[go: up one dir, main page]

GB356787A - Process for the production of concentrated aliphatic acids - Google Patents

Process for the production of concentrated aliphatic acids

Info

Publication number
GB356787A
GB356787A GB1463230A GB1463230A GB356787A GB 356787 A GB356787 A GB 356787A GB 1463230 A GB1463230 A GB 1463230A GB 1463230 A GB1463230 A GB 1463230A GB 356787 A GB356787 A GB 356787A
Authority
GB
United Kingdom
Prior art keywords
acid
column
entraining liquid
entraining
liquid
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
GB1463230A
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.)
Henry Dreyfuss Associates LLC
Original Assignee
Henry Dreyfuss Associates LLC
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 Henry Dreyfuss Associates LLC filed Critical Henry Dreyfuss Associates LLC
Priority to GB1463230A priority Critical patent/GB356787A/en
Publication of GB356787A publication Critical patent/GB356787A/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
    • C07C51/43Separation; 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
    • C07C51/46Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation by azeotropic distillation

Landscapes

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

Abstract

In the concentration of acetic, propionic, butyric, and other lower acids by distilling with an added liquid (termed an entraining liquid) which forms with water an azeotropic mixture boiling at a lower temperature than the acid, the aqueous acid and the entraining liquid are brought into the form of a homogeneous mixture prior to the distillation. The dilute acid and entraining liquid may be mixed with concentrated acid, for instance they may be each introduced into the heated concentrated acid in such proportions that the mixture does not separate into layers. The dilute acid and entraining liquid may be introduced continuously into a heated mixture of concentrated acid and entraining liquid in a still, which is preferably provided with a rectifying column, and the entraining liquid which separates from the condensate is returned to the still, concentrated acid being withdrawn from the still and treated in an auxiliary distillation p column to separate anhydrous acid. Or dilute acid, entraining liquid, and concentrated acid in proportions to form a homogeneous mixture, may be introduced into a distilling column, an azeotropic mixture of water and entraining liquid passing off at the top and concentrated acid being withdrawn at the bottom without needing an auxiliary column. If desired the dilute acid, entraining liquid and concentrated acid may be mixed in a separate vessel, the mixture being withdrawn continuously and fed to a distillation column for instance at a point one-third from the bottom, an auxiliary column being unnecessary. In all cases the column may be provided with a dephlegmator or other device for returning a part of the condensate to the column, and the heat of the vapour and of the concentrated acid may be utilized for instance to heat the dilute acid and the entraining liquid. Suitable entraining liquids are hydrocarbons such as benzene or xylene, halogenated hydrocarbons such as trichlorethylene and ethylene dichloride and esters such as ethyl, propyl, and butyl acetates or mixtures of such bodies.ALSO:In the concentration of acetic, propionic, butyric and other lower aliphatic acids by distilling with an added liquid (termed an entraining liquid) which forms with water an azeotropic mixture boiling at a lower temperature than the acid, the aqueous acid and the entraining liquid are brought into the form of a homogeneous mixture prior to the distillation. The dilute acid and entraining liquid may be mixed with concentrated acid, for instance they may be each introduced into the heated concentrated acid in such proportions that the mixture does not separate into layers. The dilute acid and entraining liquid may be introduced continuously into a heated mixture of concentrated acid and entraining liquid in a still, which is preferably provided with a rectifying column, and the entraining liquid which separates from the condensate is returned to the still, concentrated acid being withdrawn from the still and treated in an auxiliary distillation column to separate anhydrous acid. Or dilute acid, entraining liquid, and concentrated acid in proportions to form a homogenous mixture, may be introduced into a distilling column, an azeotropic mixture of water and entraining liquid passing off at the top and concentrated acid being withdrawn at the bottom without needing an auxiliary column. If desired the dilute acid, entraining liquid and concentrated acid may be mixed in a separate vessel, the mixture being withdrawn continuously and fed to a distillation column, for instance at a point one third from the bottom, an auxiliary column being unnecessary. In all cases the column may be provided with a dephlegmator or other device for returning a part of the condensate to the column, and the heat of the vapour and of the concentrated acid may be utilized for instance to heat the dilute acid and/or the entraining liquid. Suitable entraining liquids are hydrocarbons such as benzene or xylene, halogenated hydrocarbons such as trichlorethylene and ethylene dichloride and esters such as ethyl, propyl and butyl acetates or mixtures of such bodies.
GB1463230A 1930-05-13 1930-05-13 Process for the production of concentrated aliphatic acids Expired GB356787A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB1463230A GB356787A (en) 1930-05-13 1930-05-13 Process for the production of concentrated aliphatic acids

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1463230A GB356787A (en) 1930-05-13 1930-05-13 Process for the production of concentrated aliphatic acids

Publications (1)

Publication Number Publication Date
GB356787A true GB356787A (en) 1931-09-14

Family

ID=10044746

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1463230A Expired GB356787A (en) 1930-05-13 1930-05-13 Process for the production of concentrated aliphatic acids

Country Status (1)

Country Link
GB (1) GB356787A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4661208A (en) * 1984-11-02 1987-04-28 Shin-Etsu Vinyl Acetate Co., Ltd. Method for dehydrating distillation of an aqueous solution of carboxylic acid

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4661208A (en) * 1984-11-02 1987-04-28 Shin-Etsu Vinyl Acetate Co., Ltd. Method for dehydrating distillation of an aqueous solution of carboxylic acid

Similar Documents

Publication Publication Date Title
GB478326A (en) Improvements in the manufacture of ketene, acetic anhydride or a homologue thereof
GB356787A (en) Process for the production of concentrated aliphatic acids
GB478325A (en) Improvements in the manufacture of ketene, acetic anhydride or a homologue thereof
GB356741A (en) Improvements in or relating to the concentration of solutions of lower aliphatic acids
US2080194A (en) Apparatus and process for the continuous distillation-rectification of musts containing acetone, ethyl alcohol, and butyl-alcohol
GB628656A (en) Improvements in or relating to the hydrolysis of organic esters
US1931687A (en) Manufacture of aliphatic
GB467044A (en) Process of preparing nitriles
US1936172A (en) Treatment of organic compounds
GB645218A (en) Esterification using azeotropic distillation
US1897816A (en) Process for the dehydration of acetic acid
GB587704A (en) An improved process for the purification of organic liquids
AR111174A1 (en) METHOD FOR THE PRODUCTION OF ACETIC ACID
GB587269A (en) Improvements in or relating to the dehydration of acetic acid or mixtures of acetic acid and acetic anhydride
GB341730A (en) Improvements in the manufacture of organic esters and acids
GB423865A (en) Improvements in the manufacture of aliphatic anhydrides
US2249829A (en) Manufacture of nitric acid esters
GB407656A (en) Process for the working up of aqueous solutions of organic acids in particular of acetic acid
GB656740A (en) Improvements in the manufacture of crotonic anhydride
GB354159A (en) Manufacture of acetic anhydride
GB666785A (en) Process and apparatus for the hydrolytic decomposition of fatty oils and fats
GB348282A (en) Improvements in the separation of anhydrous organic acids from their aqueous solutions
GB633706A (en) Recovery of acetone, ethyl alcohol and butanol from their aqueous solution by distillation
US2192259A (en) Manufacture of aliphatic anhydrides
GB438399A (en) An improved process and apparatus for the separation of acetic anhydride from mixtures containing it