Use of novel cyclic carbaldeydes as an aromatic substance
US-10112882-B2 · Oct 30, 2018 · US
US10532970B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10532970-B2 |
| Application number | US-201716307540-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 27, 2017 |
| Priority date | Jun 29, 2016 |
| Publication date | Jan 14, 2020 |
| Grant date | Jan 14, 2020 |
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Process for the preparation of alpha, beta unsaturated aldehydes by oxidation of alcohols where the oxidant is oxygen in the presence of a catalyst comprising platinum on a support in the presence of a liquid phase which contains at least 25 weight-% water based on the total weight of the liquid phase.
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The invention claimed is: 1. A process for the preparation of alpha, beta unsaturated aldehydes of general formula (I) (R 1 )(R 2 )C═C(R 3 )—CHO, (I) wherein R 1 , R 2 and R 3 , independently of one another, are selected from the group consisting of H, CH 3 and C 2 H 5 and wherein R 3 is H, by oxidation of alcohols of general formula (II) (R 1 )(R 2 )C═C(R 3 )—CH 2 —OH, (II) wherein R 1 , R 2 and R 3 have the meaning as given above in the presence of a catalyst and in the presence of a liquid phase, wherein the liquid phase contains at least 25 weight-% water based on the total weight of the liquid phase, determined at a temperature of 20° C. and a pressure of 1 bar and wherein the oxidant is oxygen, and wherein the catalyst comprises platinum on a support and the alpha, beta unsaturated aldehyde has a selectivity (based on the alcohol of general formula (II)) in the range of over 90%. 2. The process according to claim 1 , wherein an alcohol according to formula (II) is used, wherein R 3 is H and R 2 and R 1 are CH 3 . 3. The process according to claim 1 , wherein the liquid phase contains at least 50 weight-% water based on the total weight of the liquid phase. 4. The process according to claim 1 , wherein the oxidation is carried out at a temperature of 20° C. to 100° C. 5. The process according to claim 1 , wherein the oxidation is carried out under a partial pressure of oxygen between 0.2 and 8 bar. 6. The process according to claim 2 , wherein the liquid phase contains at least 50 weight % water based on the total weight of the liquid phase. 7. The process according to claim 1 , wherein the liquid phase contains at least 70 weight % water based on the total weight of the liquid phase. 8. The process according to claim 2 , wherein the liquid phase contains at least 70 weight % water based on the total weight of the liquid phase. 9. The process according to claim 2 , wherein the oxidation is carried out at a temperature of 20° C. to 100° C. 10. The process according to claim 3 , wherein the oxidation is carried out at a temperature of 20° C. to 100° C. 11. The process according to claim 1 , wherein the oxidation is carried out at a temperature of 20° C. to 70° C. 12. The process according to claim 2 , wherein the oxidation is carried out at a temperature of 20° C. to 70° C. 13. The process according to claim 3 , wherein the oxidation is carried out at a temperature of 20° C. to 70° C. 14. The process according to claim 8 , wherein the oxidation is carried out at a temperature of 20° C. to 70° C. 15. The process according to claim 2 , wherein the oxidation is carried out under a partial pressure of oxygen between 0.2 and 8 bar. 16. The process according to claim 14 , wherein the oxidation is carried out under a partial pressure of oxygen between 0.2 and 8 bar. 17. The process according to claim 1 , wherein said catalyst comprises a promotor, which enhance the activity of the catalytically active metal. 18. The process according to claim 1 , wherein said promotor is bismuth (Bi), antimony (Sb), lead (Pb), cadmium (Cd), tin (Sn) or tellurium (Te). 19. The process according to claim 1 , wherein the alpha, beta unsaturated aldehyde has a selectivity (based on the alcohol of general formula (II)) in the range of over 93%. 20. The process according to claim 1 , wherein the alpha, beta unsaturated aldehyde has a selectivity (based on the alcohol of general formula (II)) in the range of over 95%. 21. The process according to claim 1 , wherein the alpha, beta unsaturated aldehyde has a selectivity (based on the alcohol of general formula (II)) in the range of over 97%. 22. The process according to claim 1 , wherein the alpha, beta unsaturated aldehyde has a selectivity (based on the alcohol of general formula (II)) in the range of over 99%.
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