- InChI
- InChI=1S/C7H12O2/c1-3-5-6-9-7(8)4-2/h4H,2-3,5-6H2,1H3
- InChI Key
- CQEYYJKEWSMYFG-UHFFFAOYSA-N
- Formula
- C7H12O2
- SMILES
- C=CC(=O)OCCCC
- Molecular Weight1
- 128.17
- CAS
- 141-32-2
- Other Names
-
- 2-PROPENOIC ACID BUTYL ESTER
- ACRYLIC ACID BUTYL ESTER
- Acrylic acid, n-butyl ester
- BUTYL-2-PROPENOATE
- Butyl 2-propenoate
- Butyl acrylate
- Butylacrylate, inhibited
- Butylester kyseliny akrylove
- UN 2348
- acrylic acid, butyl ester
- butyl propenoate
- n-Butyl acrylate
- n-Butyl propenoate
- propenoic acid, butyl ester
- 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).
- 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.
- ρc : Critical density (kg/m3).
- 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).
- Tboil : Normal Boiling Point Temperature (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 |
|---|---|---|---|
| ΔcH°liquid | -4046.96 ± 0.58 | kJ/mol | NIST |
| ΔfG° | -138.02 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-381.10; -375.30] | kJ/mol |
|
| ΔfH°gas | -375.30 ± 0.80 | kJ/mol | NIST |
| ΔfH°gas | -381.10 | kJ/mol | NIST |
| ΔfH°liquid | [-428.40; -422.60] | kJ/mol |
|
| ΔfH°liquid | -422.60 ± 0.70 | kJ/mol | NIST |
| ΔfH°liquid | -428.40 | kJ/mol | NIST |
| ΔfusH° | 15.39 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [47.30; 47.31] | kJ/mol |
|
| ΔvapH° | 47.31 ± 0.33 | kJ/mol | NIST |
| ΔvapH° | 47.30 | kJ/mol | NIST |
| ΔvapH° | 47.30 ± 0.30 | kJ/mol | NIST |
| log10WS | -1.47 | Crippen Calculated Property | |
| logPoct/wat | 1.516 | Crippen Calculated Property | |
| McVol | 112.630 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | [2840.00; 4540.00] | kPa |
|
| Pc | 2840.00 | kPa | Critica... |
| Pc | 4540.00 ± 350.00 | kPa | NIST |
| ρc | 299.79 ± 15.38 | kg/m3 | NIST |
| Inp | [850.00; 902.00] |
|
|
| Inp | 875.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | Outlier 850.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 892.00 | NIST | |
| I | [1169.00; 1197.00] |
|
|
| I | 1175.00 | NIST | |
| I | 1178.00 | NIST | |
| I | 1169.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1189.00 | NIST | |
| I | 1189.00 | NIST | |
| Tboil | [418.20; 421.95] | K |
|
| Tboil | 418.20 | K | NIST |
| Tboil | 420.20 | K | NIST |
| Tboil | 421.95 | K | NIST |
| Tc | 644.00 ± 3.00 | K | NIST |
| Tfus | [209.15; 209.50] | K |
|
| Tfus | 209.50 | K | NIST |
| Tfus | 209.50 ± 0.50 | K | NIST |
| Tfus | 209.15 | K | NIST |
| Vc | 0.432 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [222.85; 279.98] | J/mol×K | [432.53; 612.55] |
|
| Cp,gas | 222.85 | J/mol×K | 432.53 | Joback Calculated Property |
| Cp,gas | 233.32 | J/mol×K | 462.53 | Joback Calculated Property |
| Cp,gas | 243.41 | J/mol×K | 492.54 | Joback Calculated Property |
| Cp,gas | 253.12 | J/mol×K | 522.54 | Joback Calculated Property |
| Cp,gas | 262.44 | J/mol×K | 552.54 | Joback Calculated Property |
| Cp,gas | 271.40 | J/mol×K | 582.54 | Joback Calculated Property |
| Cp,gas | 279.98 | J/mol×K | 612.55 | Joback Calculated Property |
| Cp,liquid | 251.00 | J/mol×K | 298.15 | NIST |
| η | [0.0002641; 0.0028577] | Pa×s | [239.05; 432.53] |
|
| η | 0.0028577 | Pa×s | 239.05 | Joback Calculated Property |
| η | 0.0015177 | Pa×s | 271.30 | Joback Calculated Property |
| η | 0.0009221 | Pa×s | 303.54 | Joback Calculated Property |
| η | 0.0006165 | Pa×s | 335.79 | Joback Calculated Property |
| η | 0.0004423 | Pa×s | 368.04 | Joback Calculated Property |
| η | 0.0003347 | Pa×s | 400.28 | Joback Calculated Property |
| η | 0.0002641 | Pa×s | 432.53 | Joback Calculated Property |
| ΔfusH | [17.31; 17.31] | kJ/mol | [209.50; 209.50] |
|
| ΔfusH | 17.31 | kJ/mol | 209.50 | NIST |
| ΔfusH | 17.31 | kJ/mol | 209.50 | NIST |
| ΔfusH | 17.31 | kJ/mol | 209.50 | NIST |
| ΔvapH | [40.00; 45.70] | kJ/mol | [346.50; 368.50] |
|
| ΔvapH | 44.80 | kJ/mol | 346.50 | NIST |
| ΔvapH | 45.70 ± 0.30 | kJ/mol | 368.50 | NIST |
| ΔvapH | 42.80 ± 0.30 | kJ/mol | 368.50 | NIST |
| ΔvapH | 40.00 ± 0.30 | kJ/mol | 368.50 | NIST |
| n0 | [1.40690; 1.41190] | [298.15; 313.15] |
|
|
| n0 | 1.41190 | 298.15 | Volumet... | |
| n0 | 1.41020 | 303.15 | Volumet... | |
| n0 | 1.40840 | 308.15 | Volumet... | |
| n0 | 1.40690 | 313.15 | Volumet... | |
| ρl | [853.75; 913.92] | kg/m3 | [278.15; 338.15] |
|
| ρl | 913.92 | kg/m3 | 278.15 | Thermop... |
| ρl | 911.47 | kg/m3 | 280.65 | Thermop... |
| ρl | 908.99 | kg/m3 | 283.15 | Thermop... |
| ρl | 906.51 | kg/m3 | 285.65 | Thermop... |
| ρl | 903.60 | kg/m3 | 288.15 | Densiti... |
| ρl | 904.04 | kg/m3 | 288.15 | Thermop... |
| ρl | 901.56 | kg/m3 | 290.65 | Thermop... |
| ρl | 899.07 | kg/m3 | 293.15 | Thermop... |
| ρl | 898.85 | kg/m3 | 293.15 | Densiti... |
| ρl | 896.59 | kg/m3 | 295.65 | Thermop... |
| ρl | 893.96 | kg/m3 | 298.15 | Densiti... |
| ρl | 894.10 | kg/m3 | 298.15 | Densiti... |
| ρl | 894.10 | kg/m3 | 298.15 | Thermop... |
| ρl | 894.10 | kg/m3 | 298.15 | Densiti... |
| ρl | 893.95 | kg/m3 | 298.15 | Volumet... |
| ρl | 891.61 | kg/m3 | 300.65 | Thermop... |
| ρl | 889.35 | kg/m3 | 303.15 | Densiti... |
| ρl | 889.11 | kg/m3 | 303.15 | Thermop... |
| ρl | 886.61 | kg/m3 | 305.65 | Thermop... |
| ρl | 884.11 | kg/m3 | 308.15 | Thermop... |
| ρl | 884.60 | kg/m3 | 308.15 | Densiti... |
| ρl | 881.61 | kg/m3 | 310.65 | Thermop... |
| ρl | 879.85 | kg/m3 | 313.15 | Densiti... |
| ρl | 879.10 | kg/m3 | 313.15 | Thermop... |
| ρl | 876.58 | kg/m3 | 315.65 | Thermop... |
| ρl | 874.07 | kg/m3 | 318.15 | Thermop... |
| ρl | 875.10 | kg/m3 | 318.15 | Densiti... |
| ρl | 871.55 | kg/m3 | 320.65 | Thermop... |
| ρl | 869.02 | kg/m3 | 323.15 | Thermop... |
| ρl | 866.49 | kg/m3 | 325.65 | Thermop... |
| ρl | 863.95 | kg/m3 | 328.15 | Thermop... |
| ρl | 861.41 | kg/m3 | 330.65 | Thermop... |
| ρl | 858.86 | kg/m3 | 333.15 | Thermop... |
| ρl | 856.31 | kg/m3 | 335.65 | Thermop... |
| ρl | 853.75 | kg/m3 | 338.15 | Thermop... |
| ΔfusS | 82.61 | J/mol×K | 209.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [317.14; 442.18] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.57206e+01 | |||
| Coefficient B | -3.99833e+03 | |||
| Coefficient C | -5.80630e+01 | |||
| Temperature range, min. | 317.14 | |||
| Temperature range, max. | 442.18 | |||
| Pvap | 1.33 | kPa | 317.14 | Calculated Property |
| Pvap | 2.92 | kPa | 331.03 | Calculated Property |
| Pvap | 5.94 | kPa | 344.93 | Calculated Property |
| Pvap | 11.32 | kPa | 358.82 | Calculated Property |
| Pvap | 20.36 | kPa | 372.71 | Calculated Property |
| Pvap | 34.84 | kPa | 386.61 | Calculated Property |
| Pvap | 57.08 | kPa | 400.50 | Calculated Property |
| Pvap | 89.99 | kPa | 414.39 | Calculated Property |
| Pvap | 137.11 | kPa | 428.29 | Calculated Property |
| Pvap | 202.64 | kPa | 442.18 | Calculated Property |
| Pvap | [2.25e-04; 2641.37] | kPa | [208.55; 598.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.67290e+01 | |||
| Coefficient B | -7.34218e+03 | |||
| Coefficient C | -7.50837e+00 | |||
| Coefficient D | 4.00837e-06 | |||
| Temperature range, min. | 208.55 | |||
| Temperature range, max. | 598.00 | |||
| Pvap | 2.25e-04 | kPa | 208.55 | Calculated Property |
| Pvap | 0.03 | kPa | 251.82 | Calculated Property |
| Pvap | 0.60 | kPa | 295.09 | Calculated Property |
| Pvap | 5.81 | kPa | 338.37 | Calculated Property |
| Pvap | 31.22 | kPa | 381.64 | Calculated Property |
| Pvap | 113.70 | kPa | 424.91 | Calculated Property |
| Pvap | 316.53 | kPa | 468.18 | Calculated Property |
| Pvap | 728.07 | kPa | 511.46 | Calculated Property |
| Pvap | 1458.75 | kPa | 554.73 | Calculated Property |
| Pvap | 2641.37 | kPa | 598.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Propenoic acid, butyl ester.
Mixtures
- 1-Butanol, 3-methyl-, acetate + 2-Propenoic acid, butyl ester
- Benzene + 2-Propenoic acid, butyl ester
- Toluene + 2-Propenoic acid, butyl ester
- 2-Propenoic acid, butyl ester + o-Xylene
- Benzene, 1,3-dimethyl- + 2-Propenoic acid, butyl ester
- p-Xylene + 2-Propenoic acid, butyl ester
- 2-Propenoic acid, butyl ester + Mesitylene
- Methyl methacrylate + 2-Propenoic acid, butyl ester
- Toluene + Methyl methacrylate + 2-Propenoic acid, butyl ester
- Formamide, N,N-dimethyl- + 2-Propenoic acid, butyl ester
- N,N-Dimethylacetamide + 2-Propenoic acid, butyl ester
- Acetonitrile + 2-Propenoic acid, butyl ester
- 2-Propenoic acid, butyl ester + Tetrahydrofuran
Sources
- KDB Vapor Pressure Data
- Crippen Method
- 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
- Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
- Densities and volumes of mixing of the ternary system toluene + butyl acrylate + methyl methacrylate and its binaries at 298.15 K
- 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
- Critical Point and Vapor Pressure Measurements for 17 Compounds by a Low Residence Time Flow Method
- Thermophysical Properties of Three Compounds from the Acrylate Family
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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