GB600182A - Production of acetic acid and other lower fatty acids from their salts - Google Patents

Production of acetic acid and other lower fatty acids from their salts

Info

Publication number
GB600182A
GB600182A GB4061/42A GB406142A GB600182A GB 600182 A GB600182 A GB 600182A GB 4061/42 A GB4061/42 A GB 4061/42A GB 406142 A GB406142 A GB 406142A GB 600182 A GB600182 A GB 600182A
Authority
GB
United Kingdom
Prior art keywords
electrolyte
cathode
electrolysis
acid
anode
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
GB4061/42A
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.)
Individual
Original Assignee
Individual
Filing date
Publication date
Application filed by Individual filed Critical Individual
Publication of GB600182A publication Critical patent/GB600182A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B3/00Electrolytic production of organic compounds
    • C25B3/20Processes
    • C25B3/23Oxidation

Abstract

600,182. Electrolysis. GROOMBRIDGE, W. H., and HUNTER, W. March 27, 1942, No. 4061. [Class 41] A process for the production of a lower fatty acid of formula R.COOH, where R is an alkyl group containing up to three carbon atoms, from a metal salt thereof comprises electrolysing an aqueous solution of the salt of at least 5 per cent concentration to produce the acid as well as hydrogen and oxygen, the electrolysis being carried out at an elevated temperature not substantially exceeding 95‹ C. in a cell adapted to prevent admixture of the electrolyte surrounding the anode with that surrounding the cathode. The temperature is preferably between 80‹ and 95‹ C. The anode, preferably of nickel, may be immersed in electrolyte contained in a porous vessel, made, for example, of unglazed porcelain or earthenware, the vessel being immersed in an outer vessel containing the cathode electrolyte. A cover is provided to seal both vessels from each other and from the atmosphere. Suitable unions in the cover provide for the separate removal of hydrogen and oxygen. In the recovery of the acid and base from solutions of sodium acetate, electrolysis should preferably be carried out until for each initial two molecules of sodium acetate the anode electrolyte contains one molecule of titratable acetic acid. The cathode electrolyte can remain in the cell until it consists of a solution of caustic soda only. The removal of the electrolytes and their replacement can be carried out without interruption of the process. Acetic acid can be recovered from the withdrawn anode electrolyte by distillation or by means involving the crystallization and decomposition of acid sodium acetate. To prevent the cathode from being coated with the base in the electrolysis of solutions of salts of bases of low solubility, a porous screen may be interposed. between the cathode and electrolyte, and the space between filled, with an electrolyte free from the base.
GB4061/42A 1942-03-27 Production of acetic acid and other lower fatty acids from their salts Expired GB600182A (en)

Publications (1)

Publication Number Publication Date
GB600182A true GB600182A (en) 1948-04-02

Family

ID=1627899

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4061/42A Expired GB600182A (en) 1942-03-27 Production of acetic acid and other lower fatty acids from their salts

Country Status (1)

Country Link
GB (1) GB600182A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1047765B (en) * 1953-04-02 1958-12-31 Hooker Electrochemical Co Process and device for the production of saturated aliphatic carboxylic acids by electrolysis of aqueous solutions of their salts in multi-chambered cells
US4311799A (en) * 1978-01-26 1982-01-19 Asahi Kasei Kogyo Kabushiki Kaisha Novel basic cross-linked polymers
EP1659197A1 (en) * 2004-11-18 2006-05-24 Nederlandse Organisatie voor toegepast-natuurwetenschappelijk onderzoek TNO Process for the recovery of acids
CN104518242A (en) * 2013-10-01 2015-04-15 汽车能源供应公司 Method of manufacturing nonaqueous electrolyte secondary battery

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1047765B (en) * 1953-04-02 1958-12-31 Hooker Electrochemical Co Process and device for the production of saturated aliphatic carboxylic acids by electrolysis of aqueous solutions of their salts in multi-chambered cells
US4311799A (en) * 1978-01-26 1982-01-19 Asahi Kasei Kogyo Kabushiki Kaisha Novel basic cross-linked polymers
EP1659197A1 (en) * 2004-11-18 2006-05-24 Nederlandse Organisatie voor toegepast-natuurwetenschappelijk onderzoek TNO Process for the recovery of acids
WO2006054893A2 (en) * 2004-11-18 2006-05-26 Nederlandse Organisatie Voor Toegepast-Natuurwetenschappelijk Onderzoek Tno Process for the recovery of acids
WO2006054893A3 (en) * 2004-11-18 2006-07-06 Schappelijk Onderzoek Tno Nl O Process for the recovery of acids
CN104518242A (en) * 2013-10-01 2015-04-15 汽车能源供应公司 Method of manufacturing nonaqueous electrolyte secondary battery
CN104518242B (en) * 2013-10-01 2017-06-23 汽车能源供应公司 The manufacture method of rechargeable nonaqueous electrolytic battery

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