Method for producing thermoplastic compositions for mechanically and/or thermally stressed components
US-2022246252-A1 · Aug 4, 2022 · US
US11976373B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11976373-B2 |
| Application number | US-202118001079-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 26, 2021 |
| Priority date | Jun 10, 2020 |
| Publication date | May 7, 2024 |
| Grant date | May 7, 2024 |
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A method for the electrochemical preparation of alkanedicarboxylic acids involves a ring-opening oxidation with a doped Ni(O)OH foam electrode in an aqueous alkaline solution.
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The invention claimed is: 1. A method for the preparation of alkanedicarboxylic acids, the method comprising: oxidizing a cyclic reactant in a ring-opening oxidation in an aqueous alkaline solution, wherein the oxidation is carried out at an Ni(O)OH foam electrode doped with at least one element of main group 5 and/or 6, according to Scheme (I): wherein represents a single or double bond, R accordingly being present or not, wherein R is hydrogen or an acyl radical, wherein the acyl radical is a radical of an aliphatic monocarboxylic acid having 2 to 8 carbon atoms, and wherein A is a hydrocarbon having 4 to 30 carbon atoms, in which all ring carbon atoms of A in the cyclic reactant of scheme (I) bear at least one hydrogen substituent, and wherein the Ni(O)OH foam electrode comprises 2 to 10% by weight of phosphorus, the phosphorus as an element and based on a metal mass of the Ni(O)OH foam electrode. 2. The method according to claim 1 , wherein the Ni(O)OH foam electrode is doped with at least one selected from the group consisting of phosphorus, arsenic, selenium, and sulfur. 3. The method according to claim 1 , wherein the Ni(O)OH foam electrode comprises 3 to 9% by weight of the phosphorus, the phosphorus as an element and based on the metal mass of the electrode. 4. The method according to claim 1 , wherein the Ni(O)OH foam electrode is two or more millimeters thick. 5. The method according to claim 1 , wherein the Ni(O)OH foam electrode comprises nickel as metal. 6. The method according to claim 5 , wherein the Ni(O)OH foam electrode comprises the nickel in an amount of at least 80% by weight. 7. The method according to claim 1 , wherein the aqueous alkaline solution comprises up to 30% by volume of a cosolvent. 8. The method according to claim 1 , wherein an alkaline additive in the aqueous alkaline solution is lithium hydroxide, sodium hydroxide, or potassium hydroxide. 9. The method according to claim 8 , wherein a concentration of the alkaline additive is 0.5 to 2 mol/1, based on the aqueous alkaline solution. 10. The method according to claim 8 , wherein no further anions of bases are present in the aqueous alkaline solution other than the alkaline additive. 11. The method according to claim 1 , wherein in scheme (I) when R=hydrogen and is a single bond, a concentration of cycloalkanols is 0.06 to 0.5 mol/1. 12. The method according to claim 11 , wherein the concentration of cycloalkanols is 0.09 to 0.11 mol/1. 13. The method according to claim 1 , wherein the ring-opening oxidation is according to Scheme (II): wherein R 1 , R 2 , R 3 are the same or different, and are hydrogen or alkyl radicals having 1 to 8 carbon atoms, linear or branched, in which at least one of R 1 , R 2 , R 3 is an alkyl radical. 14. The method according to claim 13 , wherein only one of R 1 , R 2 , R 3 is an alkyl radical having 1 to 4 carbon atoms. 15. The method according to claim 13 , wherein R 1 and R 3 are hydrogen and R 2 is an alkyl radical having 1 to 4 carbon atoms. 16. The method according to claim 1 , wherein the method is carried out at a current density of 2 to 10 mA/cm 2 , an area referring to a geometric area without consideration of inner surface area of the foam. 17. The method according to claim 1 , wherein the oxidizing comprises electrolysis carried out in a batch electrolytic cell or in a continuous flow electrolytic cell. 18. The method according to claim 17 , wherein the oxidizing comprises electrolysis carried out in the continuous flow electrolytic cell. 19. The method according to claim 1 , wherein a cathode material is stainless steel, platinum, nickel, or a mixture thereof. 20. The method according to claim 1 , wherein the oxidizing comprises electrolysis carried out at a temperature of 20-70° C.
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