GB298137A - Improved process for concentrating acetic acid - Google Patents
Improved process for concentrating acetic acidInfo
- Publication number
- GB298137A GB298137A GB28386/28A GB2838628A GB298137A GB 298137 A GB298137 A GB 298137A GB 28386/28 A GB28386/28 A GB 28386/28A GB 2838628 A GB2838628 A GB 2838628A GB 298137 A GB298137 A GB 298137A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acetic acid
- butyl acetate
- per cent
- still
- water
- 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
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
298,137. Wacker Ges. f³r Elektrochemische Industrie Ges., Dr. A. Oct. 3, 1927, [Convention date]. Right to Patent relinquished. Acetic acid.-Dilute acetic acid is concentrated by distillation with an acetic ester of boiling point between 105-135‹ C., e.g. butyl acetate, iso-butyl acetate, iso-amyl acetate, &c. Thus, acetic acid of 40 per cent strength may be mixed with butyl acetate and heated in a still connected to a distillation column and dephlegmator until practically all the water has been removed in the form of an azeotropic mixture. The condensate obtained separates in an aqueous and an oily layer of which the latter containing the butyl acetate is run back into the still whilst the aqueous layer containing 0.2 per cent of acetic acid is drawn off. A residue in the still is finally obtained containing a small percentage of butyl acetate to which sufficient water in vapour or liquid form is added, to form an azeotropic mixture which is heated, the butyl acetate and the water distilling off leaving a residue of acetic acid of 95 per cent strength.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE298137X | 1927-10-03 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB298137A true GB298137A (en) | 1929-09-19 |
Family
ID=6090891
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB28386/28A Expired GB298137A (en) | 1927-10-03 | 1928-10-03 | Improved process for concentrating acetic acid |
Country Status (3)
Country | Link |
---|---|
CH (1) | CH139504A (en) |
FR (1) | FR661343A (en) |
GB (1) | GB298137A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5980696A (en) * | 1994-08-23 | 1999-11-09 | E. I. Du Pont De Nemours And Company | Dehydration of acetic acid by azeotropic distillation in the production of an aromatic acid |
US6150553A (en) * | 1998-08-11 | 2000-11-21 | E. I. Du Pont De Nemours And Company | Method for recovering methyl acetate and residual acetic acid in the production acid of pure terephthalic acid |
US9133094B2 (en) | 2011-04-18 | 2015-09-15 | Angus Chemical Company | Apparatus and process for nitration selectivity flexibility enabled by azeotropic distillation |
US9180384B2 (en) | 2010-12-10 | 2015-11-10 | Dow Global Technologies Llc | Apparatus and process for using olefin as an azeotropic entrainer for isolating 1,3-DICHLORO-2-propanol from a 2,2′-oxybis (1-chloropropane) waste stream |
US9192877B2 (en) | 2010-12-10 | 2015-11-24 | Angus Chemical Company | Apparatus and process for using a nitroalkane as an entrainer for azeotropic removal of water from aqueous acid solution |
-
1928
- 1928-09-25 CH CH139504D patent/CH139504A/en unknown
- 1928-10-01 FR FR661343D patent/FR661343A/en not_active Expired
- 1928-10-03 GB GB28386/28A patent/GB298137A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5980696A (en) * | 1994-08-23 | 1999-11-09 | E. I. Du Pont De Nemours And Company | Dehydration of acetic acid by azeotropic distillation in the production of an aromatic acid |
US6150553A (en) * | 1998-08-11 | 2000-11-21 | E. I. Du Pont De Nemours And Company | Method for recovering methyl acetate and residual acetic acid in the production acid of pure terephthalic acid |
US9180384B2 (en) | 2010-12-10 | 2015-11-10 | Dow Global Technologies Llc | Apparatus and process for using olefin as an azeotropic entrainer for isolating 1,3-DICHLORO-2-propanol from a 2,2′-oxybis (1-chloropropane) waste stream |
US9192877B2 (en) | 2010-12-10 | 2015-11-24 | Angus Chemical Company | Apparatus and process for using a nitroalkane as an entrainer for azeotropic removal of water from aqueous acid solution |
US9133094B2 (en) | 2011-04-18 | 2015-09-15 | Angus Chemical Company | Apparatus and process for nitration selectivity flexibility enabled by azeotropic distillation |
Also Published As
Publication number | Publication date |
---|---|
CH139504A (en) | 1930-04-30 |
FR661343A (en) | 1929-07-24 |
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