Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 131.92 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -502.69 | kJ/mol | Joback Calculated Property |
ΔfusH° | 49.21 | kJ/mol | Joback Calculated Property |
ΔvapH° | 64.18 | kJ/mol | Joback Calculated Property |
log10WS | -8.79 | Crippen Calculated Property | |
logPoct/wat | 8.684 | Crippen Calculated Property | |
McVol | 320.840 | ml/mol | McGowan Calculated Property |
Pc | 906.15 | kPa | Joback Calculated Property |
Tboil | 702.32 | K | Joback Calculated Property |
Tc | 867.26 | K | Joback Calculated Property |
Tfus | 322.70 | K | Joback Calculated Property |
Vc | 1.262 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [962.39; 1080.72] | J/mol×K | [702.32; 867.26] | |
T(K) Ideal gas heat capacity (J/mol×K) 960 980 1000 1020 1040 1060 1080 700 750 800 850 | ||||
Cp,gas | 962.39 | J/mol×K | 702.32 | Joback Calculated Property |
Cp,gas | 984.38 | J/mol×K | 729.81 | Joback Calculated Property |
Cp,gas | 1005.42 | J/mol×K | 757.30 | Joback Calculated Property |
Cp,gas | 1025.55 | J/mol×K | 784.79 | Joback Calculated Property |
Cp,gas | 1044.78 | J/mol×K | 812.28 | Joback Calculated Property |
Cp,gas | 1063.16 | J/mol×K | 839.77 | Joback Calculated Property |
Cp,gas | 1080.72 | J/mol×K | 867.26 | Joback Calculated Property |
η | [0.0000698; 0.0040182] | Pa×s | [322.70; 702.32] | |
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-3 400 500 600 700 | ||||
η | 0.0040182 | Pa×s | 322.70 | Joback Calculated Property |
η | 0.0011754 | Pa×s | 385.97 | Joback Calculated Property |
η | 0.0004861 | Pa×s | 449.24 | Joback Calculated Property |
η | 0.0002500 | Pa×s | 512.51 | Joback Calculated Property |
η | 0.0001488 | Pa×s | 575.78 | Joback Calculated Property |
η | 0.0000982 | Pa×s | 639.05 | Joback Calculated Property |
η | 0.0000698 | Pa×s | 702.32 | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [463.37; 662.06] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42685e+01 | |||
Coefficient B | -4.95271e+03 | |||
Coefficient C | -1.09120e+02 | |||
Temperature range, min. | 463.37 | |||
Temperature range, max. | 662.06 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 500 550 600 650 | ||||
Pvap | 1.33 | kPa | 463.37 | Calculated Property |
Pvap | 3.03 | kPa | 485.45 | Calculated Property |
Pvap | 6.28 | kPa | 507.52 | Calculated Property |
Pvap | 12.06 | kPa | 529.60 | Calculated Property |
Pvap | 21.70 | kPa | 551.68 | Calculated Property |
Pvap | 36.93 | kPa | 573.75 | Calculated Property |
Pvap | 59.90 | kPa | 595.83 | Calculated Property |
Pvap | 93.15 | kPa | 617.91 | Calculated Property |
Pvap | 139.63 | kPa | 639.98 | Calculated Property |
Pvap | 202.65 | kPa | 662.06 | Calculated Property |
Find more compounds similar to Pentadecane, 8-heptyl-.
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