GB718485A - Manufacture of ethyl toluenes and methyl styrenes - Google Patents
Manufacture of ethyl toluenes and methyl styrenesInfo
- Publication number
- GB718485A GB718485A GB30692/52A GB3069252A GB718485A GB 718485 A GB718485 A GB 718485A GB 30692/52 A GB30692/52 A GB 30692/52A GB 3069252 A GB3069252 A GB 3069252A GB 718485 A GB718485 A GB 718485A
- Authority
- GB
- United Kingdom
- Prior art keywords
- mixture
- fraction
- isomer
- per cent
- toluene
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C15/00—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts
- C07C15/40—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals
- C07C15/42—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals monocyclic
- C07C15/44—Cyclic hydrocarbons containing only six-membered aromatic rings as cyclic parts substituted by unsaturated carbon radicals monocyclic the hydrocarbon substituent containing a carbon-to-carbon double bond
- C07C15/46—Styrene; Ring-alkylated styrenes
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/54—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition of unsaturated hydrocarbons to saturated hydrocarbons or to hydrocarbons containing a six-membered aromatic ring with no unsaturation outside the aromatic ring
- C07C2/64—Addition to a carbon atom of a six-membered aromatic ring
- C07C2/66—Catalytic processes
- C07C2/68—Catalytic processes with halides
Abstract
Toluene is ethylated in the presence of a Friedel-Crafts' catalyst and the ethylation mixture fractionally distilled to obtain a fraction rich in toluene, a fraction rich in o-ethyltoluene, and a fraction rich in a mixture of m- and p-ethyltoluenes and containing not more than 0.5 per cent by weight of the o isomer. This last fraction may be dehydrogenated and a fraction consisting of m- and p-methylstyrenes and less than 0.5 per cent of o-isomer, indane, and indene recovered. This is polymerizable to colourless, thermoplastic resins. The ethylation is preferably effected with ethylene and activated aluminium chloride, e.g. at 90-101 DEG C., in the presence of the recycled o-ethyltoluene fraction and poly-ethyltoluenes whereby formation of the desired products is enhanced. Unreacted toluene is also recycled. The products are fractionated under reduced pressure, and a fraction containing o-, m- and p-ethyltoluenes separated and refractionated to recover a mixture of m- and p-isomers usually with less than 0.2 per cent of o-isomer. This mixture is dehydrogenated with or without gaseous diluents and catalysts, preferably in admixture with steam and with solid or fluidized catalysts at 550-700 DEG C. The product is fractionally distilled, preferably in a series of columns at reduced pressure, to recover a mixture of m-and p-methylstyrenes. U.S.A. Specification 2,531,327 is referred to.ALSO:Toluene is ethylated in the presence of a Friedel-Crafts' catalyst and the ethylation mixture fractionally distilled to obtain a fraction rich in toluene, a fraction rich in o-ethyltoluene, and a fraction rich in a mixture of m- and p-ethyltoluenes and containing not more than 0.5 per cent. by weight of the o isomer. This last fraction may be dehydrogenated and a fraction consisting of m- and p-methylstyrenes and less than 0.5 per cent. of o-isomer, indane, and indene recovered. The ethylation products are fractionated under reduced pressure, and a fraction containing om- and pethyltoluenes separated and refractionated to recover a mixture of m- and p-isomers usually with less than 0.2 per cent. of o-isomer. This mixture is dehydrogenated and the product fractionally distilled, preferably in a series of columns at reduced pressure, to recover a mixture of m- and p-methylstyrenes.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US718485XA | 1952-02-28 | 1952-02-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB718485A true GB718485A (en) | 1954-11-17 |
Family
ID=22103983
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB30692/52A Expired GB718485A (en) | 1952-02-28 | 1952-12-03 | Manufacture of ethyl toluenes and methyl styrenes |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB718485A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0062625A1 (en) * | 1981-04-02 | 1982-10-13 | Cosden Technology Inc. | Process for the production of vinyltoluene |
-
1952
- 1952-12-03 GB GB30692/52A patent/GB718485A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0062625A1 (en) * | 1981-04-02 | 1982-10-13 | Cosden Technology Inc. | Process for the production of vinyltoluene |
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