Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 17.58 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -244.93 | kJ/mol | Joback Calculated Property |
ΔfusH° | 8.50 | kJ/mol | Joback Calculated Property |
ΔvapH° | 42.70 | kJ/mol | NIST |
log10WS | -2.86 | Crippen Calculated Property | |
logPoct/wat | 3.325 | Crippen Calculated Property | |
McVol | 137.670 | ml/mol | McGowan Calculated Property |
Pc | 2361.07 | kPa | Joback Calculated Property |
Inp | [815.00; 853.00] |
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|
Inp | 850.00 | NIST | |
Inp | 843.00 | NIST | |
Inp | 845.80 | NIST | |
Inp | 850.05 | NIST | |
Inp | 849.30 | NIST | |
Inp | 851.40 | NIST | |
Inp | 848.30 | NIST | |
Inp | 848.40 | NIST | |
Inp | 849.90 | NIST | |
Inp | 850.10 | NIST | |
Inp | 852.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 849.70 | NIST | |
Inp | 849.00 | NIST | |
Inp | 852.00 | NIST | |
Inp | 840.00 | NIST | |
Inp | 841.00 | NIST | |
Inp | 842.00 | NIST | |
Inp | 843.00 | NIST | |
Inp | 844.00 | NIST | |
Inp | 848.00 | NIST | |
Inp | 851.00 | NIST | |
Inp | 843.00 | NIST | |
Inp | 847.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 847.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 853.00 | NIST | |
Inp | 847.00 | NIST | |
Inp | 850.20 | NIST | |
Inp | 850.00 | NIST | |
Inp | 847.00 | NIST | |
Inp | 853.00 | NIST | |
Inp | Outlier 815.00 | NIST | |
Inp | 849.00 | NIST | |
Inp | 851.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 850.20 | NIST | |
Inp | 850.00 | NIST | |
Inp | 851.40 | NIST | |
Inp | 852.00 | NIST | |
Inp | 840.00 | NIST | |
Inp | 848.00 | NIST | |
Inp | 847.00 | NIST | |
Tboil | [410.35; 412.25] | K |
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Tboil | 412.00 ± 1.50 | K | NIST |
Tboil | 412.21 ± 0.30 | K | NIST |
Tboil | 412.21 ± 0.60 | K | NIST |
Tboil | 410.85 ± 0.70 | K | NIST |
Tboil | 410.35 ± 0.40 | K | NIST |
Tboil | 412.25 ± 0.30 | K | NIST |
Tc | 578.35 | K | Joback Calculated Property |
Tfus | 146.19 | K | Joback Calculated Property |
Vc | 0.521 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [272.44; 355.89] | J/mol×K | [404.00; 578.35] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 280 300 320 340 360 400 450 500 550 | ||||
Cp,gas | 272.44 | J/mol×K | 404.00 | Joback Calculated Property |
Cp,gas | 287.79 | J/mol×K | 433.06 | Joback Calculated Property |
Cp,gas | 302.55 | J/mol×K | 462.12 | Joback Calculated Property |
Cp,gas | 316.72 | J/mol×K | 491.17 | Joback Calculated Property |
Cp,gas | 330.33 | J/mol×K | 520.23 | Joback Calculated Property |
Cp,gas | 343.38 | J/mol×K | 549.29 | Joback Calculated Property |
Cp,gas | 355.89 | J/mol×K | 578.35 | Joback Calculated Property |
η | [0.0002173; 0.0558851] | Pa×s | [146.19; 404.00] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 0.01 0.02 0.03 0.04 0.05 0.06 200 300 400 | ||||
η | 0.0558851 | Pa×s | 146.19 | Joback Calculated Property |
η | 0.0077512 | Pa×s | 189.16 | Joback Calculated Property |
η | 0.0022339 | Pa×s | 232.13 | Joback Calculated Property |
η | 0.0009496 | Pa×s | 275.10 | Joback Calculated Property |
η | 0.0005086 | Pa×s | 318.06 | Joback Calculated Property |
η | 0.0003161 | Pa×s | 361.03 | Joback Calculated Property |
η | 0.0002173 | Pa×s | 404.00 | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [299.95; 440.34] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41855e+01 | |||
Coefficient B | -3.44620e+03 | |||
Coefficient C | -5.19900e+01 | |||
Temperature range, min. | 299.95 | |||
Temperature range, max. | 440.34 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 299.95 | Calculated Property |
Pvap | 3.03 | kPa | 315.55 | Calculated Property |
Pvap | 6.30 | kPa | 331.15 | Calculated Property |
Pvap | 12.11 | kPa | 346.75 | Calculated Property |
Pvap | 21.79 | kPa | 362.35 | Calculated Property |
Pvap | 37.07 | kPa | 377.94 | Calculated Property |
Pvap | 60.08 | kPa | 393.54 | Calculated Property |
Pvap | 93.36 | kPa | 409.14 | Calculated Property |
Pvap | 139.80 | kPa | 424.74 | Calculated Property |
Pvap | 202.67 | kPa | 440.34 | Calculated Property |
Pvap | [1.35; 2536.14] | kPa | [300.15; 594.50] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.02224e+01 | |||
Coefficient B | -8.04411e+03 | |||
Coefficient C | -1.11797e+01 | |||
Coefficient D | 7.24323e-06 | |||
Temperature range, min. | 300.15 | |||
Temperature range, max. | 594.50 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 300 400 500 600 | ||||
Pvap | 1.35 | kPa | 300.15 | Calculated Property |
Pvap | 6.88 | kPa | 332.86 | Calculated Property |
Pvap | 24.75 | kPa | 365.56 | Calculated Property |
Pvap | 69.34 | kPa | 398.27 | Calculated Property |
Pvap | 161.72 | kPa | 430.97 | Calculated Property |
Pvap | 329.18 | kPa | 463.68 | Calculated Property |
Pvap | 604.91 | kPa | 496.38 | Calculated Property |
Pvap | 1029.05 | kPa | 529.09 | Calculated Property |
Pvap | 1651.38 | kPa | 561.79 | Calculated Property |
Pvap | 2536.14 | kPa | 594.50 | Calculated Property |
Find more compounds similar to Hexane, 2,3,4-trimethyl-.
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