- InChI
- InChI=1S/C8H8O2/c1-6-2-4-7(5-3-6)8(9)10/h2-5H,1H3,(H,9,10)
- InChI Key
- LPNBBFKOUUSUDB-UHFFFAOYSA-N
- Formula
- C8H8O2
- SMILES
- Cc1ccc(C(=O)O)cc1
- Molecular Weight1
- 136.15
- CAS
- 99-94-5
- Other Names
-
- 4-Toluic acid
- 4-methylbenzoic acid
- Crithminic acid
- NSC 2215
- p-Carboxytoluene
- p-Methylbenzoic acid
- p-Toluylic acid
- p-Tolylcarboxylic acid
- p-toluic acid
- para-Toluic acid
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6610 | ChemSep v8.3 pure component data Compiled value | |
| PAff | 836.70 | kJ/mol | NIST |
| BasG | 805.70 | kJ/mol | NIST |
| ΔcH°solid | [-3868.00; -3862.30] | kJ/mol |
|
| ΔcH°solid | -3862.30 ± 0.90 | kJ/mol | NIST |
| ΔcH°solid | -3862.30 ± 0.92 | kJ/mol | NIST |
| ΔcH°solid | -3868.00 | kJ/mol | NIST |
| ΔfG° | -213.35 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-330.40; -322.80] | kJ/mol |
|
| ΔfH°gas | -322.80 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -330.40 ± 1.50 | kJ/mol | NIST |
| ΔfH°gas | -330.40 | kJ/mol | NIST |
| ΔfH°gas | -324.50 | kJ/mol | NIST |
| ΔfH°solid | [-429.20; -423.30] | kJ/mol |
|
| ΔfH°solid | -429.20 ± 1.50 | kJ/mol | NIST |
| ΔfH°solid | -429.20 ± 1.10 | kJ/mol | NIST |
| ΔfH°solid | -423.30 ± 3.80 | kJ/mol | NIST |
| ΔfusH° | 22.48 | kJ/mol | Thermodynamic study of the sublimation of eight 4-n-alkylbenzoic acids |
| ΔsubH° | [98.60; 98.80] | kJ/mol |
|
| ΔsubH° | Outlier 98.60 ± 0.60 | kJ/mol | NIST |
| ΔsubH° | 98.80 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 98.80 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 98.80 | kJ/mol | NIST |
| ΔsubH° | 98.80 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 98.80 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 98.80 | kJ/mol | NIST |
| ΔvapH° | 84.77 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [9.20; 9.40] | eV |
|
| IE | 9.20 ± 0.20 | eV | NIST |
| IE | 9.40 | eV | NIST |
| log10WS | -2.60 | Aq. Solubility Prediction | |
| logPoct/wat | 1.693 | Crippen Calculated Property | |
| McVol | 107.260 | ml/mol | McGowan Calculated Property |
| Pc | 3860.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 5.21 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1213.00; 1213.00] |
|
|
| Inp | 1213.00 | NIST | |
| Inp | 1213.00 | NIST | |
| Inp | 1213.00 | NIST | |
| Tboil | [547.70; 548.15] | K |
|
| Tboil | 548.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 547.70 | K | NIST |
| Tc | [773.00; 775.00] | K |
|
| Tc | 775.00 | K | Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method |
| Tc | 773.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [450.15; 455.10] | K |
|
| Tfus | 453.30 | K | Benzoic acid derivatives: Evaluation of thermochemical properties with complementary experimental and computational methods |
| Tfus | 452.10 | K | Melting Point, Enthalpy of Fusion, and Heat Capacity Measurements of Several Polyfunctional, Industrially Important Compounds by Differential Scanning Calorimetry |
| Tfus | 455.10 | K | Solid-Liquid Equilibria for Benzoic Acid + p-Toluic Acid + Chloroform, Benzoic Acid + p-Toluic Acid + Acetic Acid, and Terephthalic Acid + Isophthalic Acid + N,N-Dimethylformamide |
| Tfus | 453.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 452.75 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 453.46 | K | Aq. Solubility Prediction |
| Tfus | 455.00 ± 2.00 | K | NIST |
| Tfus | Outlier 450.15 ± 2.50 | K | NIST |
| Tfus | 452.80 ± 0.30 | K | NIST |
| Tfus | 452.80 ± 0.30 | K | NIST |
| Ttriple | 452.75 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 3.91 | ChemSep v8.3 pure component data Compiled value | |
| URi | 5.06 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.397 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2380000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.24 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,solid | 169.00 | J/mol×K | 298.00 | NIST |
| ΔfusH | [22.72; 22.72] | kJ/mol | [452.80; 452.80] |
|
| ΔfusH | 22.72 | kJ/mol | 452.80 | NIST |
| ΔfusH | 22.72 | kJ/mol | 452.80 | NIST |
| ΔfusH | 22.72 | kJ/mol | 452.80 | NIST |
| ΔfusH | 22.72 | kJ/mol | 452.80 | NIST |
| ΔfusS | [50.20; 50.20] | J/mol×K | [452.80; 452.80] |
|
| ΔfusS | 50.20 | J/mol×K | 452.80 | NIST |
| ΔfusS | 50.20 | J/mol×K | 452.80 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [116.92; 312.36] | J/mol×K | [273.00; 1000.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 8.59490e+01 | |||
| Coefficient B | -9.29050e+02 | |||
| Coefficient C | 7.15724e+00 | |||
| Coefficient D | -1.31450e-03 | |||
| Coefficient E | 5.08580e-07 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.15 | |||
| Cp,gas | 116.92 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 148.12 | J/mol×K | 353.79 | Calculated Property |
| Cp,gas | 180.04 | J/mol×K | 434.59 | Calculated Property |
| Cp,gas | 208.95 | J/mol×K | 515.38 | Calculated Property |
| Cp,gas | 233.77 | J/mol×K | 596.18 | Calculated Property |
| Cp,gas | 254.64 | J/mol×K | 676.97 | Calculated Property |
| Cp,gas | 272.21 | J/mol×K | 757.77 | Calculated Property |
| Cp,gas | 287.22 | J/mol×K | 838.56 | Calculated Property |
| Cp,gas | 300.40 | J/mol×K | 919.36 | Calculated Property |
| Cp,gas | 312.36 | J/mol×K | 1000.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [283.25; 309.17] | J/mol×K | [452.75; 548.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 2.04240e+02 | |||
| Coefficient B | 5.58580e+02 | |||
| Coefficient C | -1.82676e+00 | |||
| Coefficient D | 1.56990e-02 | |||
| Coefficient E | -1.04650e-05 | |||
| Temperature range, min. | 452.75 | |||
| Temperature range, max. | 548.15 | |||
| Cp,liquid | 283.25 | J/mol×K | 452.75 | Calculated Property |
| Cp,liquid | 286.19 | J/mol×K | 463.35 | Calculated Property |
| Cp,liquid | 289.15 | J/mol×K | 473.95 | Calculated Property |
| Cp,liquid | 292.11 | J/mol×K | 484.55 | Calculated Property |
| Cp,liquid | 295.07 | J/mol×K | 495.15 | Calculated Property |
| Cp,liquid | 298.00 | J/mol×K | 505.75 | Calculated Property |
| Cp,liquid | 300.89 | J/mol×K | 516.35 | Calculated Property |
| Cp,liquid | 303.72 | J/mol×K | 526.95 | Calculated Property |
| Cp,liquid | 306.49 | J/mol×K | 537.55 | Calculated Property |
| Cp,liquid | 309.17 | J/mol×K | 548.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0006661; 0.0001699] | Pa×s | [452.75; 598.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.63930e+01 | |||
| Coefficient B | 2.71750e+03 | |||
| Coefficient C | 5.14370e-01 | |||
| Coefficient D | -3.36080e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 452.75 | |||
| Temperature range, max. | 598.00 | |||
| η | 0.0006661 | Pa×s | 452.75 | Calculated Property |
| η | 0.0005488 | Pa×s | 468.89 | Calculated Property |
| η | 0.0004581 | Pa×s | 485.03 | Calculated Property |
| η | 0.0003869 | Pa×s | 501.17 | Calculated Property |
| η | 0.0003303 | Pa×s | 517.31 | Calculated Property |
| η | 0.0002846 | Pa×s | 533.44 | Calculated Property |
| η | 0.0002474 | Pa×s | 549.58 | Calculated Property |
| η | 0.0002167 | Pa×s | 565.72 | Calculated Property |
| η | 0.0001913 | Pa×s | 581.86 | Calculated Property |
| η | 0.0001699 | Pa×s | 598.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [66.85; 21.67] | kJ/mol | [452.75; 756.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 1.02990e+02 | |||
| Coefficient B | 9.46530e-01 | |||
| Coefficient C | -1.47400e+00 | |||
| Coefficient D | 1.55040e+00 | |||
| Coefficient E | -6.20440e-01 | |||
| Critical temperature, Tc (K) | 7.73000e+02 | |||
| Temperature range, min. | 452.75 | |||
| Temperature range, max. | 756.15 | |||
| ΔvapH | 66.85 | kJ/mol | 452.75 | Calculated Property |
| ΔvapH | 64.07 | kJ/mol | 486.46 | Calculated Property |
| ΔvapH | 61.07 | kJ/mol | 520.17 | Calculated Property |
| ΔvapH | 57.81 | kJ/mol | 553.88 | Calculated Property |
| ΔvapH | 54.22 | kJ/mol | 587.59 | Calculated Property |
| ΔvapH | 50.21 | kJ/mol | 621.31 | Calculated Property |
| ΔvapH | 45.62 | kJ/mol | 655.02 | Calculated Property |
| ΔvapH | 40.14 | kJ/mol | 688.73 | Calculated Property |
| ΔvapH | 33.06 | kJ/mol | 722.44 | Calculated Property |
| ΔvapH | 21.67 | kJ/mol | 756.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [421.56; 577.86] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.54810e+01 | |||
| Coefficient B | -4.80703e+03 | |||
| Coefficient C | -1.05173e+02 | |||
| Temperature range, min. | 421.56 | |||
| Temperature range, max. | 577.86 | |||
| Pvap | 1.33 | kPa | 421.56 | Calculated Property |
| Pvap | 2.94 | kPa | 438.93 | Calculated Property |
| Pvap | 5.99 | kPa | 456.29 | Calculated Property |
| Pvap | 11.42 | kPa | 473.66 | Calculated Property |
| Pvap | 20.55 | kPa | 491.03 | Calculated Property |
| Pvap | 35.14 | kPa | 508.39 | Calculated Property |
| Pvap | 57.49 | kPa | 525.76 | Calculated Property |
| Pvap | 90.46 | kPa | 543.13 | Calculated Property |
| Pvap | 137.49 | kPa | 560.49 | Calculated Property |
| Pvap | 202.64 | kPa | 577.86 | Calculated Property |
| Pvap | [4.59; 3866.97] | kPa | [450.00; 773.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.73882e+02 | |||
| Coefficient B | -1.69010e+04 | |||
| Coefficient C | -2.23270e+01 | |||
| Coefficient D | 7.90410e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 450.00 | |||
| Temperature range, max. | 773.00 | |||
| Pvap | 4.59 | kPa | 450.00 | Calculated Property |
| Pvap | 17.29 | kPa | 485.89 | Calculated Property |
| Pvap | 51.29 | kPa | 521.78 | Calculated Property |
| Pvap | 126.86 | kPa | 557.67 | Calculated Property |
| Pvap | 273.04 | kPa | 593.56 | Calculated Property |
| Pvap | 528.11 | kPa | 629.44 | Calculated Property |
| Pvap | 940.96 | kPa | 665.33 | Calculated Property |
| Pvap | 1574.46 | kPa | 701.22 | Calculated Property |
| Pvap | 2511.80 | kPa | 737.11 | Calculated Property |
| Pvap | 3866.97 | kPa | 773.00 | Calculated Property |
| Pvap | [5.17; 3829.19] | kPa | [452.75; 773.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46674e+02 | |||
| Coefficient B | -1.53125e+04 | |||
| Coefficient C | -1.83932e+01 | |||
| Coefficient D | 6.20185e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 452.75 | |||
| Temperature range, max. | 773.00 | |||
| Pvap | 5.17 | kPa | 452.75 | Calculated Property |
| Pvap | 18.61 | kPa | 488.33 | Calculated Property |
| Pvap | 53.69 | kPa | 523.92 | Calculated Property |
| Pvap | 130.64 | kPa | 559.50 | Calculated Property |
| Pvap | 278.55 | kPa | 595.08 | Calculated Property |
| Pvap | 535.78 | kPa | 630.67 | Calculated Property |
| Pvap | 950.63 | kPa | 666.25 | Calculated Property |
| Pvap | 1583.31 | kPa | 701.83 | Calculated Property |
| Pvap | 2509.94 | kPa | 737.42 | Calculated Property |
| Pvap | 3829.19 | kPa | 773.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1048.77; 343.57] | kg/m3 | [452.75; 773.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 8.17691e+01 | |||
| Coefficient B | 2.38000e-01 | |||
| Coefficient C | 7.73000e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Temperature range, min. | 452.75 | |||
| Temperature range, max. | 773.00 | |||
| ρl | 1048.77 | kg/m3 | 452.75 | Calculated Property |
| ρl | 1010.74 | kg/m3 | 488.33 | Calculated Property |
| ρl | 970.73 | kg/m3 | 523.92 | Calculated Property |
| ρl | 928.25 | kg/m3 | 559.50 | Calculated Property |
| ρl | 882.58 | kg/m3 | 595.08 | Calculated Property |
| ρl | 832.62 | kg/m3 | 630.67 | Calculated Property |
| ρl | 776.45 | kg/m3 | 666.25 | Calculated Property |
| ρl | 710.20 | kg/m3 | 701.83 | Calculated Property |
| ρl | 623.33 | kg/m3 | 737.42 | Calculated Property |
| ρl | 343.57 | kg/m3 | 773.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 7.80e-04] | N/m | [452.75; 756.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -9.34290e-03 | |||
| Coefficient B | 9.92570e+02 | |||
| Coefficient C | -8.47630e+00 | |||
| Coefficient D | 1.18920e-02 | |||
| Coefficient E | -1.12310e-05 | |||
| Temperature range, min. | 452.75 | |||
| Temperature range, max. | 756.15 | |||
| γ | 0.03 | N/m | 452.75 | Calculated Property |
| γ | 0.03 | N/m | 486.46 | Calculated Property |
| γ | 0.02 | N/m | 520.17 | Calculated Property |
| γ | 0.02 | N/m | 553.88 | Calculated Property |
| γ | 0.02 | N/m | 587.59 | Calculated Property |
| γ | 0.01 | N/m | 621.31 | Calculated Property |
| γ | 0.01 | N/m | 655.02 | Calculated Property |
| γ | 0.01 | N/m | 688.73 | Calculated Property |
| γ | 0.00 | N/m | 722.44 | Calculated Property |
| γ | 7.80e-04 | N/m | 756.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.05] | W/m×K | [274.00; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 2.97700e-05 | |||
| Coefficient B | 1.12140e+00 | |||
| Coefficient C | 2.06560e+02 | |||
| Coefficient D | 6.20020e+04 | |||
| Temperature range, min. | 274.00 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 274.00 | Calculated Property |
| λgas | 0.01 | W/m×K | 354.67 | Calculated Property |
| λgas | 0.02 | W/m×K | 435.33 | Calculated Property |
| λgas | 0.02 | W/m×K | 516.00 | Calculated Property |
| λgas | 0.03 | W/m×K | 596.67 | Calculated Property |
| λgas | 0.03 | W/m×K | 677.33 | Calculated Property |
| λgas | 0.04 | W/m×K | 758.00 | Calculated Property |
| λgas | 0.04 | W/m×K | 838.67 | Calculated Property |
| λgas | 0.05 | W/m×K | 919.33 | Calculated Property |
| λgas | 0.05 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.19; 0.10] | W/m×K | [231.90; 611.90] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -1.40950e-01 | |||
| Coefficient B | 2.91180e+01 | |||
| Coefficient C | -1.21240e+00 | |||
| Coefficient D | 4.91040e-05 | |||
| Coefficient E | -7.63740e-07 | |||
| Temperature range, min. | 231.90 | |||
| Temperature range, max. | 611.90 | |||
| λliquid | 0.19 | W/m×K | 231.90 | Calculated Property |
| λliquid | 0.18 | W/m×K | 274.12 | Calculated Property |
| λliquid | 0.17 | W/m×K | 316.34 | Calculated Property |
| λliquid | 0.16 | W/m×K | 358.57 | Calculated Property |
| λliquid | 0.15 | W/m×K | 400.79 | Calculated Property |
| λliquid | 0.14 | W/m×K | 443.01 | Calculated Property |
| λliquid | 0.13 | W/m×K | 485.23 | Calculated Property |
| λliquid | 0.12 | W/m×K | 527.46 | Calculated Property |
| λliquid | 0.11 | W/m×K | 569.68 | Calculated Property |
| λliquid | 0.10 | W/m×K | 611.90 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzoic acid, 4-methyl-.
Mixtures
- Benzoic acid, 4-methyl- + Water
- p-Xylene + Benzoic acid, 4-methyl-
- p-Xylene + Benzoic acid, 4-methyl- + Water
- Acetic acid, 2-methylpropyl ester + Benzoic acid, 4-methyl-
- Formamide, N,N-dimethyl- + Benzoic acid, 4-methyl-
- Benzoic acid + Trichloromethane + Benzoic acid, 4-methyl-
- Benzoic acid + Benzoic acid, 4-methyl- + Acetic acid
- Benzoic acid, 4-methyl- + Acetic acid
- Benzoic acid, 4-methyl- + Acetic acid + Water
- 1-Octanol + Benzoic acid, 4-methyl-
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- The effect of temperature on the solubility of benzoic acid derivatives in water
- Determination and modeling of aqueous solubility of 4-position substituted benzoic acid compounds in a high-temperature solution
- Solubility and partition coefficient of p-toluic acid in p-xylene and water
- Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
- Thermodynamic study of the sublimation of eight 4-n-alkylbenzoic acids
- Benzoic acid derivatives: Evaluation of thermochemical properties with complementary experimental and computational methods
- Measurement and Correlation of the Solubility for Camptothecine in Different Organic Solvents
- Melting Point, Enthalpy of Fusion, and Heat Capacity Measurements of Several Polyfunctional, Industrially Important Compounds by Differential Scanning Calorimetry
- Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
- Solid-Liquid Equilibria of Several Systems Containing Acetic Acid
- Solid-Liquid Equilibria for Benzoic Acid + p-Toluic Acid + Chloroform, Benzoic Acid + p-Toluic Acid + Acetic Acid, and Terephthalic Acid + Isophthalic Acid + N,N-Dimethylformamide
- Solubilities of Benzene Carboxylic Acids in Isobutyl Acetate from (299.73 to 353.15) K
- Solubilities of Benzoic Acid, p-Methylbenzoic Acid, m-Methylbenzoic Acid, o-Methylbenzoic Acid, p-Hydroxybenzoic Acid, and o-Nitrobenzoic Acid in 1-Octanol
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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