Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 215.46 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -359.51 | kJ/mol | Joback Calculated Property |
ΔfusH° | 50.01 | kJ/mol | Joback Calculated Property |
ΔvapH° | 74.60 | kJ/mol | Joback Calculated Property |
log10WS | -8.80 | Crippen Calculated Property | |
logPoct/wat | 7.402 | Crippen Calculated Property | |
McVol | 325.260 | ml/mol | McGowan Calculated Property |
Pc | 937.49 | kPa | Joback Calculated Property |
Tboil | 800.10 | K | Joback Calculated Property |
Tc | 988.35 | K | Joback Calculated Property |
Tfus | 449.26 | K | Joback Calculated Property |
Vc | 1.272 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [1008.76; 1118.15] | J/mol×K | [800.10; 988.35] | |
T(K) Ideal gas heat capacity (J/mol×K) 1000 1020 1040 1060 1080 1100 1120 800 850 900 950 | ||||
Cp,gas | 1008.76 | J/mol×K | 800.10 | Joback Calculated Property |
Cp,gas | 1029.54 | J/mol×K | 831.48 | Joback Calculated Property |
Cp,gas | 1049.26 | J/mol×K | 862.85 | Joback Calculated Property |
Cp,gas | 1067.95 | J/mol×K | 894.23 | Joback Calculated Property |
Cp,gas | 1085.64 | J/mol×K | 925.60 | Joback Calculated Property |
Cp,gas | 1102.36 | J/mol×K | 956.98 | Joback Calculated Property |
Cp,gas | 1118.15 | J/mol×K | 988.35 | Joback Calculated Property |
η | [0.0000615; 0.0006076] | Pa×s | [449.26; 800.10] | |
T(K) Dynamic viscosity (Pa×s) 1.00e-4 2.00e-4 3.00e-4 4.00e-4 5.00e-4 6.00e-4 500 600 700 800 | ||||
η | 0.0006076 | Pa×s | 449.26 | Joback Calculated Property |
η | 0.0003329 | Pa×s | 507.73 | Joback Calculated Property |
η | 0.0002065 | Pa×s | 566.21 | Joback Calculated Property |
η | 0.0001401 | Pa×s | 624.68 | Joback Calculated Property |
η | 0.0001015 | Pa×s | 683.15 | Joback Calculated Property |
η | 0.0000774 | Pa×s | 741.63 | Joback Calculated Property |
η | 0.0000615 | Pa×s | 800.10 | Joback Calculated Property |
ΔvapH | 68.40 | kJ/mol | 532.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [509.51; 717.49] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.44403e+01 | |||
Coefficient B | -5.34874e+03 | |||
Coefficient C | -1.31580e+02 | |||
Temperature range, min. | 509.51 | |||
Temperature range, max. | 717.49 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 550 600 650 700 | ||||
Pvap | 1.33 | kPa | 509.51 | Calculated Property |
Pvap | 3.01 | kPa | 532.62 | Calculated Property |
Pvap | 6.23 | kPa | 555.73 | Calculated Property |
Pvap | 11.96 | kPa | 578.84 | Calculated Property |
Pvap | 21.52 | kPa | 601.95 | Calculated Property |
Pvap | 36.65 | kPa | 625.05 | Calculated Property |
Pvap | 59.52 | kPa | 648.16 | Calculated Property |
Pvap | 92.72 | kPa | 671.27 | Calculated Property |
Pvap | 139.29 | kPa | 694.38 | Calculated Property |
Pvap | 202.63 | kPa | 717.49 | Calculated Property |
Find more compounds similar to Benzene, hexapropyl-.
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