Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 33.72 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -263.76 | kJ/mol | Joback Calculated Property |
ΔfusH° | 10.72 | kJ/mol | Joback Calculated Property |
ΔvapH° | 45.20 | kJ/mol | NIST |
log10WS | -3.52 | Crippen Calculated Property | |
logPoct/wat | 3.859 | Crippen Calculated Property | |
McVol | 151.760 | ml/mol | McGowan Calculated Property |
Pc | 2161.32 | kPa | Joback Calculated Property |
Inp | [881.00; 881.30] | ||
Inp | 881.00 | NIST | |
Inp | Outlier 881.30 | NIST | |
Inp | 881.00 | NIST | |
Inp | 881.00 | NIST | |
Inp | 881.00 | NIST | |
Inp | 881.00 | NIST | |
Tboil | 420.20 ± 1.50 | K | NIST |
Tc | 600.93 | K | Joback Calculated Property |
Tfus | 189.88 | K | Joback Calculated Property |
Vc | 0.579 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [316.93; 407.85] | J/mol×K | [424.53; 600.93] | |
T(K) Ideal gas heat capacity (J/mol×K) 320 340 360 380 400 450 500 550 600 | ||||
Cp,gas | 316.93 | J/mol×K | 424.53 | Joback Calculated Property |
Cp,gas | 333.94 | J/mol×K | 453.93 | Joback Calculated Property |
Cp,gas | 350.18 | J/mol×K | 483.33 | Joback Calculated Property |
Cp,gas | 365.66 | J/mol×K | 512.73 | Joback Calculated Property |
Cp,gas | 380.41 | J/mol×K | 542.13 | Joback Calculated Property |
Cp,gas | 394.47 | J/mol×K | 571.53 | Joback Calculated Property |
Cp,gas | 407.85 | J/mol×K | 600.93 | Joback Calculated Property |
η | [0.0002394; 0.0206027] | Pa×s | [189.88; 424.53] | |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-3 0.01 0.02 0.02 200 300 400 | ||||
η | 0.0206027 | Pa×s | 189.88 | Joback Calculated Property |
η | 0.0052013 | Pa×s | 228.99 | Joback Calculated Property |
η | 0.0019620 | Pa×s | 268.10 | Joback Calculated Property |
η | 0.0009486 | Pa×s | 307.20 | Joback Calculated Property |
η | 0.0005405 | Pa×s | 346.31 | Joback Calculated Property |
η | 0.0003452 | Pa×s | 385.42 | Joback Calculated Property |
η | 0.0002394 | Pa×s | 424.53 | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [307.32; 448.60] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40494e+01 | |||
Coefficient B | -3.38181e+03 | |||
Coefficient C | -6.15790e+01 | |||
Temperature range, min. | 307.32 | |||
Temperature range, max. | 448.60 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 307.32 | Calculated Property |
Pvap | 3.05 | kPa | 323.02 | Calculated Property |
Pvap | 6.34 | kPa | 338.72 | Calculated Property |
Pvap | 12.19 | kPa | 354.41 | Calculated Property |
Pvap | 21.94 | kPa | 370.11 | Calculated Property |
Pvap | 37.30 | kPa | 385.81 | Calculated Property |
Pvap | 60.39 | kPa | 401.51 | Calculated Property |
Pvap | 93.69 | kPa | 417.20 | Calculated Property |
Pvap | 140.04 | kPa | 432.90 | Calculated Property |
Pvap | 202.63 | kPa | 448.60 | Calculated Property |
Find more compounds similar to Hexane, 4-ethyl-2,2-dimethyl-.
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