Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 381.87 | kJ/mol | Joback Calculated Property |
ΔfH°gas | 242.80 | kJ/mol | Joback Calculated Property |
ΔfusH° | 21.91 | kJ/mol | Joback Calculated Property |
ΔvapH° | 84.50 ± 1.40 | kJ/mol | NIST |
IE | [7.70; 7.70] | eV |
![]() |
IE | 7.70 ± 0.03 | eV | NIST |
IE | 7.70 ± 0.03 | eV | NIST |
log10WS | [-5.85; -5.85] |
![]() |
|
log10WS | -5.85 | Aq. Sol... | |
log10WS | -5.85 | Estimat... | |
logPoct/wat | 4.301 | Crippen Calculated Property | |
McVol | 159.530 | ml/mol | McGowan Calculated Property |
Pc | 2868.87 | kPa | Joback Calculated Property |
Inp | [319.96; 1944.00] |
![]() |
|
Inp | Outlier 1901.20 | NIST | |
Inp | Outlier 1944.00 | NIST | |
Inp | Outlier 1883.00 | NIST | |
Inp | Outlier 1890.00 | NIST | |
Inp | Outlier 1888.00 | NIST | |
Inp | Outlier 1929.00 | NIST | |
Inp | Outlier 1896.00 | NIST | |
Inp | 323.59 | NIST | |
Inp | 323.90 | NIST | |
Inp | 323.60 | NIST | |
Inp | 323.79 | NIST | |
Inp | 323.52 | NIST | |
Inp | 323.67 | NIST | |
Inp | 323.92 | NIST | |
Inp | 324.21 | NIST | |
Inp | 323.78 | NIST | |
Inp | 323.70 | NIST | |
Inp | 323.90 | NIST | |
Inp | 324.00 | NIST | |
Inp | 323.52 | NIST | |
Inp | 323.79 | NIST | |
Inp | 323.64 | NIST | |
Inp | 323.90 | NIST | |
Inp | 321.10 | NIST | |
Inp | 323.54 | NIST | |
Inp | 323.52 | NIST | |
Inp | 323.54 | NIST | |
Inp | 323.78 | NIST | |
Inp | 320.00 | NIST | |
Inp | 338.91 | NIST | |
Inp | 323.30 | NIST | |
Inp | 323.30 | NIST | |
Inp | 323.90 | NIST | |
Inp | 323.60 | NIST | |
Inp | 322.61 | NIST | |
Inp | 323.60 | NIST | |
Inp | 323.60 | NIST | |
Inp | 324.60 | NIST | |
Inp | 319.96 | NIST | |
Inp | 323.90 | NIST | |
Inp | 323.91 | NIST | |
Inp | 323.80 | NIST | |
Inp | 321.28 | NIST | |
Inp | 321.43 | NIST | |
Inp | 323.90 | NIST | |
Tboil | 617.20 | K | Joback Calculated Property |
Tc | 866.35 | K | Joback Calculated Property |
Tfus | 375.67 | K | Joback Calculated Property |
Vc | 0.612 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [381.22; 456.90] | J/mol×K | [617.20; 866.35] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 380 400 420 440 460 700 800 | ||||
Cp,gas | 381.22 | J/mol×K | 617.20 | Joback Calculated Property |
Cp,gas | 396.50 | J/mol×K | 658.73 | Joback Calculated Property |
Cp,gas | 410.54 | J/mol×K | 700.25 | Joback Calculated Property |
Cp,gas | 423.46 | J/mol×K | 741.78 | Joback Calculated Property |
Cp,gas | 435.41 | J/mol×K | 783.30 | Joback Calculated Property |
Cp,gas | 446.52 | J/mol×K | 824.83 | Joback Calculated Property |
Cp,gas | 456.90 | J/mol×K | 866.35 | Joback Calculated Property |
η | [0.0004506; 0.0013574] | Pa×s | [375.67; 617.20] | ![]() |
T(K) Dynamic viscosity (Pa×s) 4.00e-4 6.00e-4 8.00e-4 1.00e-3 1.20e-3 1.40e-3 400 500 600 | ||||
η | 0.0013574 | Pa×s | 375.67 | Joback Calculated Property |
η | 0.0010334 | Pa×s | 415.93 | Joback Calculated Property |
η | 0.0008255 | Pa×s | 456.18 | Joback Calculated Property |
η | 0.0006839 | Pa×s | 496.44 | Joback Calculated Property |
η | 0.0005828 | Pa×s | 536.69 | Joback Calculated Property |
η | 0.0005079 | Pa×s | 576.95 | Joback Calculated Property |
η | 0.0004506 | Pa×s | 617.20 | Joback Calculated Property |
ΔvapH | 76.30 | kJ/mol | 398.00 | NIST |
Pvap | [1.85e-05; 5.79] | kPa | [298.15; 510.00] | ![]() |
T(K) Vapor pressure (kPa) 0 1 2 3 4 5 6 300 400 500 | ||||
Pvap | 1.85e-05 | kPa | 298.15 | Hypothe... |
Pvap | 2.28e-05 | kPa | 300.00 | Hypothe... |
Pvap | 6.66e-05 | kPa | 310.00 | Hypothe... |
Pvap | 1.80e-04 | kPa | 320.00 | Hypothe... |
Pvap | 4.56e-04 | kPa | 330.00 | Hypothe... |
Pvap | 1.08e-03 | kPa | 340.00 | Hypothe... |
Pvap | 2.40e-03 | kPa | 350.00 | Hypothe... |
Pvap | 5.07e-03 | kPa | 360.00 | Hypothe... |
Pvap | 0.01 | kPa | 370.00 | Hypothe... |
Pvap | 0.02 | kPa | 380.00 | Hypothe... |
Pvap | 0.04 | kPa | 390.00 | Hypothe... |
Pvap | 0.06 | kPa | 400.00 | Hypothe... |
Pvap | 0.11 | kPa | 410.00 | Hypothe... |
Pvap | 0.18 | kPa | 420.00 | Hypothe... |
Pvap | 0.29 | kPa | 430.00 | Hypothe... |
Pvap | 0.46 | kPa | 440.00 | Hypothe... |
Pvap | 0.71 | kPa | 450.00 | Hypothe... |
Pvap | 1.05 | kPa | 460.00 | Hypothe... |
Pvap | 1.54 | kPa | 470.00 | Hypothe... |
Pvap | 2.20 | kPa | 480.00 | Hypothe... |
Pvap | 3.09 | kPa | 490.00 | Hypothe... |
Pvap | 4.26 | kPa | 500.00 | Hypothe... |
Pvap | 5.79 | kPa | 510.00 | Hypothe... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [463.72; 667.69] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.38885e+01 | |||
Coefficient B | -4.73615e+03 | |||
Coefficient C | -1.15498e+02 | |||
Temperature range, min. | 463.72 | |||
Temperature range, max. | 667.69 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 500 550 600 650 | ||||
Pvap | 1.33 | kPa | 463.72 | Calculated Property |
Pvap | 3.06 | kPa | 486.38 | Calculated Property |
Pvap | 6.39 | kPa | 509.05 | Calculated Property |
Pvap | 12.30 | kPa | 531.71 | Calculated Property |
Pvap | 22.13 | kPa | 554.37 | Calculated Property |
Pvap | 37.60 | kPa | 577.04 | Calculated Property |
Pvap | 60.78 | kPa | 599.70 | Calculated Property |
Pvap | 94.12 | kPa | 622.36 | Calculated Property |
Pvap | 140.39 | kPa | 645.03 | Calculated Property |
Pvap | 202.66 | kPa | 667.69 | Calculated Property |
Find more compounds similar to Phenanthrene, 1-methyl-.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.