- InChI
- InChI=1S/C5H8O2/c1-3-5(6)7-4-2/h3H,1,4H2,2H3
- InChI Key
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N
- Formula
- C5H8O2
- SMILES
- C=CC(=O)OCC
- Molecular Weight1
- 100.12
- CAS
- 140-88-5
- Other Names
-
- Acrylate d'ethyle
- Acrylic acid ethyl ester
- Acrylic acid, ethyl ester (inhibited)
- Acrylsaeureaethylester
- Aethylacrylat
- Akrylanem etylu
- CH2=CHCOOC2H5
- Carboset 511
- Ethoxycarbonylethylene
- Ethyl 2-propenoate
- Ethyl acrylate, inhibited
- Ethyl ester of 2-propenoic acid
- Ethylacrylaat
- Ethylakrylat
- Ethylester kyseliny akrylove
- Etil acrilato
- Etilacrilatului
- NCI-C50384
- NSC 8263
- Rcra waste number U113
- acrylic acid, ethyl ester
- ethyl acrylate
- ethyl propenoate
- propenoic acid, ethyl ester
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (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°liquid : Liquid phase 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).
- 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.
- 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 | 0.4000 | KDB | |
| ΔcH°liquid | -2715.00 | kJ/mol | NIST |
| ΔfG° | -231.31 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-354.20; -327.80] | kJ/mol |
|
| ΔfH°gas | -331.40 | kJ/mol | NIST |
| ΔfH°gas | -354.20 | kJ/mol | NIST |
| ΔfH°gas | -327.80 | kJ/mol | NIST |
| ΔfH°liquid | [-393.40; -367.00] | kJ/mol |
|
| ΔfH°liquid | -370.60 | kJ/mol | NIST |
| ΔfH°liquid | -393.40 | kJ/mol | NIST |
| ΔfH°liquid | -367.00 | kJ/mol | NIST |
| ΔfusH° | 11.79 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [39.20; 39.20] | kJ/mol |
|
| ΔvapH° | 39.20 | kJ/mol | NIST |
| ΔvapH° | 39.20 | kJ/mol | NIST |
| IE | 10.30 | eV | NIST |
| log10WS | -0.74 | Aq. Solubility Prediction | |
| logPoct/wat | 0.735 | Crippen Calculated Property | |
| McVol | 84.450 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | 3740.00 | kPa | KDB |
| Inp | [644.00; 702.00] |
|
|
| Inp | 676.00 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 648.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 648.00 | NIST | |
| Inp | Outlier 702.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 644.00 | NIST | |
| Inp | 678.00 | NIST | |
| I | [980.00; 993.00] |
|
|
| I | 992.00 | NIST | |
| I | 993.00 | NIST | |
| I | 989.00 | NIST | |
| I | 980.00 | NIST | |
| I | 992.00 | NIST | |
| Tboil | [372.50; 373.00] | K |
|
| Tboil | 373.00 | K | KDB |
| Tboil | 373.00 | K | NIST |
| Tboil | 373.00 | K | NIST |
| Tboil | 372.75 | K | NIST |
| Tboil | 372.50 ± 3.00 | K | NIST |
| Tc | [552.00; 555.20] | K |
|
| Tc | 555.20 | K | DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development |
| Tc | 552.00 | K | KDB |
| Tfus | [201.00; 202.10] | K |
|
| Tfus | 201.00 | K | KDB |
| Tfus | 202.10 | K | Aq. Solubility Prediction |
| Tfus | 201.15 | K | NIST |
| Vc | 0.320 | m3/kmol | KDB |
| Zc | 0.2607630 | KDB |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [118.08; 256.88] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.07610e+01 | |||
| Coefficient B | 4.04020e-01 | |||
| Coefficient C | -1.76500e-04 | |||
| Coefficient D | 8.60000e-09 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 118.08 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 141.98 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 163.71 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 183.27 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 200.70 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 216.04 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 229.29 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 240.50 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 249.69 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 256.88 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0031180; 0.0002233] | Pa×s | [201.42; 387.52] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.12607e+01 | |||
| Coefficient B | 1.10580e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 201.42 | |||
| Temperature range, max. | 387.52 | |||
| η | 0.0031180 | Pa×s | 201.42 | Calculated Property |
| η | 0.0018702 | Pa×s | 222.09 | Calculated Property |
| η | 0.0012238 | Pa×s | 242.77 | Calculated Property |
| η | 0.0008560 | Pa×s | 263.45 | Calculated Property |
| η | 0.0006306 | Pa×s | 284.13 | Calculated Property |
| η | 0.0004843 | Pa×s | 304.81 | Calculated Property |
| η | 0.0003846 | Pa×s | 325.49 | Calculated Property |
| η | 0.0003140 | Pa×s | 346.16 | Calculated Property |
| η | 0.0002622 | Pa×s | 366.84 | Calculated Property |
| η | 0.0002233 | Pa×s | 387.52 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [274.70; 397.18] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46709e+01 | |||
| Coefficient B | -3.28201e+03 | |||
| Coefficient C | -4.65160e+01 | |||
| Temperature range, min. | 274.70 | |||
| Temperature range, max. | 397.18 | |||
| Pvap | 1.33 | kPa | 274.70 | Calculated Property |
| Pvap | 3.00 | kPa | 288.31 | Calculated Property |
| Pvap | 6.18 | kPa | 301.92 | Calculated Property |
| Pvap | 11.83 | kPa | 315.53 | Calculated Property |
| Pvap | 21.29 | kPa | 329.14 | Calculated Property |
| Pvap | 36.29 | kPa | 342.74 | Calculated Property |
| Pvap | 59.04 | kPa | 356.35 | Calculated Property |
| Pvap | 92.19 | kPa | 369.96 | Calculated Property |
| Pvap | 138.88 | kPa | 383.57 | Calculated Property |
| Pvap | 202.65 | kPa | 397.18 | Calculated Property |
| Pvap | [1.55e-03; 3733.07] | kPa | [201.95; 553.00] |
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 | 9.87203e+01 | |||
| Coefficient B | -7.84512e+03 | |||
| Coefficient C | -1.25776e+01 | |||
| Coefficient D | 1.02128e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 201.95 | |||
| Temperature range, max. | 553.00 | |||
| Pvap | 1.55e-03 | kPa | 201.95 | Calculated Property |
| Pvap | 0.11 | kPa | 240.96 | Calculated Property |
| Pvap | 1.87 | kPa | 279.96 | Calculated Property |
| Pvap | 14.20 | kPa | 318.97 | Calculated Property |
| Pvap | 63.53 | kPa | 357.97 | Calculated Property |
| Pvap | 201.30 | kPa | 396.98 | Calculated Property |
| Pvap | 505.65 | kPa | 435.98 | Calculated Property |
| Pvap | 1084.25 | kPa | 474.99 | Calculated Property |
| Pvap | 2086.75 | kPa | 513.99 | Calculated Property |
| Pvap | 3733.07 | kPa | 553.00 | Calculated Property |
| Pvap | [0.13; 101.36] | kPa | [243.70; 372.70] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44476e+01 | |||
| Coefficient B | -3.14547e+03 | |||
| Coefficient C | -5.26780e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 243.70 | |||
| Temperature range, max. | 372.70 | |||
| Pvap | 0.13 | kPa | 243.70 | Calculated Property |
| Pvap | 0.42 | kPa | 258.03 | Calculated Property |
| Pvap | 1.14 | kPa | 272.37 | Calculated Property |
| Pvap | 2.74 | kPa | 286.70 | Calculated Property |
| Pvap | 5.94 | kPa | 301.03 | Calculated Property |
| Pvap | 11.86 | kPa | 315.37 | Calculated Property |
| Pvap | 22.04 | kPa | 329.70 | Calculated Property |
| Pvap | 38.54 | kPa | 344.03 | Calculated Property |
| Pvap | 63.93 | kPa | 358.37 | Calculated Property |
| Pvap | 101.36 | kPa | 372.70 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Propenoic acid, ethyl ester.
Mixtures
- 2-Propenoic acid, ethyl ester + Formamide, N,N-dimethyl-
- 2-Propenoic acid, ethyl ester + N,N-Dimethylacetamide
- 2-Propenoic acid, ethyl ester + Tetrahydrofuran
- 2-Propenoic acid, ethyl ester + Acetonitrile
- 2-Propenoic acid, ethyl ester + Benzene
- 2-Propenoic acid, ethyl ester + 1-Butanol, 3-methyl-, acetate
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
- Volumetric, Viscometric, Ultrasonic, and Refractive Index Properties of Liquid Mixtures of Benzene with Industrially Important Monomers at Different Temperatures
- 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
- 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
- DIPPR Project 851 - Thirty Years of Vapor-Liquid Critical Point Measurements and Experimental Technique Development
- Thermophysical Properties of Three Compounds from the Acrylate Family
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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