GB721301A - Improvements in or relating to the separation of acetic acid from aqueous mixtures of organic compounds by distillation - Google Patents

Improvements in or relating to the separation of acetic acid from aqueous mixtures of organic compounds by distillation

Info

Publication number
GB721301A
GB721301A GB709552A GB709552A GB721301A GB 721301 A GB721301 A GB 721301A GB 709552 A GB709552 A GB 709552A GB 709552 A GB709552 A GB 709552A GB 721301 A GB721301 A GB 721301A
Authority
GB
United Kingdom
Prior art keywords
formic acid
water
acetic acid
mixture
acetic
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
GB709552A
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.)
GORDON HINSLEY BYGRAVE
ROBERT LESTER COWLEY
Anglo Iranian Oil Co Ltd
Original Assignee
GORDON HINSLEY BYGRAVE
ROBERT LESTER COWLEY
Anglo Iranian Oil Co 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 GORDON HINSLEY BYGRAVE, ROBERT LESTER COWLEY, Anglo Iranian Oil Co Ltd filed Critical GORDON HINSLEY BYGRAVE
Priority to GB709552A priority Critical patent/GB721301A/en
Publication of GB721301A publication Critical patent/GB721301A/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
    • 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
    • C07C51/487Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification

Landscapes

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

Abstract

Acetic acid is separated from mixtures of lower fatty acids containing formic acid and water in addition to acetic acid, by adding acetic anhydride to the mixture in an amount in excess of that required to react with all the water present to form acetic acid, and simultaneously or thereafter submitting the mixture to fractional distillation whereby an acetic acid fraction, substantially free of formic acid, is obtained after formic acid has been distilled over. At the temperature at which the distillation is carried out formic acid decomposes at an appreciable rate into carbon monoxide and water; it is therefore desirable to use sufficient anhydride to react not only with the water originally present in the mixture but also with that produced by decomposition of formic acid. Feedstocks for the process may contain ketones and esters in addition to fatty acids and water. Thus a suitable feedstock is the crude product obtained by the partial aerial oxidation of lower hydrocarbons.ALSO:Acetic acid is separated from mixtures of lower fatty acids containing formic acid and water in addition to acetic acid, by adding acetic anhydride to the mixture in an amount in excess of that required to react with all the water present to form acetic acid, and simultaneously or thereafter submitting the mixture to fractional distillation whereby an acetic acid fraction, substantially free of formic acid, is obtained after formic acid has been distilled over. At the temperature at which the distillation is carried out formic acid decomposes at an appreciable rate into carbon monoxide and water; it is therefore desirable to use sufficient anhydride to react not only with the water originally present in the mixture but also with that produced by decomposition of formic acid. Feedstocks for the process may contain ketones and esters in addition to fatty acids and water. Thus a suitable feedstock is the crude product obtained by the partial aerial oxidation of lower hydrocarbons. An initial azeotropic distillation, using hexane or toluene as entrainer, will separate most of the formic acid, esters and water as an overhead fraction, leaving a bottoms fraction containing acetic and propionic acids, together with the remaining formic acid and water. This bottoms product is then treated with excess acetic anhydride as described above. In an example, a mixture containing acetic acid (86.8 per cent), formic acid (11.2 per cent) and water (2 per cent) was distilled in the presence of 14 per cent (based on the feed) of acetic anhydride using a column equivalent to 40 theoretical plates. Distillate was removed until the overhead temperature reached 113 DEG C., and this left a bottoms product of acetic acid containing only 0.15 per cent of formic acid.
GB709552A 1952-03-19 1952-03-19 Improvements in or relating to the separation of acetic acid from aqueous mixtures of organic compounds by distillation Expired GB721301A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB709552A GB721301A (en) 1952-03-19 1952-03-19 Improvements in or relating to the separation of acetic acid from aqueous mixtures of organic compounds by distillation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB709552A GB721301A (en) 1952-03-19 1952-03-19 Improvements in or relating to the separation of acetic acid from aqueous mixtures of organic compounds by distillation

Publications (1)

Publication Number Publication Date
GB721301A true GB721301A (en) 1955-01-05

Family

ID=9826524

Family Applications (1)

Application Number Title Priority Date Filing Date
GB709552A Expired GB721301A (en) 1952-03-19 1952-03-19 Improvements in or relating to the separation of acetic acid from aqueous mixtures of organic compounds by distillation

Country Status (1)

Country Link
GB (1) GB721301A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2893923A (en) * 1954-05-28 1959-07-07 Celanese Corp Purification of acetic acid by azeotropic distillation
WO2017083677A1 (en) * 2015-11-13 2017-05-18 Celanese International Corporation Processes for purifying acetic acid and hydrating anhydride

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2893923A (en) * 1954-05-28 1959-07-07 Celanese Corp Purification of acetic acid by azeotropic distillation
WO2017083677A1 (en) * 2015-11-13 2017-05-18 Celanese International Corporation Processes for purifying acetic acid and hydrating anhydride
US9908835B2 (en) * 2015-11-13 2018-03-06 Celanese International Corporation Processes for purifying acetic and hydrating anhydride
KR20180081708A (en) * 2015-11-13 2018-07-17 셀라니즈 인터내셔날 코포레이션 Process for purifying acetic acid and hydrating anhydride
US10160714B2 (en) 2015-11-13 2018-12-25 Celanese International Corporation Processes for purifying acetic acid and hydrating anhydride
US10689319B2 (en) 2015-11-13 2020-06-23 Celanese International Corporation Processes for purifying acetic acid and hydrating anhydride
US10899696B2 (en) 2015-11-13 2021-01-26 Celanese International Corporation Processes for purifying acetic acid and hydrating anhydride

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