | 559.64 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 200 300 400 500 | ||||
Pvap | 1.04e-06 | kPa | 164.16 | Calculated Property |
Pvap | 1.54e-03 | kPa | 208.10 | Calculated Property |
Pvap | 0.13 | kPa | 252.04 | Calculated Property |
Pvap | 2.44 | kPa | 295.99 | Calculated Property |
Pvap | 18.77 | kPa | 339.93 | Calculated Property |
Pvap | 83.36 | kPa | 383.87 | Calculated Property |
Pvap | 259.37 | kPa | 427.81 | Calculated Property |
Pvap | 636.04 | kPa | 471.76 | Calculated Property |
Pvap | 1326.32 | kPa | 515.70 | Calculated Property |
Pvap | 2474.20 | kPa | 559.64 | Calculated Property |
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