- InChI
- InChI=1S/C6H10O2/c1-4-8-6(7)5(2)3/h2,4H2,1,3H3
- InChI Key
- SUPCQIBBMFXVTL-UHFFFAOYSA-N
- Formula
- C6H10O2
- SMILES
- C=C(C)C(=O)OCC
- Molecular Weight1
- 114.14
- CAS
- 97-63-2
- Other Names
-
- 2-Methyl-2-propenoic acid ethyl ester
- 2-Methylacrylic acid, ethyl ester
- 2-Propenoic acid, 2-methyl-, ethyl ester
- 2-methylpropenoic acid, ethyl ester
- EMA
- ETHYL 2-METHYL-2-PROPENOATE
- ETHYL METHYL ACRYLATE
- Ethyl 2-methacrylate
- Ethyl 2-methylacrylate
- Ethyl methacrylate
- Ethyl methylacrylate
- Ethyl «alpha»-methyl acrylate
- Ethyl «alpha»-methyl acrylate
- Ethylester kyseliny methakrylove
- NSC 24152
- Rcra waste number U118
- Rhoplex AC-33
- UN 2277
- ethyl 2-methylpropenoate
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- 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).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- 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 |
|---|---|---|---|
| ΔfG° | -154.99 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -296.33 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 11.49 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 37.52 | kJ/mol | Joback Calculated Property |
| log10WS | -1.05 | Crippen Calculated Property | |
| logPoct/wat | 1.126 | Crippen Calculated Property | |
| McVol | 98.540 | ml/mol | McGowan Calculated Property |
| Pc | 3456.14 | kPa | Joback Calculated Property |
| Inp | [756.00; 814.00] |
|
|
| Inp | 768.00 | NIST | |
| Inp | 773.00 | NIST | |
| Inp | 770.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 756.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 773.00 | NIST | |
| Inp | 775.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 773.00 | NIST | |
| I | [1043.00; 1046.00] |
|
|
| I | 1046.00 | NIST | |
| I | 1043.00 | NIST | |
| Tboil | 391.70 | K | NIST |
| Tc | 594.44 | K | Joback Calculated Property |
| Tfus | 213.82 | K | Joback Calculated Property |
| Vc | 0.378 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [184.88; 235.83] | J/mol×K | [409.53; 594.44] |
|
| Cp,gas | 184.88 | J/mol×K | 409.53 | Joback Calculated Property |
| Cp,gas | 194.21 | J/mol×K | 440.35 | Joback Calculated Property |
| Cp,gas | 203.19 | J/mol×K | 471.17 | Joback Calculated Property |
| Cp,gas | 211.85 | J/mol×K | 501.99 | Joback Calculated Property |
| Cp,gas | 220.17 | J/mol×K | 532.81 | Joback Calculated Property |
| Cp,gas | 228.17 | J/mol×K | 563.63 | Joback Calculated Property |
| Cp,gas | 235.83 | J/mol×K | 594.44 | Joback Calculated Property |
| ΔvapH | 38.30 | kJ/mol | 337.50 | NIST |
| ρl | [886.71; 912.30] | kg/m3 | [293.15; 318.15] |
|
| ρl | 912.30 | kg/m3 | 293.15 | Densiti... |
| ρl | 907.18 | kg/m3 | 298.15 | Densiti... |
| ρl | 902.06 | kg/m3 | 303.15 | Densiti... |
| ρl | 896.94 | kg/m3 | 308.15 | Densiti... |
| ρl | 891.83 | kg/m3 | 313.15 | Densiti... |
| ρl | 886.71 | kg/m3 | 318.15 | Densiti... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 303.20 | K | 2.40 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [284.64; 418.33] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.43808e+01 | |||
| Coefficient B | -3.40126e+03 | |||
| Coefficient C | -4.32990e+01 | |||
| Temperature range, min. | 284.64 | |||
| Temperature range, max. | 418.33 | |||
| Pvap | 1.33 | kPa | 284.64 | Calculated Property |
| Pvap | 3.02 | kPa | 299.49 | Calculated Property |
| Pvap | 6.25 | kPa | 314.35 | Calculated Property |
| Pvap | 11.99 | kPa | 329.20 | Calculated Property |
| Pvap | 21.58 | kPa | 344.06 | Calculated Property |
| Pvap | 36.75 | kPa | 358.91 | Calculated Property |
| Pvap | 59.65 | kPa | 373.77 | Calculated Property |
| Pvap | 92.88 | kPa | 388.62 | Calculated Property |
| Pvap | 139.42 | kPa | 403.48 | Calculated Property |
| Pvap | 202.66 | kPa | 418.33 | Calculated Property |
| Pvap | [0.01; 3234.04] | kPa | [223.15; 577.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.23555e+01 | |||
| Coefficient B | -6.60736e+03 | |||
| Coefficient C | -6.93770e+00 | |||
| Coefficient D | 3.86286e-06 | |||
| Temperature range, min. | 223.15 | |||
| Temperature range, max. | 577.00 | |||
| Pvap | 0.01 | kPa | 223.15 | Calculated Property |
| Pvap | 0.30 | kPa | 262.47 | Calculated Property |
| Pvap | 3.32 | kPa | 301.78 | Calculated Property |
| Pvap | 19.54 | kPa | 341.10 | Calculated Property |
| Pvap | 75.72 | kPa | 380.42 | Calculated Property |
| Pvap | 219.89 | kPa | 419.73 | Calculated Property |
| Pvap | 519.91 | kPa | 459.05 | Calculated Property |
| Pvap | 1058.35 | kPa | 498.37 | Calculated Property |
| Pvap | 1928.44 | kPa | 537.68 | Calculated Property |
| Pvap | 3234.04 | kPa | 577.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Methacrylic acid, ethyl ester.
Mixtures
- Acetonitrile + Methacrylic acid, ethyl ester
- Benzonitrile + Methacrylic acid, ethyl ester
- Carbon dioxide + Methacrylic acid, ethyl ester
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
- Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
- Densities, speeds of sound and excess properties of (benzonitrile + methyl methacrylate, or + ethyl methacrylate, or + n-butyl methacrylate) binary mixtures at temperatures from 293.15 K to 318.15 K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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