Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 257.58 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 183.23 | kJ/mol | Joback Calculated Property |
ΔfusH° | 12.03 | kJ/mol | Fusion ... |
ΔvapH° | 47.68 | kJ/mol | Joback Calculated Property |
log10WS | -1.65 | Crippen Calculated Property | |
logPoct/wat | 1.204 | Crippen Calculated Property | |
McVol | 84.070 | ml/mol | McGowan Calculated Property |
Pc | 3272.78 | kPa | Joback Calculated Property |
S°liquid | 239.45 | J/mol×K | NIST |
Tboil | [559.20; 559.35] | K |
![]() |
Tboil | 559.20 | K | NIST |
Tboil | 559.35 ± 3.00 | K | NIST |
Tc | 729.38 | K | Joback Calculated Property |
Tfus | 243.60 ± 0.60 | K | NIST |
Ttriple | 244.21 ± 0.02 | K | NIST |
Vc | 0.367 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [167.81; 201.25] | J/mol×K | [517.96; 729.38] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 165 170 175 180 185 190 195 200 550 600 650 700 | ||||
Cp,gas | 167.81 | J/mol×K | 517.96 | Joback Calculated Property |
Cp,gas | 174.14 | J/mol×K | 553.20 | Joback Calculated Property |
Cp,gas | 180.15 | J/mol×K | 588.43 | Joback Calculated Property |
Cp,gas | 185.86 | J/mol×K | 623.67 | Joback Calculated Property |
Cp,gas | 191.28 | J/mol×K | 658.91 | Joback Calculated Property |
Cp,gas | 196.41 | J/mol×K | 694.14 | Joback Calculated Property |
Cp,gas | 201.25 | J/mol×K | 729.38 | Joback Calculated Property |
Cp,liquid | 186.26 | J/mol×K | 298.15 | NIST |
ΔfusH | [12.03; 12.59] | kJ/mol | [242.00; 244.21] | ![]() |
ΔfusH | 12.03 | kJ/mol | 242.00 | NIST |
ΔfusH | 12.59 | kJ/mol | 244.20 | NIST |
ΔfusH | 12.59 | kJ/mol | 244.20 | NIST |
ΔfusH | 12.59 | kJ/mol | 244.21 | NIST |
ΔvapH | [60.10; 66.80] | kJ/mol | [290.00; 462.00] | ![]() |
ΔvapH | 66.80 | kJ/mol | 290.00 | NIST |
ΔvapH | 60.10 | kJ/mol | 462.00 | NIST |
ΔfusS | 51.53 | J/mol×K | 244.21 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [416.49; 592.71] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.60720e+01 | |||
Coefficient B | -5.95750e+03 | |||
Coefficient C | -3.90620e+01 | |||
Temperature range, min. | 416.49 | |||
Temperature range, max. | 592.71 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
Pvap | 1.33 | kPa | 416.49 | Calculated Property |
Pvap | 2.90 | kPa | 436.07 | Calculated Property |
Pvap | 5.88 | kPa | 455.65 | Calculated Property |
Pvap | 11.17 | kPa | 475.23 | Calculated Property |
Pvap | 20.09 | kPa | 494.81 | Calculated Property |
Pvap | 34.42 | kPa | 514.39 | Calculated Property |
Pvap | 56.51 | kPa | 533.97 | Calculated Property |
Pvap | 89.35 | kPa | 553.55 | Calculated Property |
Pvap | 136.60 | kPa | 573.13 | Calculated Property |
Pvap | 202.67 | kPa | 592.71 | Calculated Property |
Pvap | [2.35e-06; 3192.63] | kPa | [244.21; 782.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.90371e+01 | |||
Coefficient B | -1.13046e+04 | |||
Coefficient C | -1.20138e+01 | |||
Coefficient D | 5.75911e-06 | |||
Temperature range, min. | 244.21 | |||
Temperature range, max. | 782.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 400 600 | ||||
Pvap | 2.35e-06 | kPa | 244.21 | Calculated Property |
Pvap | 1.83e-03 | kPa | 303.96 | Calculated Property |
Pvap | 0.12 | kPa | 363.72 | Calculated Property |
Pvap | 2.03 | kPa | 423.47 | Calculated Property |
Pvap | 15.44 | kPa | 483.23 | Calculated Property |
Pvap | 71.07 | kPa | 542.98 | Calculated Property |
Pvap | 236.90 | kPa | 602.74 | Calculated Property |
Pvap | 638.49 | kPa | 662.49 | Calculated Property |
Pvap | 1495.04 | kPa | 722.25 | Calculated Property |
Pvap | 3192.63 | kPa | 782.00 | Calculated Property |
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