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A continuous process for the production of epichlorohydrin

Assignee: Shell Internationale Research Maatschappij BV
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Filing: 1987-05-14
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Granted: —
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Expires: 2007-05-14
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Abstract

Abstract A process for the production of epichlorohydrin is disclosed which comprises reacting allyl chloride, chlorine and water to form an intermediate, then rapid conversion and separation of epichloro­hydrin product; the epichlorohydrin-depleted reaction mixture is cooled and subjected to electrodialysis then reverse osmosis to concentrate and remove deleterious by-products, and at least a substantial portion of the resultant permeate is recycled to the reaction zone, thereby enabling reduced operating costs and/or improved yield.

Inventors

  • 👤 George Constantin Blytas

Bibliographic Details

Application Number —
Jurisdiction EP
Data Source google_patents
Last Synchronized 2026-11-01 15:14
CPC Classifications
C; C07; C07D; C07D303/00; C07D303/02; C07D303/08; B; B01; B01D; B01D61/00; B01D61/58; C07D301/00; C07D301/02; C07D301/24; C07D301/26; B01D2311/00; B01D2311/04; B01D61/02; B01D61/025; B01D61/14; B01D61/145; B01D61/42; B01D61/44

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 217 words
A continuous process for the production of epichlorohydrin which comprises a) reacting allyl chloride, chlorine and water in a first reaction zone to produce an aqueous solution of dichlorohydrin, b) reacting said dichlorohydrin solution with an excess of a basic substance in a second reaction zone under conditions of temperature and contact time of the reactants whereby the dichloro­hydrin is substantially converted to epichlorohydrin, c) separating the formed epichlorohydrin rapidly and substantially completely from the aqueous reaction mixture as overhead by flash distillation, d) cooling said reaction mixture depleted in epichlorohydrin to a temperature below 70 °C, e) electrodialyzing said cooled reaction mixture in an electro­dialysis zone to afford: 1) an electrodialysis concentrate stream having an inorganic chloride content higher than said cooled reaction mixture feed to the electrodialysis zone, and 2) a diluate stream containing organic chloride compounds and having a lower inorganic chloride content than said reaction mixture feed, f) removing said concentrate stream of step (e), g) subjecting said diluate stream to reverse osmosis to form a retentate stream having a higher content of organic and inorganic chlorides than said diluate stream, and a permeate stream substantially depleted in both organic and inorganic chlorides, h) removing said retentate stream, and i) recycling at least part of said permeate stream to said first reaction zone.
Claim 2
Dependent Claim 217 words
A continuous process for the production of epichlorohydrin which comprises a) reacting allyl chloride, chlorine and water in a first reaction zone to produce an aqueous solution of dichlorohydrin, b) reacting said dichlorohydrin solution with an excess of a basic substance in a second reaction zone under conditions of temperature and contact time of the reactants whereby the dichloro­hydrin is substantially converted to epichlorohydrin, c) separating the formed epichlorohydrin rapidly and substantially completely from the aqueous reaction mixture as overhead by flash distillation, d) cooling said reaction mixture depleted in epichlorohydrin to a temperature below 70 °C, e) electrodialyzing said cooled reaction mixture in an electro­dialysis zone to afford: 1) an electrodialysis concentrate stream having an inorganic chloride content higher than said cooled reaction mixture feed to the electrodialysis zone, and 2) a diluate stream containing organic chloride compounds and having a lower inorganic chloride content than said reaction mixture feed, f) removing said concentrate stream of step (e), g) subjecting said diluate stream to reverse osmosis to form a retentate stream having a higher content of organic and inorganic chlorides than said diluate stream, and a permeate stream substantially depleted in both organic and inorganic chlorides, h) removing said retentate stream, and i) recycling at least part of said permeate stream to said first reaction zone.
Claim 3
Dependent Claim 48 words
A process as claimed in claim 1 wherein after step (d), said cooled reaction mixture is subjected to an ultrafiltration step to separate any insoluble material and afford a filtrate depleted in insoluble material, and said filtrate is passed as feed to the electrodialysis zone of step (e).
Claim 4
Dependent Claim 27 words
A process as claimed in claim 1 or 2 wherein said basic substance is a hydroxide or carbonate of an alkali metal or an alkaline earth metal.
Claim 5
Dependent Claim 17 words
A process as claimed in claim 3 wherein said basic substance is caustic soda, lime or limestone.
Claim 6
Dependent Claim 41 words
A process as claimed in claim 1 wherein in step (a) the first reaction zone comprises a plurality of reaction stages arranged in series flow, and said permeate stream from step (i) is recycled to the first of such reaction stages.
Claim 7
Dependent Claim 27 words
A process as claimed in claim 1 wherein in step (d) said reaction mixture is cooled to a temperature in the range from 35 to 60 °C.
Claim 8
Dependent Claim 24 words
A process as claimed in claim 1 or 5 wherein at least 50% of said permeate stream is recycled to said first reaction zone.
Claim 9
Dependent Claim 22 words
A process as claimed in claim 7 wherein at least 75% of said permeate stream is recycled to said first reaction zone.

References Cited (Backward Citations)

US2177419A Cited
US2714121A Cited
US2714123A Cited
US4496753A Cited

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