- InChI
- InChI=1S/C4H6O2/c1-3-6-4(2)5/h3H,1H2,2H3
- InChI Key
- XTXRWKRVRITETP-UHFFFAOYSA-N
- Formula
- C4H6O2
- SMILES
- C=COC(C)=O
- Molecular Weight1
- 86.09
- CAS
- 108-05-4
- Other Names
-
- 1-ACETOXYETHYLENE
- Acetate de vinyle
- Acetic acid vinyl ester
- Acetic acid, ethylene ether
- Acetoxyethene
- CH3CO2CH=CH2
- ETHENYL ETHANOATE
- Ethanoic acid, ethenyl ester
- Ethenyl acetate
- Everflex 81L
- NSC 8404
- Octan winylu
- Plyamul 40305-00
- Unocal 76 Res 6206
- Unocal 76 Res S-55
- VAC
- VINYL ETHANOATE
- Vinile (acetato di)
- Vinnapas A 50
- Vinyl A monomer
- Vinyl acetate
- Vinyl acetate h.q.
- Vinyl acetate monomer
- Vinyl ester of acetic acid
- Vinylacetaat
- Vinylacetat
- Vinyle (acetate de)
- Vinylester kyseliny octove
- VyAc
- Zeset T
- acetic acid, vinyl ester
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- 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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- 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.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3400 | KDB | |
| PAff | 813.90 | kJ/mol | NIST |
| Tig | 699.82 | K | KDB |
| BasG | 782.90 | kJ/mol | NIST |
| ΔcH°liquid | -2086.00 ± 10.00 | kJ/mol | NIST |
| μ | 1.70 | debye | KDB |
| LFL | 2.60 | % in Air | KDB |
| UFL | 13.40 | % in Air | KDB |
| Tflash,cc | 268.15 | K | KDB |
| Tflash,oc | 265.37 | K | KDB |
| ΔfG° | -163.28 | kJ/mol | Joback Calculated Property |
| Rg | 3.0890 | KDB | |
| ΔfH°gas | [-316.00; -309.00] | kJ/mol |
|
| ΔfH°gas | -316.00 | kJ/mol | KDB |
| ΔfH°gas | -313.60 | kJ/mol | NIST |
| ΔfH°gas | -309.00 ± 10.00 | kJ/mol | NIST |
| ΔfH°liquid | [-350.80; -346.00] | kJ/mol |
|
| ΔfH°liquid | -350.80 | kJ/mol | NIST |
| ΔfH°liquid | -346.00 ± 10.00 | kJ/mol | NIST |
| ΔfusH° | 7.62 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 37.20 ± 0.84 | kJ/mol | NIST |
| IE | [9.19; 9.85] | eV |
|
| IE | 9.20 | eV | NIST |
| IE | 9.20 | eV | NIST |
| IE | 9.19 ± 0.05 | eV | NIST |
| IE | 9.85 | eV | NIST |
| IE | 9.85 ± 0.05 | eV | NIST |
| log10WS | -0.71 | Crippen Calculated Property | |
| logPoct/wat | 0.693 | Crippen Calculated Property | |
| McVol | 70.360 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | [4185.00; 4350.00] | kPa |
|
| Pc | 4350.00 | kPa | KDB |
| Pc | 4185.00 ± 9.00 | kPa | NIST |
| Inp | [524.00; 570.00] |
|
|
| Inp | 564.00 | NIST | |
| Inp | 527.00 | NIST | |
| Inp | 529.00 | NIST | |
| Inp | 545.00 | NIST | |
| Inp | 548.00 | NIST | |
| Inp | 524.00 | NIST | |
| Inp | 546.00 | NIST | |
| Inp | 551.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 570.00 | NIST | |
| Inp | 560.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 562.00 | NIST | |
| Inp | 548.00 | NIST | |
| Inp | 564.00 | NIST | |
| I | 878.00 | NIST | |
| Tboil | [345.75; 346.10] | K |
|
| Tboil | 346.00 | K | KDB |
| Tboil | 346.10 | K | Vapor-L... |
| Tboil | 345.75 | K | Vapor L... |
| Tboil | 345.95 | K | Isobari... |
| Tc | [519.13; 525.00] | K |
|
| Tc | 525.00 | K | KDB |
| Tc | 519.13 ± 0.40 | K | NIST |
| Tfus | [172.95; 180.35] | K |
|
| Tfus | 173.00 | K | KDB |
| Tfus | 180.35 | K | NIST |
| Tfus | 172.95 ± 0.30 | K | NIST |
| Vc | 0.265 | m3/kmol | KDB |
| Zc | 0.2640820 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [116.32; 150.58] | J/mol×K | [363.89; 547.06] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 115 120 125 130 135 140 145 150 400 450 500 550 | ||||
| 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 | 169.50 | J/mol×K | 298.00 | NIST |
| η | [0.0002583; 0.0021165] | Pa×s | [205.24; 363.89] |
|
|
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 250 300 350 | ||||
| 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 | [8.46; 8.46] | kJ/mol | [180.60; 180.60] |
|
| ΔfusH | 8.46 | kJ/mol | 180.60 | NIST |
| ΔfusH | 8.46 | kJ/mol | 180.60 | NIST |
| ΔvapH | [31.40; 34.40] | kJ/mol | [320.00; 347.50] |
|
| ΔvapH | 34.40 | kJ/mol | 320.00 | NIST |
| ΔvapH | 31.40 | kJ/mol | 347.50 | NIST |
| Pvap | [97.30; 101.30] | kPa | [344.68; 346.10] |
|
| Pvap | 97.30 | kPa | 344.68 | Vapor-L... |
| Pvap | 101.30 | kPa | 345.75 | Vapor L... |
| Pvap | 101.30 | kPa | 346.10 | Vapor-L... |
| n0 | [1.39253; 1.39260] | [293.15; 298.15] |
|
|
| n0 | 1.39260 | 293.15 | Measure... | |
| n0 | 1.39253 | 298.15 | Density... | |
| ρl | [906.12; 932.00] | kg/m3 | [293.00; 313.15] |
|
|
T(K) Liquid Density (kg/m3) 905 910 915 920 925 930 295 300 305 310 | ||||
| ρl | 932.00 | kg/m3 | 293.00 | KDB |
| ρl | 931.95 | kg/m3 | 293.15 | Density... |
| ρl | 925.77 | kg/m3 | 298.15 | Densiti... |
| ρl | 925.77 | kg/m3 | 298.15 | Densiti... |
| ρl | 919.09 | kg/m3 | 303.15 | Density... |
| ρl | 919.40 | kg/m3 | 303.15 | Density... |
| ρl | 913.13 | kg/m3 | 308.15 | Densiti... |
| ρl | 913.50 | kg/m3 | 308.15 | Density... |
| ρl | 913.13 | kg/m3 | 308.15 | Densiti... |
| ρl | 906.12 | kg/m3 | 313.15 | Density... |
| ρl | 907.30 | kg/m3 | 313.15 | Density... |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 3968.13] | kPa | [253.08; 519.13] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48909e+01 | |||
| Coefficient B | -3.20824e+03 | |||
| Coefficient C | -3.33880e+01 | |||
| Temperature range, min. | 253.08 | |||
| Temperature range, max. | 519.13 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 | ||||
| Pvap | 1.33 | kPa | 253.08 | Calculated Property |
| Pvap | 7.53 | kPa | 282.64 | Calculated Property |
| Pvap | 29.49 | kPa | 312.20 | Calculated Property |
| Pvap | 88.87 | kPa | 341.76 | Calculated Property |
| Pvap | 220.80 | kPa | 371.32 | Calculated Property |
| Pvap | 473.86 | kPa | 400.89 | Calculated Property |
| Pvap | 907.65 | kPa | 430.45 | Calculated Property |
| Pvap | 1588.80 | kPa | 460.01 | Calculated Property |
| Pvap | 2586.47 | kPa | 489.57 | Calculated Property |
| Pvap | 3968.13 | kPa | 519.13 | Calculated Property |
| Pvap | [9.50e-04; 4192.26] | kPa | [180.35; 524.00] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.86249e+01 | |||
| Coefficient B | -5.47773e+03 | |||
| Coefficient C | -4.86787e+00 | |||
| Coefficient D | 2.36709e-06 | |||
| Temperature range, min. | 180.35 | |||
| Temperature range, max. | 524.00 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 300 400 500 | ||||
| Pvap | 9.50e-04 | kPa | 180.35 | Calculated Property |
| Pvap | 0.08 | kPa | 218.53 | Calculated Property |
| Pvap | 1.55 | kPa | 256.72 | Calculated Property |
| Pvap | 13.12 | kPa | 294.90 | Calculated Property |
| Pvap | 64.55 | kPa | 333.08 | Calculated Property |
| Pvap | 220.12 | kPa | 371.27 | Calculated Property |
| Pvap | 580.62 | kPa | 409.45 | Calculated Property |
| Pvap | 1272.48 | kPa | 447.63 | Calculated Property |
| Pvap | 2431.86 | kPa | 485.82 | Calculated Property |
| Pvap | 4192.26 | kPa | 524.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Acetic acid ethenyl ester.
Mixtures
- Acetic acid ethenyl ester + Propane, 2-methoxy-2-methyl-
- Carbonic acid, dimethyl ester + Acetic acid ethenyl ester
- Acetic acid ethenyl ester + Butane, 1-(ethenyloxy)-
- Diisopropyl ether + Acetic acid ethenyl ester
- Acetic acid ethenyl ester + Anisole
- Acetic acid ethenyl ester + n-Butyl ether
- Acetic acid ethenyl ester + Cyclohexane
- Benzyl alcohol + Acetic acid ethenyl ester
- 2-Propanol, 1,3-dichloro- + Acetic acid ethenyl ester
- Acetic acid ethenyl ester + Acetic acid + Water
- Ethanol + Acetic acid ethenyl ester + Water
- Diethyl carbonate + Acetic acid ethenyl ester
- Acetic acid ethenyl ester + Propanoic acid, ethenyl ester
- p-Xylene + Acetic acid ethenyl ester
- Acetic acid ethenyl ester + Methyl Alcohol
- Acetic acid ethenyl ester + 1-Butanol
- Acetonitrile + Acetic acid ethenyl ester + Quercetin
- Benzene, (1-methylethyl)- + Acetic acid ethenyl ester
- Carbon dioxide + Acetic acid ethenyl ester
- Benzenemethanol, «alpha»-methyl- + Carbon dioxide + Acetic acid ethenyl ester
Find more mixtures with Acetic acid ethenyl ester.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Phase equilibria of the ternary system vinyl acetate/(R,S)-1-phenylethanol/carbon dioxide at high pressure conditions
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Densities and derived thermodynamic properties of the binary systems of 1,1-dimethylethyl methyl ether with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at T = (298.15 and 308.15) K
- Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Density, viscosity, and speed of sound of binary liquid mixtures of vinyl acetate with butyl vinyl ether, diisopropyl ether, anisole and dibutyl ether
- Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
- The study of excess molar volumes and related properties for binary mixtures containing benzyl alcohol and 1,3-dichloro-2-propanol with vinyl acetate, ethyl acetate and t-butyl acetate at T = 293.15 to 313.15 K and P = 0.087 MPa
- Measurement and Modeling of Liquid Liquid Equilibrium for the Systems Vinyl Acetate + Acetic Acid/Ethanol + Water at 298.15 and 308.15 K
- Bubble-Point Measurement for CO2 + Vinyl Acetate and CO2 + Vinyl Acrylate Systems at High Pressures.
- Vapor-Liquid Equilibrium and Mixing Properties of Methanol + Diethyl Carbonate and Vinyl Acetate + Diethyl Carbonate Systems
- Density, Refractive Index, Speed of Sound, and Vapor-Liquid Equilibria for Binary Mixtures of Methanol + Vinyl Propionate and Vinyl Acetate + Vinyl Propionate. Vapor Pressures of Vinyl Propionate
- Vapor-Liquid Equilibria and Excess Properties of the Binary System Vinyl Acetate + p-Xylene
- Vapor Liquid Equilibrium at p/kPa = 101.3 of the Binary Mixtures of Ethenyl Acetate with Methanol and Butan-1-ol
- Solubility of Flavonoids in Organic Solvents
- Isobaric Vapor Liquid Equilibrium of Binary Mixtures of Vinyl Acetate and Ethyl Formate with Cumene at 97.3 kPa
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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