| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6555 | Relay (1.0) Calculated Property | |
| PAff | 829.80 | kJ/mol | NIST |
| BasG | 798.80 | kJ/mol | NIST |
| ΔcH°solid | [-3866.50; -3862.00] | kJ/mol |
|
| ΔcH°solid | -3866.50 ± 0.90 | kJ/mol | NIST |
| ΔcH°solid | -3865.30 ± 0.79 | kJ/mol | NIST |
| ΔcH°solid | -3862.00 | kJ/mol | NIST |
| ΔfG° | -224.65 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-329.10; -327.90] | kJ/mol |
|
| ΔfH°gas | -327.90 ± 1.40 | kJ/mol | NIST |
| ΔfH°gas | -329.10 | kJ/mol | NIST |
| ΔfH°solid | [-426.10; -424.90] | kJ/mol |
|
| ΔfH°solid | -424.90 ± 1.40 | kJ/mol | NIST |
| ΔfH°solid | -426.10 ± 0.96 | kJ/mol | NIST |
| ΔfusH° | 20.27 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [97.00; 97.00] | kJ/mol |
|
| ΔsubH° | 97.00 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 97.00 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 97.00 | kJ/mol | NIST |
| ΔsubH° | 97.00 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 97.00 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 97.00 | kJ/mol | NIST |
| ΔvapH° | 83.30 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.40 ± 0.20 | eV | NIST |
| log10WS | -2.14 | Aq. Solubility Prediction | |
| logPoct/wat | 1.693 | Crippen Calculated Property | |
| McVol | 107.260 | ml/mol | McGowan Calculated Property |
| Pc | 4000.70 | kPa | Joback Calculated Property |
| Inp | [1249.00; 1325.00] |
|
|
| Inp | 1249.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Tboil | 536.20 | K | NIST |
| Tc | 771.00 | K | Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method |
| Tfus | [381.90; 384.40] | K |
|
| Tfus | 382.40 | K | Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements |
| Tfus | 383.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 383.07 | K | Aq. Solubility Prediction |
| Tfus | 384.00 ± 1.50 | K | NIST |
| Tfus | 384.40 ± 2.00 | K | NIST |
| Tfus | 381.90 ± 0.20 | K | NIST |
| Tfus | 381.90 ± 0.20 | K | NIST |
| Vc | 0.388 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,solid | 163.60 | J/mol×K | 298.00 | NIST |
| ΔfusH | [15.73; 15.73] | kJ/mol | [381.90; 381.90] | |
| ΔfusH | 15.73 | kJ/mol | 381.90 | NIST |
| ΔfusH | 15.73 | kJ/mol | 381.90 | NIST |
| ΔfusH | 15.73 | kJ/mol | 381.90 | NIST |
| ΔfusH | 15.73 | kJ/mol | 381.90 | NIST |
| ΔvapH | 62.80 | kJ/mol | 503.00 | NIST |
| ΔfusS | [41.20; 41.20] | J/mol×K | [381.90; 381.90] | |
| ΔfusS | 41.20 | J/mol×K | 381.90 | NIST |
| ΔfusS | 41.20 | J/mol×K | 381.90 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [134.11; 321.27] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -1.93900e+01 | |||
| Coefficient B | 6.76220e-01 | |||
| Coefficient C | -4.48160e-04 | |||
| Coefficient D | 1.12600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 134.11 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 168.74 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 199.08 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 225.48 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 248.31 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 267.92 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 284.66 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 298.90 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 310.98 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 321.27 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0010803; 0.0002728] | Pa×s | [382.97; 539.70] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.15692e+01 | |||
| Coefficient B | 1.81482e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 382.97 | |||
| Temperature range, max. | 539.70 | |||
| η | 0.0010803 | Pa×s | 382.97 | Calculated Property |
| η | 0.0008791 | Pa×s | 400.39 | Calculated Property |
| η | 0.0007278 | Pa×s | 417.80 | Calculated Property |
| η | 0.0006117 | Pa×s | 435.22 | Calculated Property |
| η | 0.0005210 | Pa×s | 452.63 | Calculated Property |
| η | 0.0004491 | Pa×s | 470.04 | Calculated Property |
| η | 0.0003912 | Pa×s | 487.46 | Calculated Property |
| η | 0.0003441 | Pa×s | 504.87 | Calculated Property |
| η | 0.0003052 | Pa×s | 522.29 | Calculated Property |
| η | 0.0002728 | Pa×s | 539.70 | Calculated Property |
Find more compounds similar to M-TOLUIC ACID.
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.
Calculated This icon marks a calculated value or equation: a prediction, not a measurement.
Compiled This icon marks a compiled value or equation: taken from a data compilation such as ChemSep, not from an original measurement report.
These property values are available through the Cheméo API. A free account gives you an access key.