Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2020 | KDB | |
ΔcH°gas | -2709.80 ± 1.20 | kJ/mol | NIST |
μ | 0.30 | debye | KDB |
ΔfG° | 65.90 | kJ/mol | KDB |
Δc,grossH | 2687.84 | kJ/mol | KDB |
Δc,netH | 2511.781 | kJ/mol | KDB |
ΔfH°gas | [-7.70; -6.99] | kJ/mol |
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ΔfH°gas | -6.99 | kJ/mol | KDB |
ΔfH°gas | -7.70 ± 1.30 | kJ/mol | NIST |
ΔfusH° | 6.32 | kJ/mol | Joback Calculated Property |
ΔvapH° | [22.10; 22.70] | kJ/mol |
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ΔvapH° | 22.70 | kJ/mol | NIST |
ΔvapH° | 22.10 | kJ/mol | NIST |
IE | [9.07; 9.40] | eV |
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IE | 9.11 ± 0.01 | eV | NIST |
IE | 9.13 | eV | NIST |
IE | 9.13 | eV | NIST |
IE | 9.11 ± 0.02 | eV | NIST |
IE | 9.11 ± 0.01 | eV | NIST |
IE | 9.12 ± 0.02 | eV | NIST |
IE | 9.12 ± 0.01 | eV | NIST |
IE | 9.10 | eV | NIST |
IE | 9.07 | eV | NIST |
IE | 9.12 | eV | NIST |
IE | 9.12 | eV | NIST |
IE | 9.13 ± 0.01 | eV | NIST |
IE | 9.13 | eV | NIST |
IE | 9.32 ± 0.01 | eV | NIST |
IE | 9.20 | eV | NIST |
IE | 9.11 ± 0.03 | eV | NIST |
IE | Outlier 9.36 | eV | NIST |
IE | Outlier 9.40 | eV | NIST |
IE | 9.29 | eV | NIST |
log10WS | -1.35 | Crippen Calculated Property | |
logPoct/wat | 1.582 | Crippen Calculated Property | |
McVol | 62.920 | ml/mol | McGowan Calculated Property |
NFPA Fire | 4 | KDB | |
NFPA Health | 1 | KDB | |
Pc | [4197.00; 4225.50] | kPa |
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Pc | 4197.00 | kPa | KDB |
Pc | 4225.50 | kPa | Thermod... |
Pc | 4210.00 ± 50.00 | kPa | NIST |
ρc | 240.13 ± 2.81 | kg/m3 | NIST |
Inp | [411.00; 431.00] |
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|
Inp | 426.00 | NIST | |
Inp | 425.00 | NIST | |
Inp | 417.00 | NIST | |
Inp | 425.00 | NIST | |
Inp | 425.00 | NIST | |
Inp | 418.00 | NIST | |
Inp | 416.50 | NIST | |
Inp | 416.50 | NIST | |
Inp | 416.30 | NIST | |
Inp | 416.50 | NIST | |
Inp | 416.85 | NIST | |
Inp | 417.00 | NIST | |
Inp | 417.00 | NIST | |
Inp | 427.30 | NIST | |
Inp | 417.00 | NIST | |
Inp | 417.00 | NIST | |
Inp | 411.00 | NIST | |
Inp | 416.00 | NIST | |
Inp | 417.00 | NIST | |
Inp | 417.00 | NIST | |
Inp | 418.00 | NIST | |
Inp | 427.00 | NIST | |
Inp | 427.00 | NIST | |
Inp | 428.20 | NIST | |
Inp | 420.00 | NIST | |
Inp | 416.44 | NIST | |
Inp | 418.18 | NIST | |
Inp | 411.00 | NIST | |
Inp | 417.00 | NIST | |
Inp | 417.00 | NIST | |
Inp | Outlier 431.00 | NIST | |
Inp | 422.00 | NIST | |
Inp | 426.00 | NIST | |
Inp | 416.00 | NIST | |
Inp | 420.00 | NIST | |
Inp | 416.00 | NIST | |
Inp | 416.00 | NIST | |
Inp | 417.00 | NIST | |
Inp | 428.00 | NIST | |
Inp | 421.00 | NIST | |
Inp | 420.00 | NIST | |
Inp | 427.00 | NIST | |
Inp | 428.00 | NIST | |
Inp | 426.00 | NIST | |
Inp | 418.00 | NIST | |
Inp | 416.85 | NIST | |
Inp | 417.00 | NIST | |
Inp | 420.00 | NIST | |
I | [468.00; 481.00] |
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|
I | 481.00 | NIST | |
I | 468.00 | NIST | |
I | 468.00 | NIST | |
S°liquid | [212.88; 220.00] | J/mol×K |
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S°liquid | 220.00 | J/mol×K | NIST |
S°liquid | 219.91 | J/mol×K | NIST |
S°liquid | 212.88 | J/mol×K | NIST |
Tboil | [276.79; 276.90] | K |
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Tboil | 276.86 | K | KDB |
Tboil | 276.90 | K | NIST |
Tboil | 276.90 | K | NIST |
Tboil | 276.90 ± 0.50 | K | NIST |
Tboil | 276.80 ± 0.30 | K | NIST |
Tboil | 276.81 ± 0.55 | K | NIST |
Tboil | 276.79 ± 0.20 | K | NIST |
Tboil | 276.85 ± 0.60 | K | NIST |
Tc | [435.50; 435.60] | K |
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Tc | 435.58 | K | KDB |
Tc | 435.50 ± 0.10 | K | NIST |
Tc | 435.60 | K | NIST |
Tc | 435.55 ± 0.30 | K | NIST |
Tfus | [133.85; 134.20] | K |
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Tfus | 134.20 | K | KDB |
Tfus | 133.85 ± 0.50 | K | NIST |
Ttriple | [133.80; 134.26] | K |
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Ttriple | 134.26 ± 0.02 | K | NIST |
Ttriple | 134.26 ± 0.02 | K | NIST |
Ttriple | 133.80 ± 0.20 | K | NIST |
Vc | [0.234; 0.234] | m3/kmol |
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Vc | 0.234 | m3/kmol | KDB |
Vc | 0.234 | m3/kmol | NIST |
Zc | 0.2711750 | KDB | |
Zra | 0.27 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [70.80; 96.27] | J/mol×K | [250.00; 371.24] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 70 75 80 85 90 95 250 300 350 | ||||
Cp,gas | 70.80 ± 1.60 | J/mol×K | 250.00 | NIST |
Cp,gas | 71.10 ± 1.60 | J/mol×K | 255.00 | NIST |
Cp,gas | 71.70 ± 1.70 | J/mol×K | 260.00 | NIST |
Cp,gas | 72.30 ± 1.70 | J/mol×K | 265.00 | NIST |
Cp,gas | 72.90 ± 1.70 | J/mol×K | 270.00 | NIST |
Cp,gas | 73.90 ± 1.70 | J/mol×K | 275.00 | NIST |
Cp,gas | 74.70 ± 1.70 | J/mol×K | 280.00 | NIST |
Cp,gas | 75.90 ± 1.80 | J/mol×K | 285.00 | NIST |
Cp,gas | 77.20 ± 1.80 | J/mol×K | 290.00 | NIST |
Cp,gas | 78.50 ± 1.80 | J/mol×K | 295.00 | NIST |
Cp,gas | 81.13 ± 0.16 | J/mol×K | 298.58 | NIST |
Cp,gas | 79.90 ± 1.80 | J/mol×K | 300.00 | NIST |
Cp,gas | 88.24 ± 0.18 | J/mol×K | 332.85 | NIST |
Cp,gas | 96.27 ± 0.19 | J/mol×K | 371.24 | NIST |
Cp,liquid | [118.87; 130.00] | J/mol×K | [266.60; 299.80] | ![]() |
Cp,liquid | 118.87 | J/mol×K | 266.60 | NIST |
Cp,liquid | 127.00 | J/mol×K | 298.15 | NIST |
Cp,liquid | 126.15 | J/mol×K | 298.15 | NIST |
Cp,liquid | 130.00 | J/mol×K | 299.80 | NIST |
η | [0.0001436; 0.0025167] | Pa×s | [129.76; 295.08] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 150 200 250 | ||||
η | 0.0025167 | Pa×s | 129.76 | Joback Calculated Property |
η | 0.0010280 | Pa×s | 157.31 | Joback Calculated Property |
η | 0.0005483 | Pa×s | 184.87 | Joback Calculated Property |
η | 0.0003443 | Pa×s | 212.42 | Joback Calculated Property |
η | 0.0002406 | Pa×s | 239.97 | Joback Calculated Property |
η | 0.0001810 | Pa×s | 267.53 | Joback Calculated Property |
η | 0.0001436 | Pa×s | 295.08 | Joback Calculated Property |
ΔfusH | [7.31; 7.32] | kJ/mol | [133.80; 134.30] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 7.31 7.31 7.31 7.32 7.32 133.79999999999998 134 134.2 | ||||
ΔfusH | 7.32 | kJ/mol | 133.80 | NIST |
ΔfusH | 7.31 | kJ/mol | 134.26 | NIST |
ΔfusH | 7.31 | kJ/mol | 134.26 | NIST |
ΔfusH | 7.31 | kJ/mol | 134.30 | NIST |
ΔfusH | 7.31 | kJ/mol | 134.30 | NIST |
ΔvapH | [22.47; 25.30] | kJ/mol | [231.00; 407.00] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 22.5 23 23.5 24 24.5 25 25.5 250 300 350 400 | ||||
ΔvapH | 25.30 | kJ/mol | 231.00 | NIST |
ΔvapH | 22.50 | kJ/mol | 246.00 | NIST |
ΔvapH | 22.47 | kJ/mol | 246.00 | NIST |
ΔvapH | 24.40 | kJ/mol | 255.50 | NIST |
ΔvapH | 24.31 | kJ/mol | 276.73 | NIST |
ΔvapH | 23.35 | kJ/mol | 276.90 | KDB |
ΔvapH | 23.34 | kJ/mol | 276.90 | NIST |
ΔvapH | 24.00 | kJ/mol | 300.50 | NIST |
ΔvapH | 23.60 | kJ/mol | 355.00 | NIST |
ΔvapH | 23.60 | kJ/mol | 407.00 | NIST |
Pvap | [332.20; 1213.01] | kPa | [312.58; 365.43] | ![]() |
T(K) Vapor pressure (kPa) 400 600 800 1000 1200 320 340 360 | ||||
Pvap | 333.00 | kPa | 312.58 | Vapour ... |
Pvap | 332.20 | kPa | 312.59 | Isother... |
Pvap | 391.45 | kPa | 318.40 | Vapour ... |
Pvap | 561.34 | kPa | 331.92 | Vapor-L... |
Pvap | 1190.50 | kPa | 364.52 | Vapor-L... |
Pvap | 1189.60 | kPa | 364.52 | Vapor-L... |
Pvap | 1190.70 | kPa | 364.53 | Vapor-L... |
Pvap | 1213.01 | kPa | 365.43 | Vapor L... |
ρl | 621.00 | kg/m3 | 293.00 | KDB |
ΔfusS | [54.40; 54.69] | J/mol×K | [133.80; 134.26] | ![]() |
ΔfusS | 54.69 | J/mol×K | 133.80 | NIST |
ΔfusS | 54.40 | J/mol×K | 134.26 | NIST |
ΔfusS | 54.44 | J/mol×K | 134.26 | NIST |
γ | 0.01 | N/m | 293.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [199.49; 296.24] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41690e+01 | |||
Coefficient B | -2.36784e+03 | |||
Coefficient C | -2.89160e+01 | |||
Temperature range, min. | 199.49 | |||
Temperature range, max. | 296.24 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 200 250 | ||||
Pvap | 1.33 | kPa | 199.49 | Calculated Property |
Pvap | 3.04 | kPa | 210.24 | Calculated Property |
Pvap | 6.30 | kPa | 220.99 | Calculated Property |
Pvap | 12.12 | kPa | 231.74 | Calculated Property |
Pvap | 21.81 | kPa | 242.49 | Calculated Property |
Pvap | 37.10 | kPa | 253.24 | Calculated Property |
Pvap | 60.12 | kPa | 263.99 | Calculated Property |
Pvap | 93.39 | kPa | 274.74 | Calculated Property |
Pvap | 139.82 | kPa | 285.49 | Calculated Property |
Pvap | 202.64 | kPa | 296.24 | Calculated Property |
Pvap | [2.48e-04; 4205.34] | kPa | [134.26; 435.58] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.95121e+01 | |||
Coefficient B | -4.81722e+03 | |||
Coefficient C | -8.60007e+00 | |||
Coefficient D | 1.13381e-05 | |||
Temperature range, min. | 134.26 | |||
Temperature range, max. | 435.58 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 300 400 | ||||
Pvap | 2.48e-04 | kPa | 134.26 | Calculated Property |
Pvap | 0.05 | kPa | 167.74 | Calculated Property |
Pvap | 1.51 | kPa | 201.22 | Calculated Property |
Pvap | 14.44 | kPa | 234.70 | Calculated Property |
Pvap | 71.97 | kPa | 268.18 | Calculated Property |
Pvap | 238.52 | kPa | 301.66 | Calculated Property |
Pvap | 605.66 | kPa | 335.14 | Calculated Property |
Pvap | 1287.02 | kPa | 368.62 | Calculated Property |
Pvap | 2423.84 | kPa | 402.10 | Calculated Property |
Pvap | 4205.34 | kPa | 435.58 | Calculated Property |
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