Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | [-7596.50; -7439.65] | kJ/mol |
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ΔcH°liquid | -7589.90 ± 2.60 | kJ/mol | NIST |
ΔcH°liquid | -7593.00 ± 1.00 | kJ/mol | NIST |
ΔcH°liquid | -7439.65 | kJ/mol | NIST |
ΔcH°liquid | -7596.50 | kJ/mol | NIST |
ΔcH°liquid | -7537.50 ± 6.30 | kJ/mol | NIST |
ΔfG° | 99.06 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-218.40; -215.30] | kJ/mol |
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ΔfH°gas | -218.40 ± 3.10 | kJ/mol | NIST |
ΔfH°gas | -215.30 | kJ/mol | NIST |
ΔfH°liquid | [-276.40; -273.30] | kJ/mol |
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ΔfH°liquid | -276.40 ± 3.10 | kJ/mol | NIST |
ΔfH°liquid | -273.30 ± 1.20 | kJ/mol | NIST |
ΔfusH° | 10.51 | kJ/mol | Joback Calculated Property |
ΔvapH° | [57.98; 58.00] | kJ/mol |
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ΔvapH° | 57.98 | kJ/mol | NIST |
ΔvapH° | 58.00 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 58.00 | kJ/mol | NIST |
ΔvapH° | 58.00 ± 0.20 | kJ/mol | NIST |
IE | 9.41 | eV | NIST |
log10WS | -4.15 | Crippen Calculated Property | |
logPoct/wat | 4.147 | Crippen Calculated Property | |
McVol | 158.220 | ml/mol | McGowan Calculated Property |
Pc | 2603.08 | kPa | Joback Calculated Property |
Inp | [1284.00; 1327.00] |
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|
Inp | 1313.00 | NIST | |
Inp | 1324.00 | NIST | |
Inp | 1309.00 | NIST | |
Inp | 1295.00 | NIST | |
Inp | 1327.00 | NIST | |
Inp | 1284.00 | NIST | |
Inp | 1327.00 | NIST | |
Inp | 1284.00 | NIST | |
Inp | 1301.50 | NIST | |
Inp | 1301.20 | NIST | |
Inp | 1293.10 | NIST | |
Inp | 1301.50 | NIST | |
Inp | 1307.80 | NIST | |
Inp | 1304.39 | NIST | |
Inp | 1293.10 | NIST | |
Inp | 1301.50 | NIST | |
Inp | 1307.80 | NIST | |
Inp | 1301.50 | NIST | |
Inp | 1301.20 | NIST | |
Inp | 1312.00 | NIST | |
Inp | 1298.00 | NIST | |
Inp | 1313.00 | NIST | |
I | [1420.00; 1431.00] |
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|
I | 1420.00 | NIST | |
I | 1431.00 | NIST | |
Tboil | 513.06 | K | Joback Calculated Property |
Tc | 745.11 | K | Joback Calculated Property |
Tfus | 239.76 | K | Joback Calculated Property |
Ttriple | 276.90 ± 0.00 | K | NIST |
Vc | 0.574 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [385.05; 518.21] | J/mol×K | [513.06; 745.11] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 380 400 420 440 460 480 500 520 600 700 | ||||
Cp,gas | 385.05 | J/mol×K | 513.06 | Joback Calculated Property |
Cp,gas | 411.12 | J/mol×K | 551.73 | Joback Calculated Property |
Cp,gas | 435.56 | J/mol×K | 590.41 | Joback Calculated Property |
Cp,gas | 458.45 | J/mol×K | 629.08 | Joback Calculated Property |
Cp,gas | 479.81 | J/mol×K | 667.76 | Joback Calculated Property |
Cp,gas | 499.72 | J/mol×K | 706.43 | Joback Calculated Property |
Cp,gas | 518.21 | J/mol×K | 745.11 | Joback Calculated Property |
Cp,liquid | [283.00; 300.40] | J/mol×K | [298.15; 313.00] | ![]() |
Cp,liquid | 283.00 | J/mol×K | 298.15 | NIST |
Cp,liquid | 300.40 | J/mol×K | 311.00 | NIST |
Cp,liquid | 300.00 | J/mol×K | 313.00 | NIST |
η | [0.0002550; 0.0108669] | Pa×s | [239.76; 513.06] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 300 400 500 | ||||
η | 0.0108669 | Pa×s | 239.76 | Joback Calculated Property |
η | 0.0035294 | Pa×s | 285.31 | Joback Calculated Property |
η | 0.0015623 | Pa×s | 330.86 | Joback Calculated Property |
η | 0.0008424 | Pa×s | 376.41 | Joback Calculated Property |
η | 0.0005190 | Pa×s | 421.96 | Joback Calculated Property |
η | 0.0003514 | Pa×s | 467.51 | Joback Calculated Property |
η | 0.0002550 | Pa×s | 513.06 | Joback Calculated Property |
ΔfusH | [0.74; 7.08] | kJ/mol | [223.00; 277.20] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 1 2 3 4 5 6 7 240 260 | ||||
ΔfusH | 6.86 | kJ/mol | 223.00 | NIST |
ΔfusH | 1.54 | kJ/mol | 256.10 | NIST |
ΔfusH | 0.74 | kJ/mol | 267.50 | NIST |
ΔfusH | 7.08 | kJ/mol | 273.50 | NIST |
ΔfusH | 6.78 | kJ/mol | 277.20 | NIST |
ΔfusH | 6.78 | kJ/mol | 277.20 | NIST |
ΔvapH | [42.50; 53.80] | kJ/mol | [421.00; 525.00] | ![]() |
ΔvapH | 53.80 | kJ/mol | 421.00 | NIST |
ΔvapH | 50.10 | kJ/mol | 435.00 | NIST |
ΔvapH | 42.50 | kJ/mol | 525.00 | NIST |
n0 | 1.47870 | 293.15 | Density... | |
ρl | [828.60; 886.13] | kg/m3 | [293.15; 373.15] | ![]() |
T(K) Liquid Density (kg/m3) 830 840 850 860 870 880 890 300 320 340 360 | ||||
ρl | 886.05 | kg/m3 | 293.15 | Densiti... |
ρl | 886.13 | kg/m3 | 293.15 | Density... |
ρl | 882.44 | kg/m3 | 298.15 | Densiti... |
ρl | 878.93 | kg/m3 | 303.15 | Density... |
ρl | 878.84 | kg/m3 | 303.15 | Densiti... |
ρl | 875.25 | kg/m3 | 308.15 | Densiti... |
ρl | 871.66 | kg/m3 | 313.15 | Densiti... |
ρl | 871.74 | kg/m3 | 313.15 | Density... |
ρl | 868.08 | kg/m3 | 318.15 | Densiti... |
ρl | 864.50 | kg/m3 | 323.15 | Densiti... |
ρl | 864.58 | kg/m3 | 323.15 | Density... |
ρl | 860.93 | kg/m3 | 328.15 | Densiti... |
ρl | 857.35 | kg/m3 | 333.15 | Densiti... |
ρl | 857.43 | kg/m3 | 333.15 | Density... |
ρl | 850.29 | kg/m3 | 343.15 | Density... |
ρl | 843.00 | kg/m3 | 353.15 | Density... |
ρl | 835.90 | kg/m3 | 363.15 | Density... |
ρl | 828.60 | kg/m3 | 373.15 | Density... |
ΔfusS | [2.77; 25.89] | J/mol×K | [256.10; 277.20] | ![]() |
ΔfusS | 6.01 | J/mol×K | 256.10 | NIST |
ΔfusS | 2.77 | J/mol×K | 267.50 | NIST |
ΔfusS | 25.89 | J/mol×K | 273.50 | NIST |
ΔfusS | 24.46 | J/mol×K | 277.20 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 372.50 ± 0.50 | K | 1.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [374.91; 540.29] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.50496e+01 | |||
Coefficient B | -4.73244e+03 | |||
Coefficient C | -5.43230e+01 | |||
Temperature range, min. | 374.91 | |||
Temperature range, max. | 540.29 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 374.91 | Calculated Property |
Pvap | 2.97 | kPa | 393.29 | Calculated Property |
Pvap | 6.09 | kPa | 411.66 | Calculated Property |
Pvap | 11.63 | kPa | 430.04 | Calculated Property |
Pvap | 20.93 | kPa | 448.41 | Calculated Property |
Pvap | 35.73 | kPa | 466.79 | Calculated Property |
Pvap | 58.29 | kPa | 485.16 | Calculated Property |
Pvap | 91.35 | kPa | 503.54 | Calculated Property |
Pvap | 138.21 | kPa | 521.91 | Calculated Property |
Pvap | 202.64 | kPa | 540.29 | Calculated Property |
Pvap | [2.28e-03; 2535.63] | kPa | [276.78; 727.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.73446e+01 | |||
Coefficient B | -1.02483e+04 | |||
Coefficient C | -1.18827e+01 | |||
Coefficient D | 5.45803e-06 | |||
Temperature range, min. | 276.78 | |||
Temperature range, max. | 727.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 400 600 | ||||
Pvap | 2.28e-03 | kPa | 276.78 | Calculated Property |
Pvap | 0.11 | kPa | 326.80 | Calculated Property |
Pvap | 1.55 | kPa | 376.83 | Calculated Property |
Pvap | 10.62 | kPa | 426.85 | Calculated Property |
Pvap | 45.22 | kPa | 476.88 | Calculated Property |
Pvap | 139.85 | kPa | 526.90 | Calculated Property |
Pvap | 347.46 | kPa | 576.93 | Calculated Property |
Pvap | 741.46 | kPa | 626.95 | Calculated Property |
Pvap | 1422.73 | kPa | 676.98 | Calculated Property |
Pvap | 2535.63 | kPa | 727.00 | Calculated Property |
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