초록

Disclosed is a mixed oxide catalyst, preferably for selective oxidation of CO in hydrogen rich gas mixtures, or in oxygen containing gas mixtures in the presence of water and carbon dioxide, comprising about 15 to 30 at.-% Cu, about 55 to 77 at.-% Mn and about 7.5 to 10 at.-% Ce.

대표청구항 ▼

The invention claimed is: 1. Mixed oxide catalyst, preferably for selective oxidation of CO in hydrogen rich gas mixtures, or in oxygen containing gas mixtures in the presence of water and carbon dioxide, comprising about 15 to 30 at.-% Cu, about 55 to 77 at.-% Mn and about 7.5 to 15 at.-% Ce. 2.

The invention claimed is: 1. Mixed oxide catalyst, preferably for selective oxidation of CO in hydrogen rich gas mixtures, or in oxygen containing gas mixtures in the presence of water and carbon dioxide, comprising about 15 to 30 at.-% Cu, about 55 to 77 at.-% Mn and about 7.5 to 15 at.-% Ce. 2. The catalyst of claim 1, wherein the quantity of the Ce is from 7.5 to 10 at.%. 3. A process for producing the mixed oxide catalyst of claim 1 for selective oxidation of CO in a hydrogen-rich gas mixture or in an oxygen-containing gas mixture in the presence of water and carbon dioxide comprising preparing a salt solution of Cu, Mn and Ce comprising, based on the total amount of Cu, Mn-and Ce-salts, from about 15 to about 30 at. % Cu, from about 55 to 77 at.-% Mn and from about 7.5 to 15 at.-% Ce, preparing a precipitate by co-precipitation of said salt solution of Cu, Mn and Ce with an alkaline precipitating agent, and drying and calcining the precipitate. 4. The process of claim 3, wherein a salt of La is co-precipitated with salts of Cu, Mn and Ce. 5. The process of claim 3, wherein the precipitating agent is selected from NaHCO3, Na2CO3 and mixtures thereof. 6. A process for producing the mixed oxide catalyst of claim 1 for selective oxidation of CO in a hydrogen-rich gas mixture of in an oxygen-containing gas mixture in the presence of water and carbon dioxide comprising preparing a carrier compound of MnO2, impregnating the carrier with a salt solution of Cu and Ce, said amount of MnO2 and Cu-and Ce-salts being selected such that a precipitate obtained comprises, based on the total amount of Cu, Mn-and Ce-salts, from about 15 to 30 at.-% Cu, from about 55 to 77 at.-% Mn and from about 7.5 to 15 at.-% Ce, and drying and calcining the precipitate. 7. The process of claim 6, wherein the salt solution further comprises a salt of La. 8. A process for the production of the mixed oxide catalyst of claim 1 for selective oxidation of CO in a hydrogen-rich gas mixture or in an oxygen-containing gas mixture in the presence of water and carbon dioxide comprising preparing a carrier comprised of ZrO2, impregnating that carrier with a salt solution of Cu, Ce and Mn comprising, based on the total amount of Cu, Mn-and Ce-salts, from about 15 to 30 at.-% Cu, from about 55 to 77 at.-% Mn and from about 7.5 to 15 at.-% Ce, and drying and calcining the impregnated carrier. 9. The process of claim 8, wherein the carrier is further impregnated with a salt solution of La. 10. The process of claim 8, wherein the salts are fixed on the carrier by use of a precipitating agent. 11. A mixed oxide catalyst for selective oxidation of CO in a hydrogen-rich gas mixture or in an oxygen-containing gas mixture in the presence of water and carbon dioxide comprising from about 5 to about 60 at.% Cu, from about 30 to about 90 at.% Mn and from about 5 to about 15 at.% Ce. 12. The catalyst according to claim 11 further comprising from about 2 to about 5 at.-% La in the form of La2O3. 13. The catalyst according to claim 11 further comprising from about 0.2 to about 5 at.% of a metal selected from the group consisting of alkali, alkaline earth, rare earth, and mixtures thereof in the form of oxides or other compounds. 14. The catalyst of claim 11, wherein up to about 10 at.% of the Cu is replaced by a metal selected from the group consisting of cobalt, iron, nickel, zinc and mixtures thereof. 15. The catalyst of claim 11, wherein a portion of the Ce is replaced by a metal selected from the group consisting of zirconium, praseodymium and mixtures thereof. 16. The catalyst of claim 11 further comprising a carrier. 17. The catalyst of claim 16 wherein the carrier is comprised of ZrO2. 18. A process for producing the mixed oxide catalyst of claim 11 for selective oxidation of CO in a hydrogen-rich gas mixture or in an oxygen-containing gas mixture in the presence of water and carbon dioxide comprising preparing a salt solution of Cu, Mn and Ce comprising, based on the total amount of Cu, Mn-and Ce-salts, from about 5 to about 60 at.-% Cu, from about 30 to 90 at.-% Mn and from about 5 to 15 at.-% Ce, preparing a precipitate by co-precipitation of said salt solution of Cu, Mn and Ce with an alkaline precipitating agent, and drying and calcining the precipitate. 19. The process of claim 18, wherein a salt of La is co-precipitated with the salts of Cu, Mn and Ce. 20. The process of claim 18, wherein the precipitating agent is selected from NaHCO3, Na2CO3 and mixtures thereof. 21. A process for producing the mixed oxide catalyst of claim 11 for selective oxidation of CO in a hydrogen-rich gas mixture or in an oxygen-containing gas mixture in the presence of water and carbon dioxide comprising preparing a carrier compound of MnO2, impregnating the carrier with a salt solution of Cu and Ce, said amounts of MnO2 and Cu-and Ce-salts being selected such that a precipitate obtained comprises, based on the total amount of Cu, Mn-and Ce-salts, from about 5 to 60 at.-% Cu, from about 30 to 90 at.-% Mn and from about 5 to 15 at.-% Ce, and drying and calcining the precipitate. 22. The process of claim 21, wherein the salt solution further comprises a salt of La. 23. A process for the production of the mixed oxide catalyst of claim 11 for selective oxidation of CO in a hydrogen-rich gas mixture or in an oxygen-containing gas mixture in the presence of water and carbon dioxide comprising preparing a carrier comprised of ZrO2, impregnating that carrier with a salt solution of Cu, Ce and Mn comprising, based on the total amount of Cu, Mn-and Ce-salts, from about 5 to 60 at.-% Cu, from about 30 to 90 at.-% Mn and from about 5 to 15 at.-% Ce, and drying and calcining the impregnated carrier. 24. The process of claim 23, wherein the carrier is further impregnated with a salt solution of La. 25. The process of claim 23, wherein the salts are fixed on the carrier by use of a precipitating agent. 26. The catalyst of claim 11, wherein the quantity of Ce is from 5 to 10 at.-% Ce.