Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -3163.50 ± 1.30 | kJ/mol | NIST |
ΔfG° | -7.94 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -115.50 | kJ/mol | Joback Calculated Property |
ΔfH°liquid | -200.50 ± 1.60 | kJ/mol | NIST |
ΔfusH° | 18.64 | kJ/mol | Joback Calculated Property |
ΔvapH° | 59.80 ± 2.10 | kJ/mol | NIST |
log10WS | -1.69 | Crippen Calculated Property | |
logPoct/wat | 2.197 | Crippen Calculated Property | |
McVol | 108.050 | ml/mol | McGowan Calculated Property |
Pc | 3633.35 | kPa | Joback Calculated Property |
Inp | [1123.80; 1183.00] |
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Inp | 1178.00 | NIST | |
Inp | 1177.00 | NIST | |
Inp | 1177.07 | NIST | |
Inp | 1177.07 | NIST | |
Inp | 1173.25 | NIST | |
Inp | 1173.59 | NIST | |
Inp | 1136.00 | NIST | |
Inp | 1175.50 | NIST | |
Inp | 1124.00 | NIST | |
Inp | 1172.70 | NIST | |
Inp | 1123.80 | NIST | |
Inp | 1124.80 | NIST | |
Inp | 1172.70 | NIST | |
Inp | 1174.10 | NIST | |
Inp | 1178.00 | NIST | |
Inp | 1183.00 | NIST | |
Inp | 1131.00 | NIST | |
Inp | 1175.00 | NIST | |
Inp | 1178.00 | NIST | |
Inp | 1131.00 | NIST | |
Inp | 1124.00 | NIST | |
Inp | 1124.00 | NIST | |
Inp | 1178.00 | NIST | |
Inp | 1175.00 | NIST | |
Inp | 1173.59 | NIST | |
Inp | 1123.80 | NIST | |
I | [1820.00; 1820.00] |
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I | 1820.00 | NIST | |
I | 1820.00 | NIST | |
Tboil | 489.20 | K | NIST |
Tc | 641.96 | K | Joback Calculated Property |
Tfus | 229.08 | K | Joback Calculated Property |
Vc | 0.411 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [180.38; 223.12] | J/mol×K | [434.56; 641.96] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 450 500 550 600 | ||||
Cp,gas | 180.38 | J/mol×K | 434.56 | Joback Calculated Property |
Cp,gas | 188.42 | J/mol×K | 469.13 | Joback Calculated Property |
Cp,gas | 196.08 | J/mol×K | 503.69 | Joback Calculated Property |
Cp,gas | 203.38 | J/mol×K | 538.26 | Joback Calculated Property |
Cp,gas | 210.31 | J/mol×K | 572.82 | Joback Calculated Property |
Cp,gas | 216.89 | J/mol×K | 607.39 | Joback Calculated Property |
Cp,gas | 223.12 | J/mol×K | 641.96 | Joback Calculated Property |
ΔsubH | [77.20; 80.90] | kJ/mol | [270.50; 275.00] | ![]() |
ΔsubH | 80.90 | kJ/mol | 270.50 | NIST |
ΔsubH | 77.20 | kJ/mol | 275.00 | NIST |
ΔvapH | [50.30; 59.60] | kJ/mol | [323.00; 373.00] | ![]() |
ΔvapH | 59.60 | kJ/mol | 323.00 | NIST |
ΔvapH | 50.30 | kJ/mol | 373.00 | NIST |
Psub | [2.77e-05; 4.81e-03] | kPa | [248.15; 286.15] | ![]() |
T(K) Sublimation pressure (kPa) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 250 260 270 280 | ||||
Psub | 2.77e-05 | kPa | 248.15 | Vapor P... |
Psub | 5.60e-05 | kPa | 253.15 | Vapor P... |
Psub | 1.18e-04 | kPa | 258.15 | Vapor P... |
Psub | 2.41e-04 | kPa | 263.15 | Vapor P... |
Psub | 4.90e-04 | kPa | 268.15 | Vapor P... |
Psub | 9.84e-04 | kPa | 273.15 | Vapor P... |
Psub | 1.86e-03 | kPa | 278.15 | Vapor P... |
Psub | 3.34e-03 | kPa | 283.15 | Vapor P... |
Psub | 4.81e-03 | kPa | 286.15 | Vapor P... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [375.03; 514.61] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.80721e+01 | |||
Coefficient B | -6.30480e+03 | |||
Coefficient C | -2.05220e+01 | |||
Temperature range, min. | 375.03 | |||
Temperature range, max. | 514.61 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 375.03 | Calculated Property |
Pvap | 2.81 | kPa | 390.54 | Calculated Property |
Pvap | 5.58 | kPa | 406.05 | Calculated Property |
Pvap | 10.49 | kPa | 421.56 | Calculated Property |
Pvap | 18.84 | kPa | 437.07 | Calculated Property |
Pvap | 32.44 | kPa | 452.57 | Calculated Property |
Pvap | 53.79 | kPa | 468.08 | Calculated Property |
Pvap | 86.22 | kPa | 483.59 | Calculated Property |
Pvap | 134.03 | kPa | 499.10 | Calculated Property |
Pvap | 202.67 | kPa | 514.61 | Calculated Property |
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