GB455325A - Improvements in or relating to the concentration of aliphatic acids - Google Patents

Improvements in or relating to the concentration of aliphatic acids

Info

Publication number
GB455325A
GB455325A GB27642/35A GB2764235A GB455325A GB 455325 A GB455325 A GB 455325A GB 27642/35 A GB27642/35 A GB 27642/35A GB 2764235 A GB2764235 A GB 2764235A GB 455325 A GB455325 A GB 455325A
Authority
GB
United Kingdom
Prior art keywords
tank
solvent
column
acid
still
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
GB27642/35A
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.)
Acordis UK Ltd
Original Assignee
British Celanese Ltd
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 British Celanese Ltd filed Critical British Celanese Ltd
Publication of GB455325A publication Critical patent/GB455325A/en
Expired legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Extraction Or Liquid Replacement (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

<PICT:0455325/IV/1> In extraction processes for concentrating aliphatic acids from cellulose esterification processes by means of solvents, sludge is removed from the apparatus by admitting the vapour of a solvent or partial solvent and draining away the condensed solvent. The extraction of acetic acid, for example, may be effected by passing the dilute acid through a column made of or lined with stainless steel, glass, bronze or the like in countercurrent with a solvent such as phenol ethers, ethylene chloride, or mixtures of petroleum ether, kerosene or benzol with ethyl ether, ethyl acetate, chloroform, or acetone oil; and the column may contain Raschig rings or other packing material. In the apparatus described aqueous acid from 1 is fed to columns 10, 11, 12, any of which may be cut out for cleaning. Each column has an upper part 13 in which the liquid phases separate, a packed part 14, and a bottom part 15 with sight glasses 16. The bottom sections of columns 10, 11 are connected by pipes 17, 18 to the acid-feed pipes at the top of columns 11, 12 respectively, and from the bottom section of column 12 is connected to a tank 22, still 23 and dephlegmator 24. Solvent from a tank 25 is supplied to the columns in counter-current to the aqueous acid and the extract is collected in a tank 30 from which it passes by a pipe 34 to a still head 35 from which it may be returned to the tank 25 or preferably is passed through a preheater 36 to a still 38 which has a fractionating column 43. Concentrated acid is led to a tank 40, and the vapour of the solvent is condensed at 68 and returned to the tank 25. When a column is to be cleaned, it is cut out of the circuit by the appropriate valves and the liquids are drained away into a tank 50. Concentrated acid or other solvent for the sludge is vaporized in a still 53 and admitted to the column by way of a pipe 54, the condensate and sludge being received in a tank 63 where much of the sludge separates out, the remainder being led to the tank 51 or to the still 53. The process may be applied to the extraction of formic, propionic, and butyric acids. The extraction process may be that described in Specification 454,891. The Specification as open to inspection under Sect. 91 is described generally for the concentration of aliphatic compounds and mentions aqueous acids obtained by distillation or fermentation of fruits or plants or other industrial processes, and aqueous solutions of aliphatic anhydrides. This subject-matter does not appear in the Specification as accepted.
GB27642/35A 1934-10-05 1935-10-07 Improvements in or relating to the concentration of aliphatic acids Expired GB455325A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US455325XA 1934-10-05 1934-10-05

Publications (1)

Publication Number Publication Date
GB455325A true GB455325A (en) 1936-10-19

Family

ID=21938444

Family Applications (1)

Application Number Title Priority Date Filing Date
GB27642/35A Expired GB455325A (en) 1934-10-05 1935-10-07 Improvements in or relating to the concentration of aliphatic acids

Country Status (1)

Country Link
GB (1) GB455325A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20140131275A1 (en) * 2012-11-15 2014-05-15 Bayer Intellectual Property Gmbh Process for phase separation or extraction and device suitable therefor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20140131275A1 (en) * 2012-11-15 2014-05-15 Bayer Intellectual Property Gmbh Process for phase separation or extraction and device suitable therefor

Similar Documents

Publication Publication Date Title
US1939116A (en) Process for the continuous production of esters of ethyl alcohol
GB467481A (en) Processes of removing water from aqueous aliphatic acids
GB455325A (en) Improvements in or relating to the concentration of aliphatic acids
US2235056A (en) Process for the recovery of glycerol from still residues from fermentation processes
GB454891A (en) Improvements in the concentration of aliphatic acids
US2018031A (en) Concentration of aliphatic acids
US2049441A (en) Process of operation for azeotropic distillation
US2063940A (en) Process for concentrating aqueous aliphatic acids recovered from cellulose esterification processes
GB407656A (en) Process for the working up of aqueous solutions of organic acids in particular of acetic acid
GB920834A (en) Process of purifying ª ,ª -unsaturated aliphatic aldehydes resulting from aldol condensation
US1982988A (en) Production of alcohol free from fusel oil
US2334400A (en) Purification of polyhydric alcohols
US2049440A (en) Process of removing water from aqueous aliphatic acids
US2114825A (en) Process for partial dehydration of acetic acid and other lower fatty acids
US1796059A (en) Process for recovering concentrated acetic acid from dilute acetic acid
GB803047A (en) A process for rectifying ethanol by distillation under elevated pressure
SU789551A1 (en) Method of colophony boiling
KR0139006B1 (en) Method for producing eicosapentaenoic acid and ester
GB246526A (en) Process of esterification
GB438399A (en) An improved process and apparatus for the separation of acetic anhydride from mixtures containing it
GB389145A (en) Improvements in or relating to the manufacture of acetaldehyde
US2180001A (en) Purification of hardwood oils
GB456921A (en) Improvements in or relating to the concentration of acetic acid
GB758095A (en) Improvements in or relating to the removal of volatile impurities from alcohol by extractive distillation
GB587704A (en) An improved process for the purification of organic liquids