[특허]Metal oxide-coated SiC foam carriers for catalysts, and catalytic systems therefor

Centre National de la Recherche Scientifique

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Metal oxide-coated SiC foam carriers for catalysts, and catalytic systems therefor

특허상세정보
국가/구분	United States(US) Patent 등록
국제특허분류(IPC7판)	B01J-027/224 B01J-027/20 B01J-023/10
미국특허분류(USC)	502/304; 502/326; 502/302; 502/407; 502/437
출원번호	US-0101451 (1997-01-24)
우선권정보	FR-96 01181(1996-01-26)
국제출원번호	PCT/FR97/000143 (1997-01-24)
§371/§102 date	19980915 (19980915)
국제공개번호	WO97/026988 (1997-07-31)
발명자 / 주소	Prin,Marie Hervieu,Pascal
출원인 / 주소	Centre National de la Recherche Scientifique
대리인 / 주소	Dennison, Schultz & MacDonald
인용정보	피인용 횟수 : 3 인용 특허 : 13

초록

A catalyst carrier including a surface layer of oxygen-donating oxide, particularly cerine, is disclosed. A catalytic phase deposited on said carrier generally includes platinum and rhodium, thus forming a catalytic system for exhaust pipes, said catalytic phase being readily recoverable by simple leaching.

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What is claimed is: 1. A catalyst support comprising a support of SiC foam in a divided and porous state having a specific surface area of at least 5 m2/g, with a surface of SiC having thereon a superficial layer comprising an oxygen donor oxide, wherein the superficial layer resides directly on the surface of SiC without an intermediate wash coat. 2. A support according to claim 1, wherein the oxygen donor oxide is an oxide of at least one metal from group 3 of the periodic classification of the elements. 3. A support according to claim 2, wherein the oxygen donor oxide is a cerium oxide or an oxide of a mixture of rare earths. 4. A support according to claim 1, wherein the oxygen donor oxide is an oxide of at least one metal found in both group 7, 8, 9, 10 or 11 and row 5 or 6, of the periodic classification of elements. 5. A support according to claim 1, wherein the oxygen donor oxide is present in an amount of more than 1% by weight with respect to the SiC support. 6. A support according to claim 1, wherein the superficial oxygen donor oxide layer comprises a stabilizing agent for said oxide in an amount of 0.1% to 5% by weight with respect to said oxygen donor oxide. 7. A support according to claim 6, wherein said stabilizing agent is selected from the group consisting of Si, Al, Mg, Ca, Zr, La, silica, alumina, magnesia, lime, zirconia, lanthanum oxide and mixtures thereof. 8. A support according to claim 1, having a specific surface area in the range 1.5 to 4 times that of said SiC foam in its divided state. 9. A support according to claim 1, having a bimodal pore spectrum with a macroporosity range of 5 to 100 μm and a mesoporosity range of 0.007 to 0.5 μm. 10. A process for the production of a support according to of claim 1, comprising the steps of: a) preparing a solution of a precursor of the oxygen donor oxide; b) impregnating said SiC foam in its divided state with said solution; c) separating excess of said solution; and d) calcining said impregnated foam at a temperature which is at which said precursor decomposes but lower than a temperature at which said oxide sinters, to form a layer of said oxide on said SiC foam in its divided state. 11. A process according to claim 10, wherein said solution is an aqueous solution and said precursor is a cerium salt which is soluble in water. 12. A process according to claim 11, wherein said salt is a cerous nitrate. 13. A process according to claim 10, wherein the excess of said solution is separated by centrifugation. 14. A process according to claim 11, wherein the cerium oxide/SiC ratio is varied by at least one of the steps of: in step a) of the process, changing the concentration of the cerium oxide precursor in said solution between 20% by weight and the solubility limit of said precursor in said solution, and in step c) of the process, changing the degree to which said excess is separated. 15. A catalytic system comprising an active catalytic phase comprising one or more active catayltic elements, deposited on said catalyst support according to claim 1. 16. A catalytic system according to claim 15, wherein said active catalytic phase is selected from the group consisting of platinum, palladium, rhodium and mixtures thereof, to form a catalytic system for the treatment of exhaust gases. 17. A catalytic system according to claim 16, wherein said catalytic system contains platinum in the range 0.05% to 3% by weight, and rhodium in the range 0.01% to 3% by weight. 18. A catalytic system according to claim 16, containing Pt and Rh in a weight ratio in the range of 3 to 6. 19. A process for the production of said catalytic system according to claims 15, comprising the steps of: a) preparing a solution of a precursor of the oxygen donor oxide; b) impregnating said SiC foam in its divided state with said solution; c) separating excess of said solution; d) calcining said impregnated foam at a temperature which is at which said precursor decomposes but lower than a temperature at which said oxide sinters, to form a layer of said oxide on said SiC foam in its divided state; e) depositing said active phase comprising at least one active catalyst element from a precursor solution thereof; f) separating said catalytic support from excess precursor solution; g) heat treating said catalytic support on which said precursor solution has been deposited, at a temperature which is greater than that at which the precursor decomposes, to form said active catalytic phase. 20. A process according to claim 19, wherein the active elements are platinum and rhodium. 21. A process according to claim 19, wherein, in step e), said deposition is carried out by adsorption of the at least one active element in the form of anionic or cationic species in solution on said support, the surface of which has been respectively positively or negatively charged by selecting a pH for said solution which is lower or higher than the isoelectric point of the hydrate of said oxygen donor oxide. 22. A process according to claim 19, wherein the at least one active element is varied in weight content by at least one step of: changing concentrations of said precursor in the solutions and, changing the amount of separation of said excess. 23. A process for recovering the catalytic phase based on precious metals in the catalytic system of claim 15, comprising treating said catalytic system by coarse grinding, lixiviation using a hot concentrated acid, then filtering to obtain a solution of at least one catalyst metal. 24. A support according to claim 2, wherein the metal is a rare earth metal. 25. A support according to claim 4, wherein the at least one metal is selected from the group consisting of Pt, Rh and Pd. 26. A support according to claim 5, wherein the oxygen donor oxide is present in an amount of 10 to 50% by weight.

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Metal oxide-coated SiC foam carriers for catalysts, and catalytic systems therefor

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Metal oxide-coated SiC foam carriers for catalysts, and catalytic systems therefor

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