GB468218A - Improved process for the preparation of acetic anhydride - Google Patents
Improved process for the preparation of acetic anhydrideInfo
- Publication number
- GB468218A GB468218A GB36033/35A GB3603335A GB468218A GB 468218 A GB468218 A GB 468218A GB 36033/35 A GB36033/35 A GB 36033/35A GB 3603335 A GB3603335 A GB 3603335A GB 468218 A GB468218 A GB 468218A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acetic acid
- column
- vapour
- anhydride
- cooled
- 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
- WFDIJRYMOXRFFG-UHFFFAOYSA-N Acetic anhydride Chemical compound CC(=O)OC(C)=O WFDIJRYMOXRFFG-UHFFFAOYSA-N 0.000 title abstract 12
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 abstract 30
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract 2
- CCGKOQOJPYTBIH-UHFFFAOYSA-N ethenone Chemical compound C=C=O CCGKOQOJPYTBIH-UHFFFAOYSA-N 0.000 abstract 2
- 229910000599 Cr alloy Inorganic materials 0.000 abstract 1
- PQLVXDKIJBQVDF-UHFFFAOYSA-N acetic acid;hydrate Chemical compound O.CC(O)=O PQLVXDKIJBQVDF-UHFFFAOYSA-N 0.000 abstract 1
- 229910021529 ammonia Inorganic materials 0.000 abstract 1
- 150000008064 anhydrides Chemical class 0.000 abstract 1
- 239000003054 catalyst Substances 0.000 abstract 1
- 239000000788 chromium alloy Substances 0.000 abstract 1
- 238000001816 cooling Methods 0.000 abstract 1
- 238000005194 fractionation Methods 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000000203 mixture Substances 0.000 abstract 1
- 230000004048 modification Effects 0.000 abstract 1
- 238000012986 modification Methods 0.000 abstract 1
- DQWPFSLDHJDLRL-UHFFFAOYSA-N triethyl phosphate Chemical compound CCOP(=O)(OCC)OCC DQWPFSLDHJDLRL-UHFFFAOYSA-N 0.000 abstract 1
- 239000002912 waste gas Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/54—Preparation of carboxylic acid anhydrides
- C07C51/56—Preparation of carboxylic acid anhydrides from organic acids, their salts, their esters or their halides, e.g. by carboxylation
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
<PICT:0468218/IV/1> <PICT:0468218/IV/2> Acetic anhydride is produced by heating acetic acid vapour in presence of an anhydrideforming catalyst, cooling the reaction vapours, to condense acetic acid water and acetic anhydride as described in the parent case, and then separating the acetic acid and reacting it with the ketene which remains uncondensed. The reaction vapours from an apparatus b, Fig. I, are cooled at c, the condensate passing to a fractionating column d, water containing some acetic acid being withdrawn at the top and condensed at g, while the ketene vapour passes from the cooler c to the bottom of a trickle tower e where it reacts with acetic acid from the column d forming anhydride, and the reaction heat in e vaporizes a part of the acetic acid, which passes to the column d by a pipe m and assists the fractionation in d; reduced pressure is maintained by a pump i. In a modification, Fig. II, the vapour liberated in e is cooled at l or by an external cooler, and waste gas escapes to the pump i; if for any reason there is too little acetic acid in e, more is added through m. In an example, acetic acid vapour containing 0,1 per cent of ammonia and 0,3 per cent of triethyl phosphate is passed through a chromium alloy tube at 780 DEG C., a pressure of 30--40 mm. being maintained by the pump i, using the apparatus shown in Fig. II. The vapours are cooled to 0 DEG C., and the condensate fed to the column d, 55 per cent acetic acid distils from the top of the column and a mixture of 75 parts acetic acid and 25 parts acetic anhydride flows to the tower e, which is also fed with additional acetic acid.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE468218X | 1935-01-16 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB468218A true GB468218A (en) | 1937-06-30 |
Family
ID=6540821
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB36033/35A Expired GB468218A (en) | 1935-01-16 | 1935-12-31 | Improved process for the preparation of acetic anhydride |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB468218A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2743296A (en) * | 1951-11-30 | 1956-04-24 | Eastman Kodak Co | Manufacture of lower aliphatic acid anhydrides |
| WO2006062558A1 (en) * | 2004-08-18 | 2006-06-15 | Celanese International Corporation | Acetate anhydride and acetate ester co-production |
-
1935
- 1935-12-31 GB GB36033/35A patent/GB468218A/en not_active Expired
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2743296A (en) * | 1951-11-30 | 1956-04-24 | Eastman Kodak Co | Manufacture of lower aliphatic acid anhydrides |
| WO2006062558A1 (en) * | 2004-08-18 | 2006-06-15 | Celanese International Corporation | Acetate anhydride and acetate ester co-production |
| CN101006041B (en) * | 2004-08-18 | 2011-01-05 | 塞拉尼斯国际公司 | Co-production of acetic anhydride and acetate |
| KR101143178B1 (en) * | 2004-08-18 | 2012-05-08 | 셀라니즈 인터내셔날 코포레이션 | Acetic anhydride and acetate ester co-production |
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