GB727078A - Purifying acetic acid by azeotropic distillation - Google Patents
Purifying acetic acid by azeotropic distillationInfo
- Publication number
- GB727078A GB727078A GB29953/52A GB2995352A GB727078A GB 727078 A GB727078 A GB 727078A GB 29953/52 A GB29953/52 A GB 29953/52A GB 2995352 A GB2995352 A GB 2995352A GB 727078 A GB727078 A GB 727078A
- Authority
- GB
- United Kingdom
- Prior art keywords
- column
- acetic acid
- per cent
- line
- higher boiling
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
- C07C51/44—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation
- C07C51/46—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation by distillation by azeotropic distillation
Abstract
<PICT:0727078/III/1> Acetic acid is separated from formic acid in mixtures containing the two acids, water and higher boiling aliphatic acids, by subjecting the mixture to fractional distillation together with a paraffinic hydrocarbon liquid containing not more than 6 carbon atoms per molecule, whereby the formic acid and water distil over with the hydrocarbon and there is obtained as base product acetic acid containing the higher boiling acids but free from formic acid. Suitable hydrocarbons are pentane and hexane. A crude feed comprising acetic acid (64.6 per cent.), water (29.1 per cent.), formic acid (4.3 per cent) and higher boiling compounds (2 per cent.) including propionic, n-butyric and succinic acids, is introduced into column 1 through line 2 at the rate of 100 volumes per minute; while the column is heated by reboiler 3, and 98 volumes per minute of pentane are introduced into the column through line 4. The overhead product, taken off through line 5, is condensed; and the condensate is allowed to separate into two layers in decanter 6. The lower layer, which is an aqueous solution of formic acid, is withdrawn through line 7. The pentane layer is returned to column 1 through line 4. A mixture comprising acetic acid and the higher boiling compounds is withdrawn from reboiler 3, and passed through line 9 to column 11. A mixture comprising 83.3 per cent. of the higher boiling compounds and 16.7 per cent. of acetic acid is withdrawn from reboiler 12; while the distillate, which contains 99.5 per cent. of acetic acid, is passed to column 4. A final product containing 99.7 per cent. acetic acid is taken overhead from column 14, and is collected in receiver 15. The base product from column 14 contains 70 per cent. acetic acid, and is recycled through line 18 to column 11.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US727078XA | 1951-11-28 | 1951-11-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB727078A true GB727078A (en) | 1955-03-30 |
Family
ID=22109278
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB29953/52A Expired GB727078A (en) | 1951-11-28 | 1952-11-26 | Purifying acetic acid by azeotropic distillation |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB727078A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1227885B (en) * | 1961-11-25 | 1966-11-03 | Knapsack Ag | Process for the production of pure concentrated acetic acid from aqueous mixtures of paraffin oxidation |
US3383291A (en) * | 1965-06-09 | 1968-05-14 | Halcon International Inc | Recovery of trialkyl aluminum catalysts by plural distillation with hydrocarbon vapor stripping |
WO2001007390A1 (en) * | 1999-07-22 | 2001-02-01 | Consortium für elektrochemische Industrie GmbH | A method for the separation and purification of an aqueous mixture consisting of acetic acid and formic acid as the main components |
DE10065466A1 (en) * | 2000-12-28 | 2002-07-18 | Consortium Elektrochem Ind | Process for the separation of an aqueous mixture of the main components acetic acid and formic acid |
-
1952
- 1952-11-26 GB GB29953/52A patent/GB727078A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1227885B (en) * | 1961-11-25 | 1966-11-03 | Knapsack Ag | Process for the production of pure concentrated acetic acid from aqueous mixtures of paraffin oxidation |
US3383291A (en) * | 1965-06-09 | 1968-05-14 | Halcon International Inc | Recovery of trialkyl aluminum catalysts by plural distillation with hydrocarbon vapor stripping |
WO2001007390A1 (en) * | 1999-07-22 | 2001-02-01 | Consortium für elektrochemische Industrie GmbH | A method for the separation and purification of an aqueous mixture consisting of acetic acid and formic acid as the main components |
US6695952B1 (en) | 1999-07-22 | 2004-02-24 | Consortium Fur Elektrochemische Industrie Gmbh | Method for the separation of and purification of an aqueous mixture consisting of the main components acetic acid and formic acid |
DE10065466A1 (en) * | 2000-12-28 | 2002-07-18 | Consortium Elektrochem Ind | Process for the separation of an aqueous mixture of the main components acetic acid and formic acid |
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