- InChI
- InChI=1S/C4H6O2/c1-3-4(5)6-2/h3H,1H2,2H3
- InChI Key
- BAPJBEWLBFYGME-UHFFFAOYSA-N
- Formula
- C4H6O2
- SMILES
- C=CC(=O)OC
- Molecular Weight1
- 86.09
- CAS
- 96-33-3
- Other Names
-
- Acrylate de methyle
- Acrylic acid methyl ester
- Acrylsaeuremethylester
- CH2=CHCOOCH3
- Curithane 103
- METHOXYCARBONYLETHYLENE
- METHYL PROPENOATE
- Methyl 2-propenoate
- Methyl acrylate
- Methyl ester acrylic acid
- Methyl ester of 2-propenoic acid
- Methyl prop-2-enoate
- Methyl propenate
- Methyl-acrylat
- Methylacrylaat
- Methylester kyseliny akrylove
- Metilacrilato
- NSC 24146
- UN 1919
- acrylic acid, methyl ester
- propenoic acid, methyl ester
- ω : Acentric Factor.
- 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).
- 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- 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).
- 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).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3500 | KDB | |
| PAff | 825.80 | kJ/mol | NIST |
| BasG | 794.80 | kJ/mol | NIST |
| ΔcH°liquid | -2069.40 ± 0.67 | kJ/mol | NIST |
| ΔfG° | -163.28 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -333.00 | kJ/mol | NIST |
| ΔfH°liquid | -362.20 | kJ/mol | NIST |
| ΔfusH° | 7.62 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [29.20; 29.20] | kJ/mol |
|
| ΔvapH° | 29.20 | kJ/mol | NIST |
| ΔvapH° | 29.20 | kJ/mol | NIST |
| IE | [9.90; 10.74] | eV |
|
| IE | 9.90 | eV | NIST |
| IE | 10.74 | eV | NIST |
| IE | 10.72 | eV | NIST |
| log10WS | [-0.22; -0.22] |
|
|
| log10WS | -0.22 | Aq. Sol... | |
| log10WS | -0.22 | Estimat... | |
| logPoct/wat | 0.345 | Crippen Calculated Property | |
| McVol | 70.360 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | 4300.00 | kPa | KDB |
| Inp | [566.00; 625.00] |
|
|
| Inp | 597.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 568.00 | NIST | |
| Inp | 574.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 569.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 591.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 599.00 | NIST | |
| Inp | 566.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 625.00 | NIST | |
| Inp | 625.00 | NIST | |
| I | [937.00; 941.00] |
|
|
| I | 940.00 | NIST | |
| I | 941.00 | NIST | |
| I | 937.00 | NIST | |
| I | 938.00 | NIST | |
| I | 938.00 | NIST | |
| Tboil | [353.00; 354.10] | K |
|
| Tboil | 353.50 | K | KDB |
| Tboil | 353.70 | K | NIST |
| Tboil | 353.00 | K | NIST |
| Tboil | 354.10 ± 0.60 | K | NIST |
| Tboil | 353.00 ± 2.00 | K | NIST |
| Tc | 536.00 | K | KDB |
| Tfus | [196.70; 197.77] | K |
|
| Tfus | 196.70 | K | KDB |
| Tfus | 197.77 | K | Aq. Sol... |
| Tfus | 197.50 | K | NIST |
| Tfus | 197.50 ± 0.20 | K | NIST |
| Vc | 0.265 | m3/kmol | KDB |
| Zc | 0.2556890 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [116.32; 150.58] | J/mol×K | [363.89; 547.06] |
|
| Cp,gas | 116.32 | J/mol×K | 363.89 | Joback Calculated Property |
| Cp,gas | 122.50 | J/mol×K | 394.42 | Joback Calculated Property |
| Cp,gas | 128.49 | J/mol×K | 424.95 | Joback Calculated Property |
| Cp,gas | 134.29 | J/mol×K | 455.47 | Joback Calculated Property |
| Cp,gas | 139.91 | J/mol×K | 486.00 | Joback Calculated Property |
| Cp,gas | 145.34 | J/mol×K | 516.53 | Joback Calculated Property |
| Cp,gas | 150.58 | J/mol×K | 547.06 | Joback Calculated Property |
| Cp,liquid | [133.40; 172.30] | J/mol×K | [297.00; 298.15] |
|
| Cp,liquid | 133.40 | J/mol×K | 297.00 | NIST |
| Cp,liquid | 172.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 161.50 | J/mol×K | 298.15 | NIST |
| η | [0.0002583; 0.0021165] | Pa×s | [205.24; 363.89] |
|
| η | 0.0021165 | Pa×s | 205.24 | Joback Calculated Property |
| η | 0.0012203 | Pa×s | 231.68 | Joback Calculated Property |
| η | 0.0007877 | Pa×s | 258.12 | Joback Calculated Property |
| η | 0.0005515 | Pa×s | 284.56 | Joback Calculated Property |
| η | 0.0004102 | Pa×s | 311.01 | Joback Calculated Property |
| η | 0.0003197 | Pa×s | 337.45 | Joback Calculated Property |
| η | 0.0002583 | Pa×s | 363.89 | Joback Calculated Property |
| ΔfusH | [9.73; 9.73] | kJ/mol | [197.50; 197.50] |
|
| ΔfusH | 9.73 | kJ/mol | 197.50 | NIST |
| ΔfusH | 9.73 | kJ/mol | 197.50 | NIST |
| ΔfusH | 9.73 | kJ/mol | 197.50 | NIST |
| ΔvapH | [28.80; 38.00] | kJ/mol | [291.00; 335.00] |
|
| ΔvapH | 38.00 | kJ/mol | 291.00 | NIST |
| ΔvapH | 28.80 | kJ/mol | 318.00 | NIST |
| ΔvapH | 34.20 | kJ/mol | 335.00 | NIST |
| n0 | [1.39440; 1.40000] | [298.15; 313.15] |
|
|
| n0 | 1.40000 | 298.15 | Volumet... | |
| n0 | 1.39790 | 303.15 | Volumet... | |
| n0 | 1.39540 | 308.15 | Volumet... | |
| n0 | 1.39440 | 313.15 | Volumet... | |
| ρl | [898.59; 973.52] | kg/m3 | [278.15; 338.15] |
|
| ρl | 973.52 | kg/m3 | 278.15 | Thermop... |
| ρl | 970.51 | kg/m3 | 280.65 | Thermop... |
| ρl | 967.49 | kg/m3 | 283.15 | Thermop... |
| ρl | 964.46 | kg/m3 | 285.65 | Thermop... |
| ρl | 961.42 | kg/m3 | 288.15 | Thermop... |
| ρl | 958.37 | kg/m3 | 290.65 | Thermop... |
| ρl | 955.98 | kg/m3 | 293.00 | KDB |
| ρl | 955.31 | kg/m3 | 293.15 | Thermop... |
| ρl | 952.25 | kg/m3 | 295.65 | Thermop... |
| ρl | 949.17 | kg/m3 | 298.15 | Self-ag... |
| ρl | 947.56 | kg/m3 | 298.15 | Densiti... |
| ρl | 949.17 | kg/m3 | 298.15 | Thermop... |
| ρl | 946.10 | kg/m3 | 300.65 | Thermop... |
| ρl | 943.00 | kg/m3 | 303.15 | Thermop... |
| ρl | 939.91 | kg/m3 | 305.65 | Thermop... |
| ρl | 936.80 | kg/m3 | 308.15 | Thermop... |
| ρl | 933.68 | kg/m3 | 310.65 | Thermop... |
| ρl | 930.55 | kg/m3 | 313.15 | Thermop... |
| ρl | 927.41 | kg/m3 | 315.65 | Thermop... |
| ρl | 924.25 | kg/m3 | 318.15 | Thermop... |
| ρl | 921.09 | kg/m3 | 320.65 | Thermop... |
| ρl | 917.91 | kg/m3 | 323.15 | Thermop... |
| ρl | 914.73 | kg/m3 | 325.65 | Thermop... |
| ρl | 911.53 | kg/m3 | 328.15 | Thermop... |
| ρl | 908.31 | kg/m3 | 330.65 | Thermop... |
| ρl | 905.09 | kg/m3 | 333.15 | Thermop... |
| ρl | 901.85 | kg/m3 | 335.65 | Thermop... |
| ρl | 898.59 | kg/m3 | 338.15 | Thermop... |
| ΔfusS | 49.26 | J/mol×K | 197.50 | NIST |
| csound,fluid | [1095.70; 1226.60] | m/s | [288.15; 318.15] |
|
| csound,fluid | 1226.60 | m/s | 288.15 | Ultraso... |
| csound,fluid | 1204.60 | m/s | 293.15 | Ultraso... |
| csound,fluid | 1183.60 | m/s | 298.15 | Ultraso... |
| csound,fluid | 1162.20 | m/s | 303.15 | Ultraso... |
| csound,fluid | 1139.10 | m/s | 308.15 | Ultraso... |
| csound,fluid | 1117.80 | m/s | 313.15 | Ultraso... |
| csound,fluid | 1095.70 | m/s | 318.15 | Ultraso... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [259.45; 376.82] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.47471e+01 | |||
| Coefficient B | -3.18738e+03 | |||
| Coefficient C | -3.90130e+01 | |||
| Temperature range, min. | 259.45 | |||
| Temperature range, max. | 376.82 | |||
| Pvap | 1.33 | kPa | 259.45 | Calculated Property |
| Pvap | 2.99 | kPa | 272.49 | Calculated Property |
| Pvap | 6.16 | kPa | 285.53 | Calculated Property |
| Pvap | 11.79 | kPa | 298.57 | Calculated Property |
| Pvap | 21.21 | kPa | 311.61 | Calculated Property |
| Pvap | 36.18 | kPa | 324.66 | Calculated Property |
| Pvap | 58.89 | kPa | 337.70 | Calculated Property |
| Pvap | 92.03 | kPa | 350.74 | Calculated Property |
| Pvap | 138.75 | kPa | 363.78 | Calculated Property |
| Pvap | 202.67 | kPa | 376.82 | Calculated Property |
| Pvap | [4.11e-03; 4206.00] | kPa | [196.32; 536.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.86079e+01 | |||
| Coefficient B | -6.30414e+03 | |||
| Coefficient C | -7.99764e+00 | |||
| Coefficient D | 6.11250e-06 | |||
| Temperature range, min. | 196.32 | |||
| Temperature range, max. | 536.00 | |||
| Pvap | 4.11e-03 | kPa | 196.32 | Calculated Property |
| Pvap | 0.20 | kPa | 234.06 | Calculated Property |
| Pvap | 2.82 | kPa | 271.80 | Calculated Property |
| Pvap | 19.31 | kPa | 309.55 | Calculated Property |
| Pvap | 81.88 | kPa | 347.29 | Calculated Property |
| Pvap | 251.75 | kPa | 385.03 | Calculated Property |
| Pvap | 619.30 | kPa | 422.77 | Calculated Property |
| Pvap | 1300.58 | kPa | 460.52 | Calculated Property |
| Pvap | 2437.46 | kPa | 498.26 | Calculated Property |
| Pvap | 4206.00 | kPa | 536.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Propenoic acid, methyl ester.
Mixtures
- Benzene + 2-Propenoic acid, methyl ester
- Formamide, N,N-dimethyl- + 2-Propenoic acid, methyl ester
- 2-Propenoic acid, methyl ester + N,N-Dimethylacetamide
- 2-Propenoic acid, methyl ester + 1-Butanol
- 2-Propenoic acid, methyl ester + 1-Hexanol
- 2-Propenoic acid, methyl ester + 1-Octanol
- 2-Propenoic acid, methyl ester + 1-Decanol
- 2-Propenoic acid, methyl ester + Water
- Acetonitrile + 2-Propenoic acid, methyl ester
- 2-Propenoic acid, methyl ester + Tetrahydrofuran
- 2-Propenoic acid, methyl ester + Ethylene
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Volumetric, Viscometric, Ultrasonic, and Refractive Index Properties of Liquid Mixtures of Benzene with Industrially Important Monomers at Different Temperatures
- Measurement and prediction of phase equilibria of ethylene + methyl acrylate + poly(ethylene-co-methyl acrylate) systems
- Ultrasonic velocities, densities, and excess molar volumes of binary mixtures of N,N-dimethyl formamide with methyl acrylate, or ethyl acrylate, or butyl acrylate, or 2-ethyl hexyl acrylate at T = 308.15 K
- Densities and volumetric properties of binary mixtures of N,N-dimethylformamide/N,N-dimethylacetamide with some alkyl acrylates at temperatures from 288.15 K to 318.15 K
- Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
- Self-aggregation of liquids from biomass in aqueous solution
- Densities and volumetric properties of (acetonitrile + alkyl acrylate monomer) binary mixtures at temperatures from 293.15 K to 318.15 K
- Temperature and concentration dependence of volumetric properties of (tetrahydrofuran + methyl acrylate, or + ethyl acrylate, or + n-butyl acrylate, or + tert-butyl acrylate) binary mixtures
- Thermophysical Properties of Three Compounds from the Acrylate Family
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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.