Names | |
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Preferred IUPAC name
Ethenyl acetate
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Systematic IUPAC name
Ethenyl ethanoate
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Other names
Acetic acid vinyl ester, vinyl ethanoate, acetoxyethene, VyAc, VAM, zeset T, VAM vinyl acetate monomer, acetic acid ethenyl ester, 1-acetoxyethylene
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Identifiers | |
3D model (Jmol)
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ChEBI | |
ChemSpider | |
ECHA InfoCard | 100.003.224 |
EC Number | 203-545-4 |
KEGG | |
MeSH | C011566 |
PubChem CID
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UNII | |
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Properties | |
C4H6O2 | |
Molar mass | 86.09 g/mol |
Appearance | Colorless liquid |
Density | 0.934 g/cm3 |
Melting point | −93.5 °C (−136.3 °F; 179.7 K) |
Boiling point | 72.7 °C (162.9 °F; 345.8 K) |
-46.4·10−6 cm3/mol | |
Hazards | |
Safety data sheet | ICSC 0347 |
R-phrases | R11 |
S-phrases | S16, S23, S29, S33 |
NFPA 704 | |
Flash point | −8 °C (18 °F; 265 K) |
427 °C (801 °F; 700 K) | |
Explosive limits | 2.6–13.40% |
US health exposure limits (NIOSH): | |
PEL (Permissible)
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none |
Except where otherwise noted, data are given for materials in their standard state (at 25 °C [77 °F], 100 kPa).
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what is ?) | (|
Infobox references | |
Vinyl acetate is an organic compound with the formula CH3CO2CHCH2. A colorless liquid with a pungent odor, it is the precursor to polyvinyl acetate, an important polymer in industry. Unlike many other acetate esters, the odor of vinyl acetate is thoroughly disagreeable and is not used to any substantial degree as an odorant.
The worldwide production capacity of vinyl acetate monomer (VAM) was estimated at 6,154,000 tonnes/annum in 2007, with most capacity concentrated in the United States (1,585,000 all in Texas), China (1,261,000), Japan (725,000) and Taiwan (650,000). The average list price for 2008 was $1600/tonne. Celanese is the largest producer (ca 25% of the worldwide capacity), while other significant producers include China Petrochemical Corporation (7%), Chang Chun Group (6%) and LyondellBasell (5%).
It is a key ingredient in furniture glue.
The major industrial route involves the reaction of ethylene and acetic acid with oxygen in the presence of a palladium catalyst.
The main side reaction is the combustion of organic precursors. Vinyl acetate was once prepared by hydroesterification. This method involves the gas-phase addition of acetic acid to acetylene in the presence of metal catalysts. By this route, using mercury(II) catalysts, vinyl acetate was first prepared by Klatte in 1912. Another route to vinyl acetate involves thermal decomposition of ethylidene diacetate:
It can be polymerized to give polyvinyl acetate (PVA). With other monomers can be used to prepare copolymers such as ethylene-vinyl acetate (EVA), vinyl acetate-acrylic acid (VA/AA), polyvinyl chloride acetate (PVCA), and polyvinylpyrrolidone (Vp/Va Copolymer, used in hair gels). Due to the instability of the radical, attempts to control the polymerization via most 'living/controlled' radical processes have proved problematic. However, RAFT (or more specifically MADIX) polymerization offers a convenient method of controlling the synthesis of PVA by the addition of a xanthate or a dithiocarbamate chain transfer agent.