Method for cycloaddition of dimethyl muconate

US10913702B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10913702-B2
Application numberUS-201816771999-A
CountryUS
Kind codeB2
Filing dateDec 14, 2018
Priority dateJan 15, 2018
Publication dateFeb 9, 2021
Grant dateFeb 9, 2021

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

A method for cycloaddition of dimethyl muconate is disclosed. According to the method, a direct transferring of a solid phase trans,trans-dimehtyl muconate into a reactor pre-filled with ethylene gas increases the efficiency of the reaction and suppress side reactions resulting an improvements in yield and purity. Furthermore, the method is capable of obtaining a high yield of dimethylcyclohex-2-en-1,4-dicarboxylate at a lower cost, and therefore is also useful for the mass synthesis of dimethyl terephthalate.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process for cycloaddition of dimethyl muconate, which comprises: (1) preparing a reactor filled with ethylene gas; and (2) introducing a compound of the following Formula 1 in a solid phase to the reactor and carrying out a cycloaddition reaction to obtain a compound of the following Formula 2 2. The process for cycloaddition of dimethyl muconate of claim 1 , wherein the reactor in step (1) has an internal pressure of 140 bar or more. 3. The process for cycloaddition of dimethyl muconate of claim 1 , wherein the reactor in step (1) has an internal temperature of 170 to 250° C. 4. The process for cycloaddition of dimethyl muconate of claim 1 , wherein in step (2), the compound of Formula 1 is divided into two or more and then introduced into the reactor. 5. The process for cycloaddition of dimethyl muconate of claim 4 , wherein the cycloaddition reaction is carried out for 1 to 6 hours at the time of each divided introduction. 6. The process for cycloaddition of dimethyl muconate of claim 1 , wherein the reactor in step (1) is filled with a solvent for the cycloaddition reaction of the compound of Formula 1. 7. The process for cycloaddition of dimethyl muconate of claim 6 , wherein the total amount of the compound of Formula 1 divided and introduced into the reactor is 1.0 to 3.0 moles based on 1 liter of the solvent, and the yield of the cycloaddition reaction is 85% or more. 8. The process for cycloaddition of dimethyl muconate of claim 6 , wherein in step (2), the compound of Formula 1 is divided into two or more and then introduced into the reactor; and the amount of the compound of Formula 1 introduced into the reactor at each time is 0.1 to 0.5 mole based on 1 liter of the solvent. 9. The process for cycloaddition of dimethyl muconate of claim 8 , wherein the total amount of the compound of Formula 1 divided and introduced into the reactor is 1.0 to 3.0 moles based on 1 liter of the solvent. 10. The process for cycloaddition of dimethyl muconate of claim 6 , wherein the solvent is selected from the group consisting of meta-xylene, tetrahydrofuran, ethyl acetate, dimethyl ethylene glycol, N-methyl pyrrolidone, dimethylsulfoxide, and mixtures thereof. 11. The process for cycloaddition of dimethyl muconate of claim 1 , wherein the reactor in step (1) is filled with a solvent for the cycloaddition reaction of the compound of Formula 1 and has an internal pressure of 140 bar or more and an internal temperature of 170 to 250° C.; and in step (2), the compound of Formula 1 is divided into two or more and then introduced into the reactor, wherein the amount of the compound of Formula 1 introduced into the reactor at each time is 0.1 to 0.5 mole based on 1 liter of the solvent, the total amount of the compound of Formula 1 divided and introduced into the reactor is 1.0 to 3.0 moles based on 1 liter of the solvent, and the cycloaddition reaction is carried out for 1 to 6 hours at the time of each divided introduction. 12. A process for preparing dimethyl terephthalate, which comprises: (1) preparing a reactor filled with ethylene gas; (2) introducing a compound of the following Formula 1 in a solid phase to the reactor and carrying out a cycloaddition reaction to obtain a compound of the following Formula 2; and (3) obtaining dimethyl terephthalate from the compound of Formula 2 through an aromatization reaction

Assignees

Inventors

Classifications

  • Terephthalic acid esters · CPC title

  • of acids with a six-membered ring · CPC title

  • Use of additives, e.g. for stabilisation · CPC title

  • C07C67/347Primary

    by addition to unsaturated carbon-to-carbon bonds · CPC title

  • C07C67/317Primary

    by splitting-off hydrogen or functional groups; by hydrogenolysis of functional groups · CPC title

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What does patent US10913702B2 cover?
A method for cycloaddition of dimethyl muconate is disclosed. According to the method, a direct transferring of a solid phase trans,trans-dimehtyl muconate into a reactor pre-filled with ethylene gas increases the efficiency of the reaction and suppress side reactions resulting an improvements in yield and purity. Furthermore, the method is capable of obtaining a high yield of dimethylcyclohex-…
Who is the assignee on this patent?
Sk Chemicals Co Ltd
What technology area does this patent fall under?
Primary CPC classification C07C67/347. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Feb 09 2021 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).