GB792860A - Process for making (chloromethyl) styrene - Google Patents

Process for making (chloromethyl) styrene

Info

Publication number
GB792860A
GB792860A GB12881/56A GB1288156A GB792860A GB 792860 A GB792860 A GB 792860A GB 12881/56 A GB12881/56 A GB 12881/56A GB 1288156 A GB1288156 A GB 1288156A GB 792860 A GB792860 A GB 792860A
Authority
GB
United Kingdom
Prior art keywords
per cent
chloroethyl
benzyl chloride
weight
vapours
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
Application number
GB12881/56A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Dow Chemical Co
Original Assignee
Dow Chemical Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Dow Chemical Co filed Critical Dow Chemical Co
Publication of GB792860A publication Critical patent/GB792860A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/25Preparation of halogenated hydrocarbons by splitting-off hydrogen halides from halogenated hydrocarbons

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

A (chloromethyl)styrene is prepared by dehydrochlorination of a (chloroethyl)benzyl chloride by heating vapours thereof at 420 DEG to 700 DEG C. at a pressure for the vapours not greater than 0.2 atmospheres and for a time such that not more than 10 per cent by weight of the (chloroethyl)benzyl chloride which is dehydrochlorinated undergoes pyrolysis to form by-products of lower boiling-points than that of the (chloromethyl)styrene. The (chloroethyl)benzyl chloride may be the ortho-, meta- or paraisomer or mixtures of these and the chlorine atom may occupy either the a - or b -position in the ethyl side-chain. An inert diluent such as carbon dioxide, nitrogen, helium, a saturated lower aliphatic hydrocarbon, vapours of a benzene hydrocarbon or steam can be used, advantageously at 500 DEG to 620 DEG C. for 0.01 to 10 seconds at total pressures between 0.01 and 1.5 atmospheres absolute pressure, the diluent being employed in such amount that the pressure of the (chloroethyl)benzyl chloride does not exceed 0.2 atmospheres. Advantageously, a mixture comprising one part by weight of a (chloroethyl)benzyl chloride and from one to 10 parts by weight of steam is used, the process being conducted in a conventional manner, preferably with the steam being superheated and supplying at least a portion of the heat, with final cooling of the vapours to condense liquid product which is then distilled. Polymerization inhibitors such as sulphur, dinitro-o-cresol, tert.-butyl catechol or hydroquinone may be added at any stage of the reaction or distillation or to the final products. In examples: (1) a mixture of about 70 per cent by weight p-(chloroethyl) benzyl chloride and 30 per cent of the o-isomer, containing 95 per cent of (alpha-chloroethyl) benzyl chlorides and 5 per cent of the beta-isomers is mixed with steam and dehydrohalogenated at 550 DEG to 600 DEG C. for 0.25 seconds, the vapours being condensed to a liquid product which is fractionally distilled to give 95 per cent pure (chloromethyl)styrene; (2) the process of (1) is repeated at 580 DEG to 610 DEG C. and 60 to 80 mm. absolute pressure for 0.4 seconds; (3) para(chloroethyl)benzyl chloride containing 95 per cent by weight of the alpha-isomer and 5 per cent of the beta-isomer is dehydrohalogenated in three separate experiments, the conditions being similar to those employed in (1) with minor variations in time and temperature; (4) a mixture similar to that used in (1) is dehydrohalogenated in the absence of steam, the reaction time being 0.7 second at 385 DEG to 500 DEG C. and 20 to 30 mm. pressure, to give a product containing 68 per cent by weight of (chloromethyl)styrene which is purified by distillation. Specification 792,859 is referred to.
GB12881/56A 1955-05-09 1956-04-26 Process for making (chloromethyl) styrene Expired GB792860A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US792860XA 1955-05-09 1955-05-09

Publications (1)

Publication Number Publication Date
GB792860A true GB792860A (en) 1958-04-02

Family

ID=22149576

Family Applications (1)

Application Number Title Priority Date Filing Date
GB12881/56A Expired GB792860A (en) 1955-05-09 1956-04-26 Process for making (chloromethyl) styrene

Country Status (1)

Country Link
GB (1) GB792860A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2981758A (en) * 1959-04-02 1961-04-25 American Cyanamid Co Preparation of halogenated alkylvinyl aromatic compounds
WO1988009319A1 (en) * 1987-05-26 1988-12-01 The Dow Chemical Company DEHYDROBROMINATION OF SUBSTITUTED alpha-HALOCUMENE
US4861927A (en) * 1987-05-26 1989-08-29 The Dow Chemical Company Dehydrohalogenation of ring-halogenated α-halocumenes

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2981758A (en) * 1959-04-02 1961-04-25 American Cyanamid Co Preparation of halogenated alkylvinyl aromatic compounds
WO1988009319A1 (en) * 1987-05-26 1988-12-01 The Dow Chemical Company DEHYDROBROMINATION OF SUBSTITUTED alpha-HALOCUMENE
US4861927A (en) * 1987-05-26 1989-08-29 The Dow Chemical Company Dehydrohalogenation of ring-halogenated α-halocumenes

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