- InChI
- InChI=1S/C5H8O2/c1-4(2)5(6)7-3/h1H2,2-3H3
- InChI Key
- VVQNEPGJFQJSBK-UHFFFAOYSA-N
- Formula
- C5H8O2
- SMILES
- C=C(C)C(=O)OC
- Molecular Weight1
- 100.12
- CAS
- 80-62-6
- Other Names
-
- 2-(Methoxycarbonyl)-1-propene
- 2-Methyl-2-propenoic acid methyl ester
- 2-Methylacrylic acid, methyl ester
- 2-Methylacrylic, methyl ester
- 2-Propenoic acid, 2-methyl-, methyl ester
- 2-methylpropenoic acid, methyl ester
- Acryester M
- Acrylic acid, 2-methyl-, methyl ester
- CH2=C(CH3)COOCH3
- Diakon
- MMA
- Metakrylan metylu
- Methacrylate de methyle
- Methacrylic acid methyl ester
- Methacrylsaeuremethyl ester
- Methyl 2-methyl-2-propenoate
- Methyl 2-methylpropenoate
- Methyl ester of 2-methyl-2-propenoic acid
- Methyl methacrylate monomer
- Methyl methylacrylate
- Methyl «alpha»-methylacrylate
- Methyl «alpha»-methylacrylate
- Methyl-methacrylat
- Methyl-«alpha»-methacrylate
- Methyl-«alpha»-methacrylate
- Methylester kyseliny methakrylove
- Methylmethacrylaat
- Metil metacrilato
- Monocite methacrylate monomer
- NCI-C50680
- NSC 4769
- Paladon
- Pegalan
- Rcra waste number U162
- TEB 3K
- methacrylic acid, methyl ester
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid 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°liquid : Liquid 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 a given temperature (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).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (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 |
|---|---|---|---|
| PAff | 831.40 | kJ/mol | NIST |
| BasG | 800.50 | kJ/mol | NIST |
| ΔcH°liquid | -2724.60 ± 4.00 | kJ/mol | NIST |
| ΔfG° | -163.41 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-348.70; -331.00] | kJ/mol |
|
| ΔfH°gas | -348.70 | kJ/mol | NIST |
| ΔfH°gas | -342.30 | kJ/mol | NIST |
| ΔfH°gas | -331.00 | kJ/mol | NIST |
| ΔfH°liquid | [-388.80; -382.40] | kJ/mol |
|
| ΔfH°liquid | -382.40 | kJ/mol | NIST |
| ΔfH°liquid | -388.80 ± 4.00 | kJ/mol | NIST |
| ΔfusH° | 8.90 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 40.10 | kJ/mol | NIST |
| IE | [9.70; 10.28] | eV |
|
| IE | 9.70 | eV | NIST |
| IE | 10.06 | eV | NIST |
| IE | 10.28 | eV | NIST |
| log10WS | -0.80 | Aq. Sol... | |
| logPoct/wat | 0.735 | Crippen Calculated Property | |
| McVol | 84.450 | ml/mol | McGowan Calculated Property |
| Pc | 3881.95 | kPa | Joback Calculated Property |
| Inp | [666.00; 732.00] |
|
|
| Inp | 714.30 | NIST | |
| Inp | 717.33 | NIST | |
| Inp | 716.28 | NIST | |
| Inp | 713.44 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 700.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 670.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 710.40 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 710.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 699.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 732.00 | NIST | |
| I | [1002.00; 1010.00] |
|
|
| I | 1010.00 | NIST | |
| I | 1002.00 | NIST | |
| I | 1008.00 | NIST | |
| I | 1002.00 | NIST | |
| I | 1008.00 | NIST | |
| S°liquid | 266.20 | J/mol×K | NIST |
| Tboil | 386.65 | K | Joback Calculated Property |
| Tc | 572.77 | K | Joback Calculated Property |
| Tfus | [225.00; 225.60] | K |
|
| Tfus | 225.26 | K | Aq. Sol... |
| Tfus | 225.60 | K | NIST |
| Tfus | 225.60 | K | NIST |
| Tfus | 225.00 | K | NIST |
| Tfus | 225.60 ± 0.20 | K | NIST |
| Tfus | 225.50 ± 0.20 | K | NIST |
| Tfus | 225.15 ± 0.40 | K | NIST |
| Ttriple | 225.59 ± 0.02 | K | NIST |
| Vc | 0.322 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [149.36; 192.58] | J/mol×K | [386.65; 572.77] |
|
| Cp,gas | 149.36 | J/mol×K | 386.65 | Joback Calculated Property |
| Cp,gas | 157.23 | J/mol×K | 417.67 | Joback Calculated Property |
| Cp,gas | 164.83 | J/mol×K | 448.69 | Joback Calculated Property |
| Cp,gas | 172.17 | J/mol×K | 479.71 | Joback Calculated Property |
| Cp,gas | 179.24 | J/mol×K | 510.73 | Joback Calculated Property |
| Cp,gas | 186.04 | J/mol×K | 541.75 | Joback Calculated Property |
| Cp,gas | 192.58 | J/mol×K | 572.77 | Joback Calculated Property |
| Cp,liquid | [188.49; 215.30] | J/mol×K | [293.00; 300.00] |
|
| Cp,liquid | 188.49 | J/mol×K | 293.00 | NIST |
| Cp,liquid | 191.09 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 215.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 215.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 210.55 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 192.40 | J/mol×K | 300.00 | NIST |
| Cp,solid | 150.20 | J/mol×K | 210.00 | NIST |
| η | [0.0003398; 0.0006808] | Pa×s | [283.15; 353.15] |
|
| η | 0.0006808 | Pa×s | 283.15 | Density... |
| η | 0.0006808 | Pa×s | 283.15 | Excess ... |
| η | 0.0006337 | Pa×s | 288.15 | Excess ... |
| η | 0.0006337 | Pa×s | 288.15 | Density... |
| η | 0.0005899 | Pa×s | 293.15 | Density... |
| η | 0.0005899 | Pa×s | 293.15 | Excess ... |
| η | 0.0005540 | Pa×s | 298.15 | Excess ... |
| η | 0.0005540 | Pa×s | 298.15 | Density... |
| η | 0.0005248 | Pa×s | 303.15 | Density... |
| η | 0.0005248 | Pa×s | 303.15 | Excess ... |
| η | 0.0004956 | Pa×s | 308.15 | Density... |
| η | 0.0004956 | Pa×s | 308.15 | Excess ... |
| η | 0.0004719 | Pa×s | 313.15 | Density... |
| η | 0.0004719 | Pa×s | 313.15 | Excess ... |
| η | 0.0004497 | Pa×s | 318.15 | Density... |
| η | 0.0004497 | Pa×s | 318.15 | Excess ... |
| η | 0.0004294 | Pa×s | 323.15 | Excess ... |
| η | 0.0004294 | Pa×s | 323.15 | Density... |
| η | 0.0004100 | Pa×s | 328.15 | Density... |
| η | 0.0004100 | Pa×s | 328.15 | Excess ... |
| η | 0.0003938 | Pa×s | 333.15 | Excess ... |
| η | 0.0003938 | Pa×s | 333.15 | Density... |
| η | 0.0003636 | Pa×s | 343.15 | Density... |
| η | 0.0003398 | Pa×s | 353.15 | Density... |
| ΔfusH | [12.24; 14.44] | kJ/mol | [225.00; 225.59] |
|
| ΔfusH | 12.24 | kJ/mol | 225.00 | NIST |
| ΔfusH | 12.24 | kJ/mol | 225.00 | NIST |
| ΔfusH | 13.45 | kJ/mol | 225.50 | NIST |
| ΔfusH | 14.44 | kJ/mol | 225.59 | NIST |
| ΔsubH | 60.70 | kJ/mol | 208.50 | NIST |
| ΔvapH | [33.30; 39.00] | kJ/mol | [333.00; 340.50] |
|
| ΔvapH | 37.90 | kJ/mol | 333.00 | NIST |
| ΔvapH | 37.70 | kJ/mol | 333.00 | NIST |
| ΔvapH | 39.00 | kJ/mol | 337.00 | NIST |
| ΔvapH | 38.00 | kJ/mol | 339.00 | NIST |
| ΔvapH | 36.30 ± 0.20 | kJ/mol | 340.50 | NIST |
| ΔvapH | 33.30 ± 0.40 | kJ/mol | 340.50 | NIST |
| ΔvapH | 38.80 ± 0.10 | kJ/mol | 340.50 | NIST |
| ρl | [914.66; 949.10] | kg/m3 | [288.15; 318.15] |
|
| ρl | 949.10 | kg/m3 | 288.15 | Densiti... |
| ρl | 943.37 | kg/m3 | 293.15 | Densiti... |
| ρl | 943.38 | kg/m3 | 293.15 | Densiti... |
| ρl | 937.65 | kg/m3 | 298.15 | Densiti... |
| ρl | 937.63 | kg/m3 | 298.15 | Densiti... |
| ρl | 937.63 | kg/m3 | 298.15 | Volumet... |
| ρl | 937.64 | kg/m3 | 298.15 | Densiti... |
| ρl | 931.90 | kg/m3 | 303.15 | Densiti... |
| ρl | 931.89 | kg/m3 | 303.15 | Densiti... |
| ρl | 926.15 | kg/m3 | 308.15 | Densiti... |
| ρl | 926.16 | kg/m3 | 308.15 | Densiti... |
| ρl | 920.41 | kg/m3 | 313.15 | Densiti... |
| ρl | 920.42 | kg/m3 | 313.15 | Densiti... |
| ρl | 914.66 | kg/m3 | 318.15 | Densiti... |
| ρl | 914.67 | kg/m3 | 318.15 | Densiti... |
| ΔfusS | [59.65; 64.00] | J/mol×K | [225.50; 225.59] |
|
| ΔfusS | 59.65 | J/mol×K | 225.50 | NIST |
| ΔfusS | 64.00 | J/mol×K | 225.59 | NIST |
| csound,fluid | [1152.00; 1182.00] | m/s | [298.15; 308.15] |
|
| csound,fluid | 1181.00 | m/s | 298.15 | Densiti... |
| csound,fluid | 1182.00 | m/s | 298.15 | Densiti... |
| csound,fluid | 1153.00 | m/s | 308.15 | Densiti... |
| csound,fluid | 1152.00 | m/s | 308.15 | Densiti... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.02; 3783.32] | kPa | [224.95; 564.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.28053e+02 | |||
| Coefficient B | -8.95480e+03 | |||
| Coefficient C | -1.71457e+01 | |||
| Coefficient D | 1.47176e-05 | |||
| Temperature range, min. | 224.95 | |||
| Temperature range, max. | 564.00 | |||
| Pvap | 0.02 | kPa | 224.95 | Calculated Property |
| Pvap | 0.58 | kPa | 262.62 | Calculated Property |
| Pvap | 5.74 | kPa | 300.29 | Calculated Property |
| Pvap | 29.95 | kPa | 337.97 | Calculated Property |
| Pvap | 103.59 | kPa | 375.64 | Calculated Property |
| Pvap | 273.70 | kPa | 413.31 | Calculated Property |
| Pvap | 605.13 | kPa | 450.98 | Calculated Property |
| Pvap | 1189.92 | kPa | 488.66 | Calculated Property |
| Pvap | 2170.45 | kPa | 526.33 | Calculated Property |
| Pvap | 3783.32 | kPa | 564.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Methyl methacrylate.
Mixtures
- 1-Butanol, 3-methyl-, acetate + Methyl methacrylate
- Toluene + Methyl methacrylate
- Methyl methacrylate + 2-Propenoic acid, butyl ester
- Toluene + Methyl methacrylate + 2-Propenoic acid, butyl ester
- Formamide, N,N-dimethyl- + Methyl methacrylate
- N,N-Dimethylacetamide + Methyl methacrylate
- Acetonitrile + Methyl methacrylate
- Benzonitrile + Methyl methacrylate
- Benzene + Ethanol, 2-butoxy- + Methyl methacrylate
- Toluene + Ethanol, 2-butoxy- + Methyl methacrylate
- Ethanol, 2-butoxy- + p-Xylene + Methyl methacrylate
- Benzene + n-Butyl ether + Methyl methacrylate
- Toluene + n-Butyl ether + Methyl methacrylate
- p-Xylene + n-Butyl ether + Methyl methacrylate
- 1-Butanol + Methyl methacrylate + Cyclohexane
- Benzene + 1-Butanol + Methyl methacrylate
- Toluene + 1-Butanol + Methyl methacrylate
- p-Xylene + 1-Butanol + Methyl methacrylate
- 1-Butanol + Ethylbenzene + Methyl methacrylate
- 1-Pentanol + Methyl methacrylate + Cyclohexane
Find more mixtures with Methyl methacrylate.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Volumetric Properties of 3-Methylbutyl Ethanoate with Ethyl Acrylate, Butyl Acrylate, Methyl Methacrylate, and Styrene at 25 C
- Liquid liquid equilibria for the ternary systems water + 1-propanol + methyl methacrylate, +butyl methacrylate, and +isobutyl methacrylate
- Liquid liquid equilibria of water + 1-butanol + methyl methacrylate or butyl methacrylate or isobutyl methacrylate at 288.15K and 318.15K
- Liquid-liquid equilibria for systems of water + methanol + methyl anthranilate at several temperatures
- Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K
- Combined effects of salinity and temperature on the solubility of organic compounds
- Densities, ultrasonic speeds, viscosities and excess properties of binary mixtures of methyl methacrylate with N,N-dimethylformamide and N,N-dimethylacetamide at different temperatures
- 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
- Densities, Excess Molar Volumes at T = (298.15 to 313.15) K, Speeds of Sound, Excess Isentropic Compressibilities, Relative Permittivities and Deviations in Molar Polarizations at T = (298.15 and 308.15) K for Methyl Methacrylate + 2-Butoxyethanol or + Dibutyl Ether + Benzene, + Toluene and + p-Xylene
- Methyl Methacrylate + Carbon Dioxide Phase Equilibria at High Pressures
- Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Liquid-Liquid Equilibria for the Ternary Systems Water + 2-Propanol + Methyl Methacrylate, + Butyl Methacrylate, and + Isobutyl Methacrylate
- Liquid-Liquid Equilibria of Water + 2-Butanol + (Methyl Methacrylate or Butyl Methacrylate or Isobutyl Methacrylate) at (288.2 and 318.2) K
- Phase Behavior Studies of 2-Hydroxyethyl Methacrylate and Methyl Methacrylate in High-Pressure Carbon Dioxide
- Excess Molar Volume and Viscosity Deviation for the Methanol + Methyl Methacrylate Binary System at T) (283.15 to 333.15) K
- Density, Excess Molar Volume, and Viscosity for the Methyl Methacrylate + 1-Butyl-3-methylimidazolium Hexafluorophosphate Ionic Liquid Binary System at Atmospheric Pressure
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
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.