GB841680A - Process for the manufacture of the lower alkyl esters of unsaturated aliphatic acids - Google Patents
Process for the manufacture of the lower alkyl esters of unsaturated aliphatic acidsInfo
- Publication number
- GB841680A GB841680A GB35215/58A GB3521558A GB841680A GB 841680 A GB841680 A GB 841680A GB 35215/58 A GB35215/58 A GB 35215/58A GB 3521558 A GB3521558 A GB 3521558A GB 841680 A GB841680 A GB 841680A
- Authority
- GB
- United Kingdom
- Prior art keywords
- acid
- unsaturated aliphatic
- water
- reactants
- silica gel
- 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
- C07C69/00—Esters of carboxylic acids; Esters of carbonic or haloformic acids
- C07C69/52—Esters of acyclic unsaturated carboxylic acids having the esterified carboxyl group bound to an acyclic carbon atom
- C07C69/533—Monocarboxylic acid esters having only one carbon-to-carbon double bond
- C07C69/54—Acrylic acid esters; Methacrylic acid esters
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
An unsaturated aliphatic ester is obtained by contacting a vapour-phase mixture comprising an a ,b -unsaturated aliphatic carboxylic acid and at least the stoichiometric proportion of a saturated aliphatic alcohol having not more than 8 carbon atoms with silica gel at a temperature above the boiling-point of the reactants and products in the presence of added water said water being added in a proportion of at least 1 mol. per mol. of said acid. The molar ratio of added water to acid is preferably in the range of 1 : 1 to 8 : 1 and it is preferred to use a stoichiometric excess of the alcohol. Specified alcohols are methanol, ethanol, butanol-1 and 2-ethyl hexanol and specified acids are acrylic and methacrylic acids. Suitable reaction temperatures are from 350 DEG to 750 DEG F. at atmospheric pressure and the process is suitably conducted in a vertical vessel containing a fixed catalyst bed, the reactants being introduced at the bottom of the vessel and the product removed overhead, or vice versa. Preferred contact times are between 15 and 120 seconds. Examples are given for the production of ethyl acrylate, n-butyl acrylate and methyl methacrylate and a comparative example is also given for the production of ethyl acrylate by reacting ethanol and acrylic acid in the vapour phase at 500 DEG F. in the presence of silica gel but without adding water to the reaction.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US841680XA | 1957-12-31 | 1957-12-31 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB841680A true GB841680A (en) | 1960-07-20 |
Family
ID=22183265
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB35215/58A Expired GB841680A (en) | 1957-12-31 | 1958-11-03 | Process for the manufacture of the lower alkyl esters of unsaturated aliphatic acids |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB841680A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1288596B (en) * | 1962-01-30 | 1969-02-06 | Knapsack Ag | Process for the production of acrylic acid n-butyl ester from aqueous acrylic acid and n-butanol |
-
1958
- 1958-11-03 GB GB35215/58A patent/GB841680A/en not_active Expired
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1288596B (en) * | 1962-01-30 | 1969-02-06 | Knapsack Ag | Process for the production of acrylic acid n-butyl ester from aqueous acrylic acid and n-butanol |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE2962683D1 (en) | Preparation of formic acid by hydrolysis of methyl formate | |
US4859793A (en) | Process for the production of fluoroalkyl acrylates | |
DK0383405T3 (en) | ester Preparation | |
GB903613A (en) | Improvements in or relating to the production of acetoacetic acid esters | |
GB841680A (en) | Process for the manufacture of the lower alkyl esters of unsaturated aliphatic acids | |
GB886750A (en) | Preparation of carboxylic esters | |
ES8303282A1 (en) | Esterification process of acetic acid by C2 to C5 alcohols. | |
GB953775A (en) | Processes for the preparation of sorbic acid and alkyl esters of sorbic acid | |
GB1107234A (en) | Production of acrylate and methacrylate esters | |
GB1028403A (en) | ||
GB952477A (en) | Improved process for obtaining ª-ª, ª-ª unsaturated carboxylic esters | |
GB1023176A (en) | Process for the preparation of acrylic acid esters | |
GB1017806A (en) | Esterification process | |
US2423641A (en) | Process for the preparation of thiol esters | |
US3182077A (en) | Dehydration of hydroxy esters | |
US3417129A (en) | Process for the manufacture of acetoacetic acid methyl ester and acetoacetic acid ethyl ester | |
GB1066117A (en) | Process for the manufacture of cyanoacetic acid esters | |
NL156124B (en) | PROCEDURE FOR PREPARING ALPHA-PHENYL ETHYL ALCOHOL BY OXIDATION OF ETHYLBENZENE. | |
US2894980A (en) | Preparation of alkoxysuccinic acid esters | |
US2540070A (en) | Acyloxymethylene-pentenoates | |
US3008979A (en) | Divinyl d-camphorate | |
GB829889A (en) | Esterification of pyridine carboxylic acids | |
SE7909596L (en) | PROCEDURE FOR PREPARING BASIC ESTERS OF SUBSTITUTED HYDROXICYCLOHEXANCHOXYL ACIDS | |
GB762690A (en) | Improved process for the recovery of synthetic polyester scrap | |
GB886436A (en) | Basic esters |