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 distillationInfo
- 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
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
-
- 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
- C07C51/487—Separation; 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.
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)
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 |
-
1952
- 1952-03-19 GB GB709552A patent/GB721301A/en not_active Expired
Cited By (7)
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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