Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -112.80 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -330.76 | kJ/mol | Joback Calculated Property |
ΔfusH° | 1.10 | kJ/mol | Thermod... |
ΔsubH° | 118.20 ± 1.00 | kJ/mol | NIST |
ΔvapH° | 68.67 | kJ/mol | Joback Calculated Property |
log10WS | -3.59 | Crippen Calculated Property | |
logPoct/wat | 3.117 | Crippen Calculated Property | |
McVol | 163.620 | ml/mol | McGowan Calculated Property |
Pc | 2773.00 | kPa | Joback Calculated Property |
Tboil | 651.67 | K | Joback Calculated Property |
Tc | 847.74 | K | Joback Calculated Property |
Tfus | 374.69 | K | Joback Calculated Property |
Vc | 0.625 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [424.06; 488.76] | J/mol×K | [651.67; 847.74] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 420 430 440 450 460 470 480 490 700 800 | ||||
Cp,gas | 424.06 | J/mol×K | 651.67 | Joback Calculated Property |
Cp,gas | 436.53 | J/mol×K | 684.35 | Joback Calculated Property |
Cp,gas | 448.28 | J/mol×K | 717.03 | Joback Calculated Property |
Cp,gas | 459.35 | J/mol×K | 749.71 | Joback Calculated Property |
Cp,gas | 469.77 | J/mol×K | 782.38 | Joback Calculated Property |
Cp,gas | 479.56 | J/mol×K | 815.06 | Joback Calculated Property |
Cp,gas | 488.76 | J/mol×K | 847.74 | Joback Calculated Property |
η | [0.0000644; 0.0030088] | Pa×s | [374.69; 651.67] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 400 500 600 | ||||
η | 0.0030088 | Pa×s | 374.69 | Joback Calculated Property |
η | 0.0011159 | Pa×s | 420.85 | Joback Calculated Property |
η | 0.0005035 | Pa×s | 467.02 | Joback Calculated Property |
η | 0.0002621 | Pa×s | 513.18 | Joback Calculated Property |
η | 0.0001520 | Pa×s | 559.34 | Joback Calculated Property |
η | 0.0000958 | Pa×s | 605.51 | Joback Calculated Property |
η | 0.0000644 | Pa×s | 651.67 | Joback Calculated Property |
ΔfusH | [1.50; 9.90] | kJ/mol | [252.00; 395.00] | ![]() |
ΔfusH | 2.60 | kJ/mol | 252.00 | NIST |
ΔfusH | 9.90 | kJ/mol | 362.00 | NIST |
ΔfusH | 1.50 | kJ/mol | 395.00 | NIST |
ΔfusS | [3.80; 27.35] | J/mol×K | [252.00; 395.00] | ![]() |
ΔfusS | 10.32 | J/mol×K | 252.00 | NIST |
ΔfusS | 27.35 | J/mol×K | 362.00 | NIST |
ΔfusS | 3.80 | J/mol×K | 395.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [414.08; 635.39] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.26782e+01 | |||
Coefficient B | -4.02101e+03 | |||
Coefficient C | -8.95600e+01 | |||
Temperature range, min. | 414.08 | |||
Temperature range, max. | 635.39 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 600 | ||||
Pvap | 1.33 | kPa | 414.08 | Calculated Property |
Pvap | 3.19 | kPa | 438.67 | Calculated Property |
Pvap | 6.81 | kPa | 463.26 | Calculated Property |
Pvap | 13.23 | kPa | 487.85 | Calculated Property |
Pvap | 23.80 | kPa | 512.44 | Calculated Property |
Pvap | 40.13 | kPa | 537.03 | Calculated Property |
Pvap | 64.09 | kPa | 561.62 | Calculated Property |
Pvap | 97.71 | kPa | 586.21 | Calculated Property |
Pvap | 143.16 | kPa | 610.80 | Calculated Property |
Pvap | 202.65 | kPa | 635.39 | Calculated Property |
Find more compounds similar to Benzoic acid, 4-pentyl-.
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