Preparation of diesters of (meth)acrylic acid from epoxides

US11319276B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11319276-B2
Application numberUS-201917268465-A
CountryUS
Kind codeB2
Filing dateAug 15, 2019
Priority dateAug 16, 2018
Publication dateMay 3, 2022
Grant dateMay 3, 2022

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

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The invention relates to a method for preparation of diesters from anhydrides of carboxylic acids.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for preparation of a diester of general Formula (I): wherein: R 1 is a hydrogen atom or a methyl group; R 2 to R 6 are independently selected from hydrogen atoms or optionally substituted aliphatic or aromatic substituents having up to 17 carbon atoms; wherein the process comprises at least process step (a): (a) reacting a (meth)acrylic anhydride of general Formula (II): with an epoxide of general Formula (III): to deliver a product mixture comprising the diester of general Formula (I); wherein the reaction is carried out in the presence of a catalyst in combination with a co-catalyst, wherein: the catalyst comprises a first catalyst, a second catalyst or a combination of both, and: the first catalyst is a halide of magnesium or a trifluoromethanesulfonate of a rare earth element; and the second catalyst is a chromium (III) salt; the co-catalyst is selected from the group consisting of: a tertiary amine; a quaternary ammonium salt; a tertiary phosphine; and a quaternary phosphonium salt. 2. The process of claim 1 , wherein: R 1 is a hydrogen atom, R 2 is a vinyl group, and the (meth)acrylic anhydride of formula (II) is acrylic acid anhydride; or alternatively: R 1 is a methyl group, R 2 is a 1-methylvinyl group and the (meth)acrylic anhydride of formula (II) is methacrylic acid anhydride. 3. The process of claim 1 , wherein the optionally substituted aliphatic or aromatic substituents having up to 17 carbon atoms are selected from the group consisting of: optionally substituted alkyl, cycloalkyl, alkenyl, or alkadienyl substituents having up to 17 carbon atoms optionally substituted with one substituent R 7 selected from: a halogen atom, —CN, —SCN, —OCN, and —NCO. 4. The process of claim 1 , wherein the epoxide of general Formula (III) is selected from the group consisting of: ethylene oxide; propylene oxide; 1-hexene oxide; cyclohexene oxide; cyclopentene oxide; 1-butene oxide; 2-butene oxide; isobutene oxide; styrene oxide; and glycidyl methacrylate. 5. The process of claim 1 , wherein process step (a) is carried out in the presence of the first catalyst, the second catalyst and the co-catalyst. 6. The process of claim 1 , wherein the co-catalyst is a quaternary ammonium salt. 7. The process of claim 1 , wherein the co-catalyst is selected from the group consisting of: tetrabutylammonium chloride; tetrabutylammonium bromide; tetraethylammonium chloride; tetrabutylammonium acetate; tetramethylammonium chloride; tetrapentylammonium bromide; cetyl-trimethylammonium bromide; 1-butyl-3-methyl-imidazolyl chloride; cetylpyridinium chloride; and triethylbenzylammonium chloride. 8. The process of claim 1 , wherein the second catalyst is a chromium (III) carboxylate. 9. The process of claim 8 , wherein the chromium (III) carboxylate is selected from the group consisting of: chromium (III) 2-ethylhexanoate; chromium (III) heptanoate; chromium (III) acetate; and chromium (III) methacrylate. 10. The process of claim 1 , wherein the total amount of the first catalyst in process step (a) is between 0.001 mol.-% and 10 mol.-%, based on the amount of the epoxide of general Formula (III). 11. The process of claim 1 , wherein the total amount of the second catalyst in process step (a) is between 0.001 mol.-% and 10 mol.-%, based on the amount of the epoxide of general Formula (III). 12. The process of claim 1 , wherein the total amount of the co-catalyst in process step (a) is between 0.001 mol.-% and 10 mol.-%, based on the amount of the epoxide of general Formula (III). 13. The process of claim 1 , wherein the molar ratio anhydride of the general Formula (II): epoxide of the general Formula (III) in process step (a) is between 5:1 and 1:0.1. 14. The process of claim 1 , wherein the temperature during process step (a) is in the range 20° C. to 140° C. 15. The process of claim 1 , wherein the process is carried out in the presence of at least 10 mol % excess of the anhydride. 16. The process of claim 15 , further comprising process steps (b) and (c) which are carried out after process step (a): (b) adding an auxiliary alcohol to the product mixture obtained in process step (a) to form a product mixture comprising the diester of the general Formula (I) and an ester of the auxiliary alcohol; and (c) removing of the ester of the auxiliary alcohol from the product mixture obtained in process step (b); wherein the auxiliary alcohol is a primary or secondary alcohol having a boiling point of not more than 150° C., measured at a pressure of 10 5 Pa. 17. The process of claim 16 , wherein, in process step (c), the ester of the auxiliary alcohol is removed from the product mixture by distillation. 18. The process of claim 17 , wherein, in process step (a) the epoxide of general Formula (III) is selected from the group consisting of: ethylene oxide; propylene oxide; 1-hexene oxide; cyclohexene oxide; cyclopentene oxide; 1-butene oxide; 2-butene oxide; isobutene oxide; styrene oxide; and glycidyl methacrylate. 19. The process of claim 18 , wherein process step (a) is carried out in the presence of the first catalyst, the second catalyst and the co-catalyst. 20. The process of claim 19 , wherein the co-catalyst is selected from the group consisting of: tetrabutylammonium chloride; tetrabutylammonium bromide; tetraethylammonium chloride; tetrabutylammonium acetate; tetramethylammonium chloride; tetrapentylammonium bromide; cetyl-trimethylammonium bromide; 1-butyl-3-methyl-imidazolyl chloride; cetylpyridinium chloride; and triethylbenzylammonium chloride; and the second catalyst is a chromium (III) carboxylate.

Assignees

Inventors

Classifications

  • with alkaline earth metals, magnesium, beryllium, zinc, cadmium or mercury · CPC title

  • Chromium · CPC title

  • Phosphines or phosphonium compounds, i.e. phosphorus bonded to at least one carbon atom, including e.g. sp2-hybridised phosphorus compounds such as phosphabenzene, the other atoms bonded to phosphorus being either carbon or hydrogen · CPC title

  • Quaternary ammonium compounds · CPC title

  • Chromium · CPC title

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What does patent US11319276B2 cover?
The invention relates to a method for preparation of diesters from anhydrides of carboxylic acids.
Who is the assignee on this patent?
Evonik Operations Gmbh
What technology area does this patent fall under?
Primary CPC classification C07C67/26. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue May 03 2022 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 6 related publications on this page (citations in our corpus or others sharing the same primary CPC).