GB687902A - Improvements in or relating to processes for the hydrolysis of methyl acetate and the treatment of aqueous mixtures of methyl acetate, methyl alcohol and acetic acid so obtained - Google Patents
Improvements in or relating to processes for the hydrolysis of methyl acetate and the treatment of aqueous mixtures of methyl acetate, methyl alcohol and acetic acid so obtainedInfo
- Publication number
- GB687902A GB687902A GB9792/51A GB979251A GB687902A GB 687902 A GB687902 A GB 687902A GB 9792/51 A GB9792/51 A GB 9792/51A GB 979251 A GB979251 A GB 979251A GB 687902 A GB687902 A GB 687902A
- Authority
- GB
- United Kingdom
- Prior art keywords
- methyl acetate
- water
- hydrolysis
- acetic acid
- atm
- 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
- C07C51/09—Preparation of carboxylic acids or their salts, halides or anhydrides from carboxylic acid esters or lactones
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
Methyl acetate is hydrolysed with water in the presence of a hydrolysation catalyst at a pressure above atmospheric and an elevated temperature below the boiling-point of the mixture at said pressure. The catalyst may be a strong acid, e.g. sulphuric acid equivalent to 0.05-2, preferably about 1 per cent by weight of the reactants. Temperature may be 48-140 DEG C. and pressure up to 10 atm., e.g. 100 DEG C. at 3 atm., or 115 DEG C. at 6 atm. The ratio of water to ester is preferably such that only 20-70 per cent is hydrolysed, viz. 0.3-2 : 1. The hydrolysis mixture is preferably subjected to the reaction conditions for 10-45 minutes. The mixture of acetic acid, methanol, methyl acetate and water obtained by said hydrolysis is distilled, the overhead of methanol and methyl acetate being in part returned as reflux, and in part scrubbed with water to give aqueous methanol and the ester. The bottoms of aqueous acetic acid is extracted with methyl acetate which may contain 10-25 per cent of cyclohexane, the extract then being distilled to drive off solvent and water and recover anhydrous acid. The methyl acetate for the extraction may be part of the feed to the hydrolysis or the product of the water scrubbing.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR687902X | 1950-04-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB687902A true GB687902A (en) | 1953-02-25 |
Family
ID=9026396
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB9792/51A Expired GB687902A (en) | 1950-04-27 | 1951-04-26 | Improvements in or relating to processes for the hydrolysis of methyl acetate and the treatment of aqueous mixtures of methyl acetate, methyl alcohol and acetic acid so obtained |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB687902A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1061063A1 (en) * | 1999-06-16 | 2000-12-20 | Kuraray Co., Ltd. | Method of producing carboxylic acid and alcohol |
WO2012164573A2 (en) | 2011-05-27 | 2012-12-06 | Reliance Industries Ltd., | Hydrolysis and esterification with acid catalysts |
WO2013132507A1 (en) | 2012-03-05 | 2013-09-12 | Reliance Industries Ltd., | An integrated process for the recovery of metal catalysts during the manufacture of purified terephthalic acid |
-
1951
- 1951-04-26 GB GB9792/51A patent/GB687902A/en not_active Expired
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1061063A1 (en) * | 1999-06-16 | 2000-12-20 | Kuraray Co., Ltd. | Method of producing carboxylic acid and alcohol |
SG82079A1 (en) * | 1999-06-16 | 2001-07-24 | Kuraray Co | Method of producing carboxylic acid and alcohol |
US6462231B1 (en) | 1999-06-16 | 2002-10-08 | Kuraray Co., Ltd. | Method of producing carboxylic acid and alcohol |
WO2012164573A2 (en) | 2011-05-27 | 2012-12-06 | Reliance Industries Ltd., | Hydrolysis and esterification with acid catalysts |
WO2013132507A1 (en) | 2012-03-05 | 2013-09-12 | Reliance Industries Ltd., | An integrated process for the recovery of metal catalysts during the manufacture of purified terephthalic acid |
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