Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4370 | KDB | |
ΔfG° | 154.15 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -33.84 | kJ/mol | Joback Calculated Property |
ΔfusH° | 18.29 | kJ/mol | Joback Calculated Property |
ΔvapH° | [55.10; 55.30] | kJ/mol |
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ΔvapH° | 55.10 ± 0.40 | kJ/mol | NIST |
ΔvapH° | 55.30 | kJ/mol | NIST |
ΔvapH° | 55.10 | kJ/mol | NIST |
log10WS | [-4.64; -4.64] |
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|
log10WS | -4.64 | Aq. Sol... | |
log10WS | -4.64 | Estimat... | |
logPoct/wat | 3.419 | Crippen Calculated Property | |
McVol | 142.090 | ml/mol | McGowan Calculated Property |
Pc | 2600.00 | kPa | KDB |
Inp | [1110.00; 1178.00] |
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|
Inp | 1144.00 | NIST | |
Inp | 1144.90 | NIST | |
Inp | 1146.00 | NIST | |
Inp | 1136.00 | NIST | |
Inp | 1142.00 | NIST | |
Inp | 1147.00 | NIST | |
Inp | 1140.00 | NIST | |
Inp | 1142.00 | NIST | |
Inp | 1145.00 | NIST | |
Inp | 1140.50 | NIST | |
Inp | 1145.00 | NIST | |
Inp | 1151.00 | NIST | |
Inp | 1157.00 | NIST | |
Inp | 1131.30 | NIST | |
Inp | 1136.20 | NIST | |
Inp | 1145.30 | NIST | |
Inp | 1150.90 | NIST | |
Inp | 1157.40 | NIST | |
Inp | 1131.30 | NIST | |
Inp | 1136.20 | NIST | |
Inp | 1133.00 | NIST | |
Inp | 1128.58 | NIST | |
Inp | Outlier 1178.00 | NIST | |
Inp | 1136.00 | NIST | |
Inp | 1135.20 | NIST | |
Inp | 1159.00 | NIST | |
Inp | 1142.00 | NIST | |
Inp | 1143.00 | NIST | |
Inp | 1141.00 | NIST | |
Inp | 1165.00 | NIST | |
Inp | 1148.70 | NIST | |
Inp | 1136.00 | NIST | |
Inp | 1142.00 | NIST | |
Inp | 1163.00 | NIST | |
Inp | 1157.00 | NIST | |
Inp | 1154.00 | NIST | |
Inp | 1146.00 | NIST | |
Inp | 1140.90 | NIST | |
Inp | 1143.10 | NIST | |
Inp | 1167.00 | NIST | |
Inp | 1144.00 | NIST | |
Inp | 1168.20 | NIST | |
Inp | 1157.30 | NIST | |
Inp | 1163.50 | NIST | |
Inp | Outlier 1177.00 | NIST | |
Inp | 1169.90 | NIST | |
Inp | Outlier 1173.50 | NIST | |
Inp | 1150.00 | NIST | |
Inp | 1134.00 | NIST | |
Inp | 1134.00 | NIST | |
Inp | 1138.36 | NIST | |
Inp | 1142.28 | NIST | |
Inp | 1144.71 | NIST | |
Inp | 1155.95 | NIST | |
Inp | 1160.10 | NIST | |
Inp | 1162.94 | NIST | |
Inp | 1141.00 | NIST | |
Inp | 1160.10 | NIST | |
Inp | 1163.00 | NIST | |
Inp | 1145.00 | NIST | |
Inp | 1145.00 | NIST | |
Inp | 1145.00 | NIST | |
Inp | 1151.00 | NIST | |
Inp | 1151.00 | NIST | |
Inp | Outlier 1123.00 | NIST | |
Inp | 1139.00 | NIST | |
Inp | 1142.00 | NIST | |
Inp | 1144.00 | NIST | |
Inp | 1150.00 | NIST | |
Inp | 1145.00 | NIST | |
Inp | 1158.00 | NIST | |
Inp | 1161.00 | NIST | |
Inp | 1167.00 | NIST | |
Inp | 1158.00 | NIST | |
Inp | 1148.00 | NIST | |
Inp | 1144.00 | NIST | |
Inp | 1158.00 | NIST | |
Inp | 1135.00 | NIST | |
Inp | 1164.90 | NIST | |
Inp | 1168.00 | NIST | |
Inp | Outlier 1110.00 | NIST | |
Inp | 1154.00 | NIST | |
Inp | 1162.00 | NIST | |
Inp | 1166.00 | NIST | |
Inp | 1157.00 | NIST | |
Inp | 1143.00 | NIST | |
Inp | 1143.00 | NIST | |
Inp | 1143.00 | NIST | |
Inp | 1135.50 | NIST | |
Inp | 1141.00 | NIST | |
Inp | 1145.00 | NIST | |
Inp | 1146.00 | NIST | |
Inp | 1150.00 | NIST | |
Inp | 1158.00 | NIST | |
Inp | 1164.90 | NIST | |
Inp | 1163.00 | NIST | |
Inp | 1143.10 | NIST | |
Inp | 1163.50 | NIST | |
Inp | 1134.00 | NIST | |
Inp | 1155.95 | NIST | |
Inp | 1160.10 | NIST | |
Inp | 1148.70 | NIST | |
I | [1376.00; 1470.20] |
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|
I | 1404.30 | NIST | |
I | 1459.30 | NIST | |
I | 1464.80 | NIST | |
I | Outlier 1470.20 | NIST | |
I | 1394.10 | NIST | |
I | 1376.30 | NIST | |
I | 1433.30 | NIST | |
I | 1409.00 | NIST | |
I | 1416.00 | NIST | |
I | 1408.00 | NIST | |
I | 1433.00 | NIST | |
I | 1414.00 | NIST | |
I | 1414.00 | NIST | |
I | 1426.00 | NIST | |
I | 1439.00 | NIST | |
I | 1453.00 | NIST | |
I | 1402.00 | NIST | |
I | 1376.00 | NIST | |
I | 1421.00 | NIST | |
I | 1422.00 | NIST | |
I | 1403.00 | NIST | |
I | 1419.00 | NIST | |
I | 1426.00 | NIST | |
I | 1426.00 | NIST | |
I | 1426.00 | NIST | |
I | 1376.00 | NIST | |
I | 1381.00 | NIST | |
I | 1426.00 | NIST | |
Tboil | [452.00; 478.60] | K |
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Tboil | 478.60 | K | KDB |
Tboil | 478.60 | K | NIST |
Tboil | 478.35 ± 0.40 | K | NIST |
Tboil | 470.00 ± 5.00 | K | NIST |
Tboil | 478.60 ± 0.40 | K | NIST |
Tboil | 477.40 ± 1.00 | K | NIST |
Tboil | 478.00 ± 2.00 | K | NIST |
Tboil | 478.00 ± 2.00 | K | NIST |
Tboil | 478.00 ± 3.00 | K | NIST |
Tboil | 478.00 ± 3.00 | K | NIST |
Tboil | 471.70 ± 4.00 | K | NIST |
Tboil | 478.50 ± 2.00 | K | NIST |
Tboil | 473.00 ± 4.00 | K | NIST |
Tboil | 473.15 ± 2.00 | K | NIST |
Tboil | 473.15 ± 2.00 | K | NIST |
Tboil | 475.00 ± 5.00 | K | NIST |
Tboil | 475.10 ± 3.00 | K | NIST |
Tboil | 461.00 ± 10.00 | K | NIST |
Tboil | Outlier 453.00 ± 15.00 | K | NIST |
Tboil | Outlier 452.00 ± 12.00 | K | NIST |
Tboil | 461.00 ± 10.00 | K | NIST |
Tboil | 461.00 ± 10.00 | K | NIST |
Tboil | 468.00 ± 10.00 | K | NIST |
Tc | 679.90 | K | KDB |
Tfus | [194.90; 198.00] | K |
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Tfus | 198.00 | K | KDB |
Tfus | 194.90 ± 0.30 | K | NIST |
Vc | 0.550 | m3/kmol | KDB |
Zc | 0.2529610 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [299.93; 383.96] | J/mol×K | [477.76; 679.70] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 300 320 340 360 380 500 550 600 650 | ||||
Cp,gas | 299.93 | J/mol×K | 477.76 | Joback Calculated Property |
Cp,gas | 315.99 | J/mol×K | 511.42 | Joback Calculated Property |
Cp,gas | 331.19 | J/mol×K | 545.07 | Joback Calculated Property |
Cp,gas | 345.55 | J/mol×K | 578.73 | Joback Calculated Property |
Cp,gas | 359.11 | J/mol×K | 612.39 | Joback Calculated Property |
Cp,gas | 371.90 | J/mol×K | 646.04 | Joback Calculated Property |
Cp,gas | 383.96 | J/mol×K | 679.70 | Joback Calculated Property |
η | [0.0002186; 0.0038056] | Pa×s | [240.15; 477.76] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 300 400 | ||||
η | 0.0038056 | Pa×s | 240.15 | Joback Calculated Property |
η | 0.0016875 | Pa×s | 279.75 | Joback Calculated Property |
η | 0.0009155 | Pa×s | 319.35 | Joback Calculated Property |
η | 0.0005684 | Pa×s | 358.96 | Joback Calculated Property |
η | 0.0003880 | Pa×s | 398.56 | Joback Calculated Property |
η | 0.0002837 | Pa×s | 438.16 | Joback Calculated Property |
η | 0.0002186 | Pa×s | 477.76 | Joback Calculated Property |
ΔvapH | 41.21 | kJ/mol | 478.60 | KDB |
Pvap | [0.02; 0.27] | kPa | [284.50; 323.20] | ![]() |
T(K) Vapor pressure (kPa) 0 0.05 0.1 0.15 0.2 0.25 290 300 310 320 | ||||
Pvap | 0.02 | kPa | 284.50 | Vapour ... |
Pvap | 0.02 | kPa | 287.50 | Vapour ... |
Pvap | 0.03 | kPa | 290.40 | Vapour ... |
Pvap | 0.03 | kPa | 293.30 | Vapour ... |
Pvap | 0.03 | kPa | 293.40 | Vapour ... |
Pvap | 0.04 | kPa | 296.30 | Vapour ... |
Pvap | 0.05 | kPa | 298.30 | Vapour ... |
Pvap | 0.07 | kPa | 303.20 | Vapour ... |
Pvap | 0.09 | kPa | 306.30 | Vapour ... |
Pvap | 0.10 | kPa | 308.20 | Vapour ... |
Pvap | 0.12 | kPa | 311.20 | Vapour ... |
Pvap | 0.15 | kPa | 314.20 | Vapour ... |
Pvap | 0.18 | kPa | 317.30 | Vapour ... |
Pvap | 0.22 | kPa | 320.30 | Vapour ... |
Pvap | 0.27 | kPa | 323.20 | Vapour ... |
n0 | 1.48870 | 293.10 | Extract... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [349.54; 510.12] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.48785e+01 | |||
Coefficient B | -4.46183e+03 | |||
Coefficient C | -4.37410e+01 | |||
Temperature range, min. | 349.54 | |||
Temperature range, max. | 510.12 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 500 | ||||
Pvap | 1.33 | kPa | 349.54 | Calculated Property |
Pvap | 2.98 | kPa | 367.38 | Calculated Property |
Pvap | 6.13 | kPa | 385.22 | Calculated Property |
Pvap | 11.72 | kPa | 403.07 | Calculated Property |
Pvap | 21.09 | kPa | 420.91 | Calculated Property |
Pvap | 35.98 | kPa | 438.75 | Calculated Property |
Pvap | 58.63 | kPa | 456.59 | Calculated Property |
Pvap | 91.73 | kPa | 474.44 | Calculated Property |
Pvap | 138.51 | kPa | 492.28 | Calculated Property |
Pvap | 202.66 | kPa | 510.12 | Calculated Property |
Pvap | [8.25e-07; 2617.20] | kPa | [198.15; 679.90] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.28216e+01 | |||
Coefficient B | -8.15428e+03 | |||
Coefficient C | -6.76421e+00 | |||
Coefficient D | 2.50375e-06 | |||
Temperature range, min. | 198.15 | |||
Temperature range, max. | 679.90 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 200 400 600 | ||||
Pvap | 8.25e-07 | kPa | 198.15 | Calculated Property |
Pvap | 1.10e-03 | kPa | 251.68 | Calculated Property |
Pvap | 0.09 | kPa | 305.21 | Calculated Property |
Pvap | 1.86 | kPa | 358.73 | Calculated Property |
Pvap | 15.43 | kPa | 412.26 | Calculated Property |
Pvap | 73.77 | kPa | 465.79 | Calculated Property |
Pvap | 245.08 | kPa | 519.32 | Calculated Property |
Pvap | 633.73 | kPa | 572.84 | Calculated Property |
Pvap | 1372.72 | kPa | 626.37 | Calculated Property |
Pvap | 2617.20 | kPa | 679.90 | Calculated Property |
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