Metal oxide-organic hybrid materials for heterogeneous catalysis and methods of making and using thereof
US-2016152648-A1 · Jun 2, 2016 · US
US10053409B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10053409-B2 |
| Application number | US-201615578959-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 2, 2016 |
| Priority date | Jun 3, 2015 |
| Publication date | Aug 21, 2018 |
| Grant date | Aug 21, 2018 |
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The present invention relates to a process for producing 3-methylcyclopentadecane-1,5-dione of formula (I), which comprises the oxidation of 14-methyl-bicyclo[10.3.0]pentadecen[1 (12)] of formula (II) with an oxidizing agent, where the oxidation is performed by using a mixture of formic acid with H 2 O 2 as sole oxidizing agent in the presence of water and where the amount of H 2 O 2 is at least 1.1 mol H 2 O 2 per mol of the compound of formula (II).
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The invention claimed is: 1. A process for preparing 3-methylcyclopentadecane-1,5-dione, which comprises oxidizing 14-methylbicyclo[10.3.0]pentadecen[1(12)] with an oxidizing agent, where the oxidation is performed by using a mixture of formic acid with H 2 O 2 as sole oxidizing agent in the presence of water and where the amount of H 2 O 2 is at least 1.1 mol H 2 O 2 per mol of 14-methylbicyclo[10.3.0]pentadecen[1(12)]. 2. The process of claim 1 , wherein the amount of H 2 O 2 is from 1.4 to 4.0 mol H 2 O 2 per mol of 14-methylbicyclo[10.3.0]pentadecen[1(12)]. 3. The process of claim 1 , wherein the amount of H 2 O 2 is from 1.5 to 3.5 mol H 2 O 2 per mol of 14-methylbicyclo[10.3.0]pentadecen[1(12)]. 4. The process of claim 1 , wherein H 2 O 2 is added to the mixture of 14-methylbicyclo[10.3.0]pentadecen[1(12)] and formic acid. 5. The process of claim 3 , wherein the total amount of added H 2 O 2 is added over a period of at least 2 h. 6. The process of claim 3 , wherein the total amount of added H 2 O 2 is added over a period of from 2 to 24 h. 7. The process of claim 3 , wherein less than 70% of the total amount of H 2 O 2 used in the process is present at the beginning of the oxidation. 8. The process of claim 3 , wherein less than 70% and at most 50% of the total amount of H 2 O 2 used in the process is present at the beginning of the oxidation. 9. The process of claim 5 , wherein at least 50% of the total amount of H 2 O 2 are added to the reaction mixture while the oxidation reaction takes place. 10. The process of claim 1 , wherein the oxidation of the compound of 14-methylbicyclo[10.3.0]pentadecen[1(12)] is performed at a temperature of −20 to 100° C. 11. The process of claim 1 , wherein the oxidation of the compound of 14-methylbicyclo[10.3.0]pentadecen[1(12)] is performed at a temperature of from 0 to 80° C. 12. The process of claim 1 , wherein the oxidation of the compound of 14-methylbicyclo[10.3.0]pentadecen[1(12)] is performed at a temperature of from 10 to 60° C. 13. The process of claim 1 , wherein the concentration of water in the reaction mixture is from 3 to 25% by weight. 14. The process of claim 1 , wherein H 2 O 2 is used as an aqueous solution. 15. The process of claim 14 , wherein the concentration of H 2 O 2 in the aqueous H 2 O 2 is from 25 to 50% by weight. 16. The process of claim 1 , where the weight ratio of 14-methylbicyclo[10.3.0]pentadecen[1(12)] and the formic acid is in the range from 1:20 to 1:2.
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