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US 4,900,849 AGranted
Process for the production of dichlorohydrin
AssigneeShell Oil Company
InventorDavid I. Saletan
Life of this patent
Estimating the term…
Abstract
A process for the continuous production of di- and/or epichlorohydrin is disclosed wherein impurities, e.g., chloroaliphatic alkanes and chloroaliphatic ethers are removed by energy efficient solvent extraction and are obtained in relatively concentrated form for further processing or disposal.
Claims7
In a continuous process for the production of dichlorohydrin an improvement for reducing the level of chloroaliphatic alkanes and chloroaliphatic ethers impurities in the dichlorohydrin product the improvement comprising in sequence:
- (a) reacting allyl chloride, water and chlorine in a reaction zone to form an aqueous mixture of dichlorohydrin, together with minor amounts of chloroaliphatic ethers impurities;
- (b) contacting in an extraction zone said reaction zone effluent with less than about 8% by volume of a water-immiscible solvent for said impurities having a greater solvency for said impurities than for dichlorohydrin and an atmospheric boiling point from about 40.degree. to about 105.degree. C., to obtain as extract an impurity-enriched solvent, and an aqueous phase containing a major amount of the dichlorohydrin;
- (c) separating said extract from said aqueous phase;
- (d) contacting in a water wash zone said separated extract from step (c) with water to obtain a water wash stream containing a major portion of dichlorohydrin present in the feed to step (d), and a washed extract stream containing less dichlorohydrin than said feed to step (d);
- (e) recycling said water wash stream to at least one of step (a) and step (b);
- (f) passing said washed extract stream from step (d) as feed to a distillation zone, and fractionating said feed by fractional distillation to obtain an overhead stream containing impurities boiling at a temperature lower than the boiling temperature of said solvent, a residual fraction containing impurities boiling at a temperature higher than the boiling temperature of said solvent, and an intermediate steam comprising regenerated solvent containing fewer impurities than said feed;
- and
- (g) recycling said regenerated solvent to the extraction zone of step (b).
5 more elements
Dependencies are inferred from the claim text.