GB831052A - A process for concentrating aqueous acrylic acid - Google Patents

A process for concentrating aqueous acrylic acid

Info

Publication number
GB831052A
GB831052A GB7028/57A GB702857A GB831052A GB 831052 A GB831052 A GB 831052A GB 7028/57 A GB7028/57 A GB 7028/57A GB 702857 A GB702857 A GB 702857A GB 831052 A GB831052 A GB 831052A
Authority
GB
United Kingdom
Prior art keywords
ketone
acrylic acid
water
solution
metal salt
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
GB7028/57A
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.)
Cavity GmbH
Original Assignee
Deutsche Solvay Werke GmbH
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 Deutsche Solvay Werke GmbH filed Critical Deutsche Solvay Werke GmbH
Publication of GB831052A publication Critical patent/GB831052A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C57/00Unsaturated compounds having carboxyl groups bound to acyclic carbon atoms
    • C07C57/02Unsaturated compounds having carboxyl groups bound to acyclic carbon atoms with only carbon-to-carbon double bonds as unsaturation
    • C07C57/03Monocarboxylic acids
    • C07C57/04Acrylic acid; Methacrylic acid
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/43Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
    • C07C51/44Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/48Separation; Purification; Stabilisation; Use of additives by liquid-liquid treatment
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C51/00Preparation of carboxylic acids or their salts, halides or anhydrides
    • C07C51/42Separation; Purification; Stabilisation; Use of additives
    • C07C51/50Use of additives, e.g. for stabilisation

Abstract

A process for concentrating aqueous acrylic acid comprises dissolving aqueous acrylic acid in a ketone which is at least partially miscible with water but immiscible with a concentrated aqueous solution of nickel, copper or cobalt salts and capable of forming together with water an azeotropic mixture boiling below 140 DEG C. at atmospheric pressure, shaking the solution with a pulverulent anhydrous nickel, cobalt or copper salt, the relative quantities of aqueous acrylic acid, ketone and metal salt used being such as to form a concentrated aqueous solution of the metal salt and disposed as a layer on the metal salt solution-a solution of acrylic acid in water and ketone, the relative quantities of water and ketone being such that the water content of the azeotropic mixture of water and ketone at atmospheric pressure is not exceeded, and then, after separation of the upper layer from the lower layer, distilling off the azeotrope of ketone and water and finally anhydrous acrylic acid from the upper layer. The aqueous acrylic acid is suitably one having a concentration of 35 to 40% and specified ketones are methyl ethyl (propyl or isopropyl) ketone, diethyl ketone, ethylisopropyl ketone and di-isopropyl ketone. Suitable salts are copper sulphate, cobalt chloride and preferably nickel chloride and/or nickel bromide and one or more of the metal salts may be used. The shaking of the solution with the metal salt or salts should preferably be effected at about 40 DEG C. and the subsequent azeotropic distillation and the acrylic acid distillation is preferably carried out in the presence of a polymerization inhibitor, e.g. hydroquinone. Examples are given in which methyl ethyl ketone is used as solvent and nickel chloride and nickel bromide respectively as the metal salt. Specification 781,805 is referred to.
GB7028/57A 1956-03-22 1957-03-04 A process for concentrating aqueous acrylic acid Expired GB831052A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE831052X 1956-03-22

Publications (1)

Publication Number Publication Date
GB831052A true GB831052A (en) 1960-03-23

Family

ID=6752130

Family Applications (1)

Application Number Title Priority Date Filing Date
GB7028/57A Expired GB831052A (en) 1956-03-22 1957-03-04 A process for concentrating aqueous acrylic acid

Country Status (1)

Country Link
GB (1) GB831052A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3337740A (en) * 1962-02-13 1967-08-22 Deering Milliken Res Corp Process for separating acrylic acid from impurities

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3337740A (en) * 1962-02-13 1967-08-22 Deering Milliken Res Corp Process for separating acrylic acid from impurities

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