- InChI
- InChI=1S/C9H10O2/c1-7-3-5-8(6-4-7)9(10)11-2/h3-6H,1-2H3
- InChI Key
- QSSJZLPUHJDYKF-UHFFFAOYSA-N
- Formula
- C9H10O2
- SMILES
- COC(=O)c1ccc(C)cc1
- Molecular Weight1
- 150.17
- CAS
- 99-75-2
- Other Names
-
- 4-(Methoxycarbonyl)toluene
- 4-Methylbenzoic acid, methyl ester
- Methyl 4-toluate
- Methyl ester of 4-methylbenzoic acid
- Methyl p-toluenecarboxylate
- NSC 24761
- methyl 4-methylbenzoate
- methyl p-methylbenzoate
- methyl p-toluate
- p-(Methoxycarbonyl)toluene
- p-Carbomethoxytoluene
- p-Toluylic acid, methyl ester
- p-toluic acid, methyl ester
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas 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).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (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).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4906 | Relay (1.0) Calculated Property | |
| PAff | 861.50 | kJ/mol | NIST |
| BasG | 830.60 | kJ/mol | NIST |
| ΔfG° | -106.24 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -312.60 ± 6.70 | kJ/mol | NIST |
| ΔfH°solid | -393.30 ± 2.40 | kJ/mol | NIST |
| ΔfusH° | 20.20 | kJ/mol | Vapor Pressures and Phase Diagrams of Two Methyl Esters of Substituted Benzoic Acids |
| ΔsubH° | [80.60; 83.30] | kJ/mol |
|
| ΔsubH° | 83.30 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 80.60 ± 6.30 | kJ/mol | NIST |
| ΔsubH° | 80.70 | kJ/mol | NIST |
| ΔvapH° | 64.54 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [8.40; 9.00] | eV |
|
| IE | 8.40 | eV | NIST |
| IE | 8.94 ± 0.04 | eV | NIST |
| IE | 9.00 | eV | NIST |
| log10WS | -2.63 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.782 | Crippen Calculated Property | |
| McVol | 121.350 | ml/mol | McGowan Calculated Property |
| Pc | 3380.21 | kPa | Joback Calculated Property |
| Inp | [205.66; 1215.60] |
|
|
| Inp | 1215.00 | NIST | |
| Inp | 1215.60 | NIST | |
| Inp | 1194.00 | NIST | |
| Inp | 1199.00 | NIST | |
| Inp | Outlier 205.66 | NIST | |
| Inp | 1215.60 | NIST | |
| I | [1725.00; 1755.00] |
|
|
| I | 1725.00 | NIST | |
| I | 1755.00 | NIST | |
| Tboil | 489.97 | K | Relay (1.0) Calculated Property |
| Tc | 694.16 | K | Relay (1.0) Calculated Property |
| Tfus | 312.32 | K | Relay (1.0) Calculated Property |
| Vc | 0.445 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [256.24; 320.16] | J/mol×K | [513.27; 730.64] |
|
| Cp,gas | 256.24 | J/mol×K | 513.27 | Joback Calculated Property |
| Cp,gas | 268.48 | J/mol×K | 549.50 | Joback Calculated Property |
| Cp,gas | 280.07 | J/mol×K | 585.73 | Joback Calculated Property |
| Cp,gas | 291.03 | J/mol×K | 621.95 | Joback Calculated Property |
| Cp,gas | 301.35 | J/mol×K | 658.18 | Joback Calculated Property |
| Cp,gas | 311.06 | J/mol×K | 694.41 | Joback Calculated Property |
| Cp,gas | 320.16 | J/mol×K | 730.64 | Joback Calculated Property |
| η | [0.0002227; 0.0017319] | Pa×s | [302.29; 513.27] |
|
| η | 0.0017319 | Pa×s | 302.29 | Joback Calculated Property |
| η | 0.0010297 | Pa×s | 337.45 | Joback Calculated Property |
| η | 0.0006754 | Pa×s | 372.62 | Joback Calculated Property |
| η | 0.0004764 | Pa×s | 407.78 | Joback Calculated Property |
| η | 0.0003552 | Pa×s | 442.94 | Joback Calculated Property |
| η | 0.0002765 | Pa×s | 478.11 | Joback Calculated Property |
| η | 0.0002227 | Pa×s | 513.27 | Joback Calculated Property |
| ΔfusH | [20.77; 20.78] | kJ/mol | [162.50; 306.50] |
|
| ΔfusH | 20.78 | kJ/mol | 162.50 | NIST |
| ΔfusH | 20.77 | kJ/mol | 306.50 | NIST |
| ΔsubH | 51.60 | kJ/mol | 448.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 376.70 | K | 2.00 | NIST |
Similar Compounds
![1,4-Benzenedicarboxylic acid, [4-(methoxycarbonyl)phenyl]methyl methyl ester.](data:image/png;base64,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)
Find more compounds similar to Benzoic acid, 4-methyl-, methyl ester.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Vapor Pressures and Phase Diagrams of Two Methyl Esters of Substituted Benzoic Acids
- Joback Method
- McGowan Method
- NIST Webbook
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that the value is more than 2 standard deviations away from the
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