Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -4348.47 ± 0.92 | kJ/mol | NIST |
μ | 2.00 | debye | KDB |
ΔfG° | -35.36 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-163.00; -162.80] | kJ/mol |
![]() |
ΔfH°gas | -162.80 | kJ/mol | KDB |
ΔfH°gas | -163.00 ± 0.75 | kJ/mol | NIST |
ΔfH°liquid | -228.80 ± 1.40 | kJ/mol | NIST |
ΔfusH° | 15.91 | kJ/mol | Joback Calculated Property |
ΔvapH° | [48.53; 65.90] | kJ/mol |
![]() |
ΔvapH° | 64.96 | kJ/mol | NIST |
ΔvapH° | 64.60 | kJ/mol | NIST |
ΔvapH° | 65.90 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 65.80 | kJ/mol | NIST |
ΔvapH° | 48.53 | kJ/mol | NIST |
IE | [8.00; 8.18] | eV |
![]() |
IE | 8.00 | eV | NIST |
IE | 8.18 | eV | NIST |
log10WS | [-1.19; -1.19] |
![]() |
|
log10WS | -1.19 | Aq. Sol... | |
log10WS | -1.19 | Estimat... | |
logPoct/wat | 2.009 | Crippen Calculated Property | |
McVol | 105.690 | ml/mol | McGowan Calculated Property |
Pc | 10132.50 ± 0.50 | kPa | NIST |
Inp | [190.90; 1181.00] |
![]() |
|
Inp | 1124.00 | NIST | |
Inp | 1126.00 | NIST | |
Inp | 1126.00 | NIST | |
Inp | 1127.00 | NIST | |
Inp | 1094.00 | NIST | |
Inp | 1094.00 | NIST | |
Inp | 1130.00 | NIST | |
Inp | 1132.00 | NIST | |
Inp | 1128.00 | NIST | |
Inp | 1162.00 | NIST | |
Inp | 1177.00 | NIST | |
Inp | 1134.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1133.00 | NIST | |
Inp | 1135.00 | NIST | |
Inp | 1150.00 | NIST | |
Inp | 1148.90 | NIST | |
Inp | 1150.10 | NIST | |
Inp | 1151.40 | NIST | |
Inp | 1160.00 | NIST | |
Inp | 1150.00 | NIST | |
Inp | 1126.00 | NIST | |
Inp | 1126.00 | NIST | |
Inp | 1172.00 | NIST | |
Inp | 1181.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1149.00 | NIST | |
Inp | 1127.00 | NIST | |
Inp | 1120.00 | NIST | |
Inp | 1151.00 | NIST | |
Inp | 1144.00 | NIST | |
Inp | 1145.00 | NIST | |
Inp | 1150.00 | NIST | |
Inp | 1154.00 | NIST | |
Inp | 1156.00 | NIST | |
Inp | 1120.00 | NIST | |
Inp | 1134.00 | NIST | |
Inp | 1149.00 | NIST | |
Inp | 1150.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1134.00 | NIST | |
Inp | Outlier 192.24 | NIST | |
Inp | Outlier 190.90 | NIST | |
Inp | Outlier 191.20 | NIST | |
Inp | Outlier 192.69 | NIST | |
I | [2070.00; 2127.00] |
![]() |
|
I | 2087.00 | NIST | |
I | 2078.00 | NIST | |
I | 2073.00 | NIST | |
I | 2090.00 | NIST | |
I | 2098.99 | NIST | |
I | 2094.74 | NIST | |
I | 2098.02 | NIST | |
I | 2098.97 | NIST | |
I | 2079.00 | NIST | |
I | 2070.00 | NIST | |
I | 2078.00 | NIST | |
I | Outlier 2127.00 | NIST | |
Tboil | 484.13 | K | KDB |
Tc | [707.55; 818.15] | K |
![]() |
Tc | 707.60 | K | KDB |
Tc | 707.55 ± 0.30 | K | NIST |
Tc | 818.15 ± 2.00 | K | NIST |
Tfus | [297.65; 297.68] | K |
![]() |
Tfus | 297.68 | K | KDB |
Tfus | 297.65 | K | Aq. Sol... |
Vc | 0.342 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [224.69; 282.81] | J/mol×K | [494.72; 722.03] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 220 230 240 250 260 270 280 500 600 700 | ||||
Cp,gas | 224.69 | J/mol×K | 494.72 | Joback Calculated Property |
Cp,gas | 236.18 | J/mol×K | 532.60 | Joback Calculated Property |
Cp,gas | 246.85 | J/mol×K | 570.49 | Joback Calculated Property |
Cp,gas | 256.78 | J/mol×K | 608.37 | Joback Calculated Property |
Cp,gas | 266.04 | J/mol×K | 646.26 | Joback Calculated Property |
Cp,gas | 274.69 | J/mol×K | 684.14 | Joback Calculated Property |
Cp,gas | 282.81 | J/mol×K | 722.03 | Joback Calculated Property |
η | [0.0000891; 0.0031710] | Pa×s | [330.58; 494.72] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 350 400 450 | ||||
η | 0.0031710 | Pa×s | 330.58 | Joback Calculated Property |
η | 0.0013928 | Pa×s | 357.94 | Joback Calculated Property |
η | 0.0006876 | Pa×s | 385.29 | Joback Calculated Property |
η | 0.0003727 | Pa×s | 412.65 | Joback Calculated Property |
η | 0.0002180 | Pa×s | 440.01 | Joback Calculated Property |
η | 0.0001358 | Pa×s | 467.36 | Joback Calculated Property |
η | 0.0000891 | Pa×s | 494.72 | Joback Calculated Property |
ΔfusH | 12.76 | kJ/mol | 297.30 | NIST |
ΔsubH | 61.50 ± 0.80 | kJ/mol | 310.00 | NIST |
ΔvapH | [51.80; 65.90] | kJ/mol | [300.00; 457.50] | ![]() |
ΔvapH | 65.90 | kJ/mol | 300.00 | NIST |
ΔvapH | 65.90 ± 0.20 | kJ/mol | 300.00 | NIST |
ΔvapH | 65.90 ± 0.20 | kJ/mol | 300.00 | NIST |
ΔvapH | 51.80 | kJ/mol | 457.50 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 485.20 | K | 102.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [367.30; 511.94] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.54387e+01 | |||
Coefficient B | -4.41754e+03 | |||
Coefficient C | -7.57380e+01 | |||
Temperature range, min. | 367.30 | |||
Temperature range, max. | 511.94 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 367.30 | Calculated Property |
Pvap | 2.94 | kPa | 383.37 | Calculated Property |
Pvap | 6.00 | kPa | 399.44 | Calculated Property |
Pvap | 11.44 | kPa | 415.51 | Calculated Property |
Pvap | 20.58 | kPa | 431.58 | Calculated Property |
Pvap | 35.20 | kPa | 447.66 | Calculated Property |
Pvap | 57.57 | kPa | 463.73 | Calculated Property |
Pvap | 90.54 | kPa | 479.80 | Calculated Property |
Pvap | 137.55 | kPa | 495.87 | Calculated Property |
Pvap | 202.64 | kPa | 511.94 | Calculated Property |
Pvap | [0.42; 4394.54] | kPa | [345.71; 707.65] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.35548e+02 | |||
Coefficient B | -1.25596e+04 | |||
Coefficient C | -1.72828e+01 | |||
Coefficient D | 7.98314e-06 | |||
Temperature range, min. | 345.71 | |||
Temperature range, max. | 707.65 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 400 500 600 700 | ||||
Pvap | 0.42 | kPa | 345.71 | Calculated Property |
Pvap | 3.53 | kPa | 385.93 | Calculated Property |
Pvap | 17.83 | kPa | 426.14 | Calculated Property |
Pvap | 63.47 | kPa | 466.36 | Calculated Property |
Pvap | 176.15 | kPa | 506.57 | Calculated Property |
Pvap | 408.60 | kPa | 546.79 | Calculated Property |
Pvap | 832.02 | kPa | 587.00 | Calculated Property |
Pvap | 1541.17 | kPa | 627.22 | Calculated Property |
Pvap | 2666.26 | kPa | 667.43 | Calculated Property |
Pvap | 4394.54 | kPa | 707.65 | Calculated Property |
Find more compounds similar to Phenol, 2,4-dimethyl-.
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.