Property | Value | Unit | Source |
---|---|---|---|
PAff | 958.80 | kJ/mol | NIST |
BasG | 926.90 | kJ/mol | NIST |
ΔcH°liquid | -4059.40 | kJ/mol | NIST |
μ | 2.20 | debye | KDB |
ΔfH°gas | [66.40; 66.44] | kJ/mol |
![]() |
ΔfH°gas | 66.44 | kJ/mol | KDB |
ΔfH°gas | 66.40 | kJ/mol | NIST |
ΔfH°liquid | 18.60 | kJ/mol | NIST |
ΔvapH° | 47.82 | kJ/mol | NIST |
IE | 8.80 ± 0.05 | eV | NIST |
log10WS | 0.40 | Aq. Sol... | |
logPoct/wat | 1.698 | Crippen Calculated Property | |
McVol | 95.710 | ml/mol | McGowan Calculated Property |
Inp | [903.20; 946.00] |
![]() |
|
Inp | 919.10 | NIST | |
Inp | 920.00 | NIST | |
Inp | 921.00 | NIST | |
Inp | 917.00 | NIST | |
Inp | 912.00 | NIST | |
Inp | 926.00 | NIST | |
Inp | 913.00 | NIST | |
Inp | 911.00 | NIST | |
Inp | 912.00 | NIST | |
Inp | 912.00 | NIST | |
Inp | 913.00 | NIST | |
Inp | Outlier 946.00 | NIST | |
Inp | 903.20 | NIST | |
Inp | 930.00 | NIST | |
Inp | 919.00 | NIST | |
Inp | 915.00 | NIST | |
Inp | 909.20 | NIST | |
Inp | 917.00 | NIST | |
Inp | 916.00 | NIST | |
Inp | 916.00 | NIST | |
Inp | 928.00 | NIST | |
Inp | 926.00 | NIST | |
Inp | 936.00 | NIST | |
Inp | 928.00 | NIST | |
Inp | 909.20 | NIST | |
Inp | 919.10 | NIST | |
Inp | 926.00 | NIST | |
Inp | 913.00 | NIST | |
Inp | 915.00 | NIST | |
Inp | 936.00 | NIST | |
I | [1325.00; 1415.00] |
![]() |
|
I | 1330.00 | NIST | |
I | 1371.00 | NIST | |
I | 1371.00 | NIST | |
I | 1370.00 | NIST | |
I | 1395.00 | NIST | |
I | 1372.00 | NIST | |
I | 1373.00 | NIST | |
I | 1415.00 | NIST | |
I | 1329.00 | NIST | |
I | 1332.00 | NIST | |
I | 1335.00 | NIST | |
I | 1330.00 | NIST | |
I | 1325.00 | NIST | |
I | 1412.00 | NIST | |
I | 1326.00 | NIST | |
I | 1325.00 | NIST | |
I | 1329.00 | NIST | |
S°liquid | 248.81 | J/mol×K | NIST |
Tboil | [426.25; 431.20] | K |
![]() |
Tboil | 430.16 | K | KDB |
Tboil | 431.20 | K | NIST |
Tboil | 429.90 ± 0.30 | K | NIST |
Tboil | 426.65 ± 3.00 | K | NIST |
Tboil | 429.15 ± 2.00 | K | NIST |
Tboil | 426.25 ± 1.50 | K | NIST |
Tc | [644.15; 644.20] | K |
![]() |
Tc | 644.20 | K | KDB |
Tc | 644.16 ± 0.30 | K | NIST |
Tc | 644.15 ± 1.00 | K | NIST |
Tfus | [257.00; 259.07] | K |
![]() |
Tfus | 257.00 | K | KDB |
Tfus | 259.07 | K | NIST |
Tfus | 257.15 ± 0.50 | K | NIST |
Tfus | 257.61 ± 0.03 | K | NIST |
Ttriple | 259.07 ± 0.01 | K | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,liquid | 184.70 | J/mol×K | 298.15 | NIST |
ΔfusH | [14.64; 14.64] | kJ/mol | [259.10; 259.10] | ![]() |
ΔfusH | 14.64 | kJ/mol | 259.10 | NIST |
ΔfusH | 14.64 | kJ/mol | 259.10 | NIST |
ΔvapH | [36.50; 44.40] | kJ/mol | [394.50; 400.50] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 36 38 40 42 44 396 398 400 | ||||
ΔvapH | 42.80 | kJ/mol | 394.50 | NIST |
ΔvapH | 44.40 | kJ/mol | 400.50 | NIST |
ΔvapH | 41.90 | kJ/mol | 400.50 | NIST |
ΔvapH | 39.40 | kJ/mol | 400.50 | NIST |
ΔvapH | 36.50 | kJ/mol | 400.50 | NIST |
ρl | 938.00 | kg/m3 | 273.00 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [319.12; 458.84] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.46024e+01 | |||
Coefficient B | -3.69877e+03 | |||
Coefficient C | -6.07320e+01 | |||
Temperature range, min. | 319.12 | |||
Temperature range, max. | 458.84 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 319.12 | Calculated Property |
Pvap | 3.00 | kPa | 334.64 | Calculated Property |
Pvap | 6.19 | kPa | 350.17 | Calculated Property |
Pvap | 11.87 | kPa | 365.69 | Calculated Property |
Pvap | 21.35 | kPa | 381.22 | Calculated Property |
Pvap | 36.40 | kPa | 396.74 | Calculated Property |
Pvap | 59.18 | kPa | 412.27 | Calculated Property |
Pvap | 92.35 | kPa | 427.79 | Calculated Property |
Pvap | 139.00 | kPa | 443.32 | Calculated Property |
Pvap | 202.66 | kPa | 458.84 | Calculated Property |
Pvap | [6.77; 114.95] | kPa | [350.00; 435.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.69764e+01 | |||
Coefficient B | -8.86176e+03 | |||
Coefficient C | -1.20654e+01 | |||
Coefficient D | 7.61858e-06 | |||
Temperature range, min. | 350.00 | |||
Temperature range, max. | 435.00 | |||
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 120 360 380 400 420 | ||||
Pvap | 6.77 | kPa | 350.00 | Calculated Property |
Pvap | 10.04 | kPa | 359.44 | Calculated Property |
Pvap | 14.55 | kPa | 368.89 | Calculated Property |
Pvap | 20.62 | kPa | 378.33 | Calculated Property |
Pvap | 28.62 | kPa | 387.78 | Calculated Property |
Pvap | 39.00 | kPa | 397.22 | Calculated Property |
Pvap | 52.25 | kPa | 406.67 | Calculated Property |
Pvap | 68.91 | kPa | 416.11 | Calculated Property |
Pvap | 89.59 | kPa | 425.56 | Calculated Property |
Pvap | 114.95 | kPa | 435.00 | Calculated Property |
Find more compounds similar to Pyridine, 2,5-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.