Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -44.67 | kJ/mol | KDB |
ΔfH°gas | -546.30 | kJ/mol | KDB |
ΔfusH° | 39.40 | kJ/mol | Heat ca... |
ΔvapH° | 112.50 ± 0.50 | kJ/mol | NIST |
log10WS | -6.20 | Crippen Calculated Property | |
logPoct/wat | 5.850 | Crippen Calculated Property | |
McVol | 256.260 | ml/mol | McGowan Calculated Property |
Pc | 1500.00 | kPa | KDB |
Inp | [1941.00; 1993.10] |
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|
Inp | 1979.00 | NIST | |
Inp | 1974.00 | NIST | |
Inp | 1986.00 | NIST | |
Inp | 1941.00 | NIST | |
Inp | 1975.00 | NIST | |
Inp | 1960.00 | NIST | |
Inp | 1993.10 | NIST | |
Inp | 1968.00 | NIST | |
Inp | 1960.00 | NIST | |
Inp | 1960.00 | NIST | |
Inp | 1982.00 | NIST | |
Inp | 1949.00 | NIST | |
Inp | 1993.00 | NIST | |
Inp | 1941.00 | NIST | |
Inp | 1993.00 | NIST | |
I | [2445.00; 2524.00] |
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I | 2445.00 | NIST | |
I | 2482.00 | NIST | |
I | 2524.00 | NIST | |
I | 2496.00 | NIST | |
I | 2475.00 | NIST | |
I | 2475.00 | NIST | |
I | 2451.00 | NIST | |
I | 2498.00 | NIST | |
I | 2475.00 | NIST | |
I | 2498.00 | NIST | |
Tboil | [581.20; 606.00] | K |
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Tboil | 606.00 | K | KDB |
Tboil | 581.20 | K | NIST |
Tc | 780.00 | K | KDB |
Tfus | [325.30; 327.15] | K |
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Tfus | 326.90 | K | KDB |
Tfus | 325.30 | K | Evaluat... |
Tfus | 327.15 ± 0.40 | K | NIST |
Vc | 1.006 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [749.49; 843.94] | J/mol×K | [680.54; 841.88] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 760 780 800 820 840 700 750 800 | ||||
Cp,gas | 749.49 | J/mol×K | 680.54 | Joback Calculated Property |
Cp,gas | 766.98 | J/mol×K | 707.43 | Joback Calculated Property |
Cp,gas | 783.74 | J/mol×K | 734.32 | Joback Calculated Property |
Cp,gas | 799.79 | J/mol×K | 761.21 | Joback Calculated Property |
Cp,gas | 815.16 | J/mol×K | 788.10 | Joback Calculated Property |
Cp,gas | 829.86 | J/mol×K | 814.99 | Joback Calculated Property |
Cp,gas | 843.94 | J/mol×K | 841.88 | Joback Calculated Property |
Cp,liquid | 649.60 | J/mol×K | 333.15 | NIST |
η | [0.0000343; 0.0067109] | Pa×s | [342.17; 680.54] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 7.00e-3 400 500 600 | ||||
η | 0.0067109 | Pa×s | 342.17 | Joback Calculated Property |
η | 0.0014953 | Pa×s | 398.56 | Joback Calculated Property |
η | 0.0004834 | Pa×s | 454.96 | Joback Calculated Property |
η | 0.0002005 | Pa×s | 511.36 | Joback Calculated Property |
η | 0.0000990 | Pa×s | 567.75 | Joback Calculated Property |
η | 0.0000556 | Pa×s | 624.14 | Joback Calculated Property |
η | 0.0000343 | Pa×s | 680.54 | Joback Calculated Property |
ΔfusH | [37.00; 63.06] | kJ/mol | [326.60; 327.30] | ![]() |
ΔfusH | 37.00 | kJ/mol | 326.60 | NIST |
ΔfusH | 37.00 | kJ/mol | 326.60 | NIST |
ΔfusH | 63.06 | kJ/mol | 327.30 | NIST |
ΔvapH | [60.67; 78.30] | kJ/mol | [540.00; 597.00] | ![]() |
ΔvapH | 78.30 | kJ/mol | 540.00 | NIST |
ΔvapH | 75.90 | kJ/mol | 548.00 | NIST |
ΔvapH | 60.67 | kJ/mol | 597.00 | KDB |
ρl | 848.00 | kg/m3 | 327.00 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [467.92; 634.46] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.61609e+01 | |||
Coefficient B | -5.70883e+03 | |||
Coefficient C | -1.08270e+02 | |||
Temperature range, min. | 467.92 | |||
Temperature range, max. | 634.46 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 500 550 600 | ||||
Pvap | 1.33 | kPa | 467.92 | Calculated Property |
Pvap | 2.90 | kPa | 486.42 | Calculated Property |
Pvap | 5.86 | kPa | 504.93 | Calculated Property |
Pvap | 11.13 | kPa | 523.43 | Calculated Property |
Pvap | 20.02 | kPa | 541.94 | Calculated Property |
Pvap | 34.31 | kPa | 560.44 | Calculated Property |
Pvap | 56.37 | kPa | 578.95 | Calculated Property |
Pvap | 89.18 | kPa | 597.45 | Calculated Property |
Pvap | 136.46 | kPa | 615.96 | Calculated Property |
Pvap | 202.66 | kPa | 634.46 | Calculated Property |
Pvap | [3.43e-05; 1457.44] | kPa | [327.05; 770.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.32218e+02 | |||
Coefficient B | -2.23722e+04 | |||
Coefficient C | -3.02228e+01 | |||
Coefficient D | 8.42167e-06 | |||
Temperature range, min. | 327.05 | |||
Temperature range, max. | 770.00 | |||
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 1400 1600 400 500 600 700 | ||||
Pvap | 3.43e-05 | kPa | 327.05 | Calculated Property |
Pvap | 5.10e-03 | kPa | 376.27 | Calculated Property |
Pvap | 0.17 | kPa | 425.48 | Calculated Property |
Pvap | 2.08 | kPa | 474.70 | Calculated Property |
Pvap | 13.37 | kPa | 523.92 | Calculated Property |
Pvap | 54.68 | kPa | 573.13 | Calculated Property |
Pvap | 163.05 | kPa | 622.35 | Calculated Property |
Pvap | 389.38 | kPa | 671.57 | Calculated Property |
Pvap | 795.42 | kPa | 720.78 | Calculated Property |
Pvap | 1457.44 | kPa | 770.00 | Calculated Property |
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