Method for producing unsaturated acid ester or unsaturated acid

US9598345B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9598345-B2
Application numberUS-201614991393-A
CountryUS
Kind codeB2
Filing dateJan 8, 2016
Priority dateJul 12, 2013
Publication dateMar 21, 2017
Grant dateMar 21, 2017

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

The present invention relates to a method for producing an unsaturated-acid ester or an unsaturated acid, containing a step of reacting a compound (1) represented by the following formula (1) with a compound represented by the following formula (2) (excluding the compound (1)) in the presence of a Lewis acid catalyst at a temperature of the boiling point of the compound (1) or higher and 350° C. or lower, thereby obtaining products including a compound represented by the following formula (3): (in formula (1) and formula (3), R 1 , R 2 and R 4 each independently may be hydrogen atom or an alkyl group, R 3 and R 5 each independently are hydrogen atom or a deuterium atom, and X is a halogen atom; in formula (2) and formula (3), R 6 may be hydrogen atom, an alkyl group or an aryl group, and R 7 is hydrogen atom or a deuterium atom).

First claim

Opening claim text (preview).

The invention claimed is: 1. A method for producing an unsaturated-acid ester or an unsaturated acid, the method comprising reacting a compound (1) of the formula (1) with a compound (2) of the formula (2), which is different from the compound of the formula (1), in the presence of a Lewis acid catalyst at a temperature within a range from 170° C. to 350° C., thereby obtaining a reaction product comprising a compound (3) of the formula (3) wherein R 1 , R 2 , and R 4 each independently are selected from the group consisting of a hydrogen atom, a deuterium atom, and an alkyl group which has a carbon number of from 1 to 3 and may be optionally substituted with a halogen atom and/or a deuterium atom, R 3 and R 5 each independently are selected from the group consisting of a hydrogen atom and a deuterium atom, and X is a chlorine atom, a fluorine atom, a bromine atom, or an iodine atom; R 6 —OR 7   (2), wherein R 6 is selected from the group consisting of a hydrogen atom, a deuterium atom, and an alkyl group which has a carbon number of from 1 to 11 and may be optionally substituted with a halogen atom and/or a deuterium atom, or an aryl group and may be optionally substituted with a halogen atom and/or a deuterium atom, and R 7 is a hydrogen atom or a deuterium atom; and wherein R 1 , R 2 , and R 4 are the same as defined with regard to the formula (1), and R 6 is the same as defined with regard to the formula (2); wherein the Lewis acid catalyst is at least one selected from the group consisting of ZnO—ZrO 2 , ZnO—Al 2 O 3 , ZnO—TiO 2 , In 2 O 3 —ZrO 2 , NiO—ZrO 2 , CoO—ZrO 2 , MnO—ZrO 2 , silica gel, γ-alumina, ZrO 2 , ZnO—SiO 2 , Zr PbO x , Al 2 O 3 —ZrO 2 , MgO—ZrO 2 , ZnO—Cr 2 O 3 , TiO 2 , and Zr—NiOx, and wherein the Lewis acid catalyst is fixed to a support. 2. The method according to claim 1 , wherein the Lewis acid catalyst is a solid acid. 3. The method according to claim 1 , wherein the reaction is conducted in a gas phase. 4. The method according to claim 1 , wherein an amount of the compound (2) is from 0.5 to 20 mol, per 1 mol of the compound (1). 5. The method according to claim 1 , wherein an amount of the compound (2) is from 1 to 10 mol, per 1 mol of the compound (1). 6. The method according to claim 1 , wherein an amount of the Lewis acid catalyst, per 1 mol of the compound (1) present in a reaction vessel, is from 0.001 to 1 mol. 7. The method according to claim 1 , wherein an amount of the Lewis acid catalyst, per 1 mol of the compound (1) present in a reaction vessel in a batch mode or per 1 mol of the compound (1) residing in a reaction vessel in a continuous mode, is from 0.01 to 0.2 mol. 8. The method according to claim 1 , wherein the reacting temperature is from 200 to 300° C. 9. The method according to claim 1 , wherein the reaction is conducted in a liquid phase. 10. The method according to claim 1 , wherein in the reaction a compound or gas which does not chemically react with starting materials and the reaction product is used as a solvent or a diluent gas, wherein the solvent is selected from the group consisting of pentane, hexane, heptane, petroleum ether, dimethyl ether, diethyl ether, tetrahydrofuran, 1,2-dimethyoxyethane, dichloromethane, chloroform, carbon tetrachloride, dichloroethane, acetic acid, benzoic acid, acetic anhydride, ethyl acetate, acetone, 2-butanone, acetonitrile, dimethylformamide, dimethylacetamide, dimethyl sulfoxide, benzene, toluene, chlorobenzene, dichlorobenzene, benzonitrile, nitromethane, nitrobenzene, and a mixture thereof, and wherein the diluent gas is selected from the group consisting of nitrogen, helium, argon, and a mixture thereof. 11. The method according to claim 10 , wherein an amount of the solvent or the diluent gas is in a range that a concentration of the compound (1) is kept at 5% by mass or higher. 12. The method according to claim 1 , wherein the reaction is conducted in a continuous mode and a space velocity is from 1 to 500,000 h −1 . 13. The method according to claim 1 , wherein a reaction pressure is from 0 MPa to 10 MPa. 14. The method according to claim 1 , wherein a reaction pressure is from 0.05 MPa to 2 MPa. 15. The method according to claim 1 , wherein when the reacting is conducted in a batch mode, a reaction time is from 10 minutes to 12 hours, and when the reacting is conducted in a continuous mode, a reaction time is from 0.1 second to 60 minutes.

Assignees

Inventors

Classifications

  • C07C67/10Primary

    by reacting carboxylic acids or symmetrical anhydrides with ester groups or with a carbon-halogen bond (preparation from carboxylic acid halides C07C67/14) · CPC title

  • Acrylic acid; Methacrylic acid · CPC title

  • by hydrolysis of —CX3 groups, X being halogen · CPC title

  • C07C67/00Primary

    Preparation of carboxylic acid esters · CPC title

  • Acrylic acid esters; Methacrylic acid esters · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US9598345B2 cover?
The present invention relates to a method for producing an unsaturated-acid ester or an unsaturated acid, containing a step of reacting a compound (1) represented by the following formula (1) with a compound represented by the following formula (2) (excluding the compound (1)) in the presence of a Lewis acid catalyst at a temperature of the boiling point of the compound (1) or higher and 350° C…
Who is the assignee on this patent?
Asahi Glass Co Ltd
What technology area does this patent fall under?
Primary CPC classification C07C67/10. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Mar 21 2017 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 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).