A process for the preparation of substituted pyridine compounds and intermediates thereof
US-2024018106-A1 · Jan 18, 2024 · US
US12404234B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12404234-B2 |
| Application number | US-202017292951-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 14, 2020 |
| Priority date | Nov 11, 2019 |
| Publication date | Sep 2, 2025 |
| Grant date | Sep 2, 2025 |
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The present invention relates to a method of producing an acrylonitrile dimer, the method including: feeding an acrylonitrile monomer, a nonpolar solvent, an alcohol solvent, and a phosphorus-based catalyst to a dimerization reactor to perform a dimerization reaction and reaction product to a distillation column; feeding the acrylonitrile monomer, the nonpolar solvent, and the alcohol solvent from the distillation column to the dimerization reactor; feeding an acrylonitrile dimer and the phosphorus-based catalyst from the distillation column to an extraction device; oxidizing the phosphorus-based catalyst by feeding water including an acid component to the extraction device to inactivate the phosphorus-based catalyst; and separating the inactivated phosphorus-based catalyst and the acrylonitrile dimer.
Opening claim text (preview).
The invention claimed is: 1. A method of producing an acrylonitrile dimer, the method comprising: feeding an acrylonitrile monomer, a nonpolar solvent, an alcohol solvent, and a phosphorus-based catalyst to a dimerization reactor to perform a dimerization reaction and feeding a reaction product to a distillation column; feeding the acrylonitrile monomer, the nonpolar solvent, and the alcohol solvent partially or entirely separated from the distillation column to the dimerization reactor; and feeding an acrylonitrile dimer and the phosphorus-based catalyst separated from the distillation column to an extraction device; oxidizing the phosphorus-based catalyst by feeding water including an acid component to the extraction device to inactivate the phosphorus-based catalyst; and separating the inactivated phosphorus-based catalyst and the acrylonitrile dimer. 2. The method of claim 1 , wherein the phosphorus-based catalyst is represented by Formula 1: in Formula 1, R represents an alkyl group having 1 to 5 carbon atoms or a cycloalkyl group having 1 to 8 carbon atoms, each of R 1 to R 3 represents hydrogen, or an alkyl group, amine group, or alkoxy group having 1 to 5 carbon atoms, and n and m are each independently an integer of 1 or 2. 3. The method of claim 1 , wherein a content of the alcohol solvent in the extraction device is 1 wt % or less. 4. The method of claim 1 , wherein a content of the nonpolar solvent in the extraction device is 5 wt % or less. 5. The method of claim 1 , wherein the water including the acid component is fed in an amount of 2 equivalents or more with respect to the phosphorus-based catalyst. 6. The method of claim 1 , wherein in the oxidizing of the phosphorus-based catalyst by feeding water including an acid component to the extraction device to inactivate the phosphorus-based catalyst, the water including the acid component includes one or more selected from the group consisting of a hydrochloric acid aqueous solution, a sulfuric acid aqueous solution, and a nitric acid aqueous solution. 7. The method of claim 1 , wherein the inactivated phosphorus-based catalyst is represented by Formula 2: in Formula 2, each of R 1 to R 3 represents hydrogen, or an alkyl group, amine group, or alkoxy group having 1 to 5 carbon atoms, and n and m are each independently an integer of 1 or 2. 8. The method of claim 1 , wherein the inactivated phosphorus-based catalyst is a solid. 9. The method of claim 1 , wherein the separating of the inactivated phosphorus-based catalyst and the acrylonitrile dimer is performed using a filter. 10. The method of claim 1 , wherein the separated phosphorus-based catalyst is reused in the dimerization reactor. 11. The method of claim 1 , wherein in the distillation column, an operation temperature is 40° C. to 150° C., and an operation pressure is 0.001 bar to 3 bar. 12. The method of claim 2 , wherein in Formula 1, R represents an ethyl group, each of R 1 to R 3 represents hydrogen, and n is 2 and m is 1. 13. The method of claim 7 , wherein in Formula 2, each of R 1 to R 3 represents hydrogen, and n is 2 and m is 1.
Separation; Purification · CPC title
Phosphorus containing compounds · CPC title
containing at least two cyano groups bound to the carbon skeleton · CPC title
Separation; Purification; Stabilisation; Use of additives · CPC title
using catalysts, e.g. selective catalysts · CPC title
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