Synthesis of a branched unsaturated compound by means of cross metathesis
US-2015376108-A1 · Dec 31, 2015 · US
US10913702B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10913702-B2 |
| Application number | US-201816771999-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 14, 2018 |
| Priority date | Jan 15, 2018 |
| Publication date | Feb 9, 2021 |
| Grant date | Feb 9, 2021 |
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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.
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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
Terephthalic acid esters · CPC title
of acids with a six-membered ring · CPC title
Use of additives, e.g. for stabilisation · CPC title
by addition to unsaturated carbon-to-carbon bonds · CPC title
by splitting-off hydrogen or functional groups; by hydrogenolysis of functional groups · CPC title
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