Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -4887.00 ± 3.00 | kJ/mol | NIST |
ΔfG° | 84.36 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 57.00 ± 3.00 | kJ/mol | NIST |
ΔfH°liquid | 24.00 ± 3.00 | kJ/mol | NIST |
ΔfusH° | 5.48 | kJ/mol | Joback Calculated Property |
ΔvapH° | 33.00 | kJ/mol | NIST |
IE | [8.90; 9.10] | eV |
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IE | 8.90 | eV | NIST |
IE | 9.10 ± 0.10 | eV | NIST |
log10WS | -2.77 | Crippen Calculated Property | |
logPoct/wat | 2.673 | Crippen Calculated Property | |
McVol | 104.120 | ml/mol | McGowan Calculated Property |
Pc | 3782.33 | kPa | Joback Calculated Property |
Inp | [923.00; 923.00] |
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|
Inp | 923.00 | NIST | |
Inp | 923.00 | NIST | |
I | [1164.00; 1164.00] |
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|
I | 1164.00 | NIST | |
I | 1164.00 | NIST | |
S°liquid | [250.00; 264.30] | J/mol×K |
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S°liquid | 250.00 | J/mol×K | NIST |
S°liquid | 264.30 | J/mol×K | NIST |
Tboil | [422.00; 422.70] | K |
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Tboil | 422.70 | K | NIST |
Tboil | 422.00 ± 3.00 | K | NIST |
Tc | 637.21 | K | Joback Calculated Property |
Tfus | [201.00; 204.00] | K |
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Tfus | 203.80 ± 0.06 | K | NIST |
Tfus | 204.00 ± 4.00 | K | NIST |
Tfus | 201.00 ± 4.00 | K | NIST |
Ttriple | 203.98 ± 0.02 | K | NIST |
Vc | 0.373 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [183.96; 270.98] | J/mol×K | [413.52; 637.21] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 180 200 220 240 260 450 500 550 600 | ||||
Cp,gas | 183.96 | J/mol×K | 413.52 | Joback Calculated Property |
Cp,gas | 200.71 | J/mol×K | 450.80 | Joback Calculated Property |
Cp,gas | 216.53 | J/mol×K | 488.08 | Joback Calculated Property |
Cp,gas | 231.45 | J/mol×K | 525.37 | Joback Calculated Property |
Cp,gas | 245.48 | J/mol×K | 562.65 | Joback Calculated Property |
Cp,gas | 258.65 | J/mol×K | 599.93 | Joback Calculated Property |
Cp,gas | 270.98 | J/mol×K | 637.21 | Joback Calculated Property |
Cp,liquid | [198.90; 208.10] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 198.90 | J/mol×K | 298.15 | NIST |
Cp,liquid | 208.10 | J/mol×K | 298.15 | NIST |
η | [0.0002081; 0.0291355] | Pa×s | [186.02; 413.52] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-3 0.01 0.02 0.02 0.03 0.03 200 300 400 | ||||
η | 0.0291355 | Pa×s | 186.02 | Joback Calculated Property |
η | 0.0063666 | Pa×s | 223.94 | Joback Calculated Property |
η | 0.0021612 | Pa×s | 261.85 | Joback Calculated Property |
η | 0.0009642 | Pa×s | 299.77 | Joback Calculated Property |
η | 0.0005156 | Pa×s | 337.69 | Joback Calculated Property |
η | 0.0003129 | Pa×s | 375.60 | Joback Calculated Property |
η | 0.0002081 | Pa×s | 413.52 | Joback Calculated Property |
ΔfusH | [-0.38; 9.83] | kJ/mol | [194.40; 204.00] | ![]() |
ΔfusH | -0.38 | kJ/mol | 194.40 | NIST |
ΔfusH | 9.83 | kJ/mol | 204.00 | NIST |
ΔfusS | 48.20 | J/mol×K | 194.40 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [308.68; 450.95] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.44781e+01 | |||
Coefficient B | -3.68378e+03 | |||
Coefficient C | -4.90830e+01 | |||
Temperature range, min. | 308.68 | |||
Temperature range, max. | 450.95 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 308.68 | Calculated Property |
Pvap | 3.01 | kPa | 324.49 | Calculated Property |
Pvap | 6.22 | kPa | 340.30 | Calculated Property |
Pvap | 11.94 | kPa | 356.10 | Calculated Property |
Pvap | 21.48 | kPa | 371.91 | Calculated Property |
Pvap | 36.59 | kPa | 387.72 | Calculated Property |
Pvap | 59.44 | kPa | 403.53 | Calculated Property |
Pvap | 92.64 | kPa | 419.33 | Calculated Property |
Pvap | 139.23 | kPa | 435.14 | Calculated Property |
Pvap | 202.64 | kPa | 450.95 | Calculated Property |
Pvap | [9.35e-05; 3842.26] | kPa | [203.98; 645.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.11397e+01 | |||
Coefficient B | -7.59295e+03 | |||
Coefficient C | -8.15275e+00 | |||
Coefficient D | 3.91389e-06 | |||
Temperature range, min. | 203.98 | |||
Temperature range, max. | 645.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 400 600 | ||||
Pvap | 9.35e-05 | kPa | 203.98 | Calculated Property |
Pvap | 0.02 | kPa | 252.98 | Calculated Property |
Pvap | 0.82 | kPa | 301.98 | Calculated Property |
Pvap | 9.09 | kPa | 350.99 | Calculated Property |
Pvap | 51.23 | kPa | 399.99 | Calculated Property |
Pvap | 186.56 | kPa | 448.99 | Calculated Property |
Pvap | 507.71 | kPa | 497.99 | Calculated Property |
Pvap | 1131.24 | kPa | 547.00 | Calculated Property |
Pvap | 2190.97 | kPa | 596.00 | Calculated Property |
Pvap | 3842.26 | kPa | 645.00 | Calculated Property |
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