초록 ▼

The present invention includes a catalyst having a layered structure with, (1) a porous support, (2) a buffer layer, (3) an interfacial layer, and optionally (4) a catalyst layer. The invention also provides a process in which a reactant is converted to a product by passing through a reaction chambe

The present invention includes a catalyst having a layered structure with, (1) a porous support, (2) a buffer layer, (3) an interfacial layer, and optionally (4) a catalyst layer. The invention also provides a process in which a reactant is converted to a product by passing through a reaction chamber containing the catalyst.

대표청구항 ▼

1. A catalyst comprising a porous metal support, a buffer layer, an interfacial layer, and a catalytically active layer on the surface; wherein the porous metal support has an average pore size of from 1 μm to 1000 μm; wherein the porous metal support is selected from the group consistin

1. A catalyst comprising a porous metal support, a buffer layer, an interfacial layer, and a catalytically active layer on the surface; wherein the porous metal support has an average pore size of from 1 μm to 1000 μm; wherein the porous metal support is selected from the group consisting of foam, felt, and wad;wherein the buffer layer is disposed between the porous support and the interfacial layer, and the interfacial layer is disposed between the catalytically active layer and the buffer layer;and wherein the buffer layer comprises a metal oxide. 2. The catalyst of claim 1 wherein the catalyst possesses thermal cycling stability such that, if exposed to 3 thermal cycles in air, the catalyst exhibits less than 2% flaking. 3. The catalyst of claim 1 wherein the catalyst possesses oxidation resistance such that, if it is heated at 580° C. in air for 2500 minutes the catalyst increases in weight by less than 5%. 4. The catalyst of claim 1 wherein the catalyst possesses oxidation resistance such that, if it is heated at 750° C. in air for 1500 minutes, the catalyst increases in weight by less than 0.5%. 5. The catalyst of claim 1 wherein the porous support is a metal and the catalytically active layer is distributed on surfaces throughout catalyst such that reactants passing through the catalyst can react anywhere along the passage through the catalyst. 6. The catalyst of claim 1 wherein said buffer layer is nonporous. 7. The catalyst of claim 1 wherein the interfacial layer has a BET surface area of at least 1 m 2 /g. 8. The catalyst of claim 1 wherein the interfacial layer comprises a material selected from the group consisting of nitrides, carbides, sulfides, halides and carbon. 9. The catalyst of claim 1 having oxidation resistance such that, if it is heated at 750° C. in air for 1500 minutes the catalyst increases in weight by less than 0.5%. 10. The catalyst of claim 1 wherein the porous support comprises a foam, felt, wad or combination thereof. 11. The catalyst of claim 1 wherein the porous metal support has an average pore size of from 1 to 500 μm. 12. The catalyst of claim 1 wherein the interfacial layer has a thickness that ranges from 1 to 50 μm. 13. A catalyst comprising a porous metal support, a buffer layer, and an interfacial layer;wherein the porous metal support has an average pore size of from 1 μm to 1000 μm; wherein the porous metal support is selected from the group consisting of foam, felt, and wad; wherein the buffer layer is disposed between the porous support and the interfacial layer; and wherein the catalyst possesses thermal cycling stability such that, if exposed to 3 thermal cycles in air, the catalyst exhibits less than 2% flaking;and wherein the buffer layer comprises a metal oxide. 14. The catalyst of claim 13 wherein the catalyst possesses oxidation resistance such that, if it is heated at 580° C. in air for 2500 minutes the catalyst increases in weight by less than 5%. 15. The catalyst of claim 14 wherein the buffer layer is between 0.05 and 10 μm thick. 16. The catalyst of claim 13 wherein the catalyst is a monolith having a width of 0.1 mm to about 2 cm and a thickness of less than 1 cm. 17. The catalyst of claim 13 wherein the porous support has a porosity in the range of 70 to 98%. 18. The catalyst of claim 13 wherein the porous support comprises a foam, felt, wad or combination thereof. 19. The catalyst of claim 13 wherein the porous metal support has an average pore size of from 1 to 500 μm. 20. The catalyst of claim 13 wherein the interfacial layer has a thickness that ranges from 1 to 50 μm. 21. The catalyst of claim 13 wherein the porous metal support comprises a foam, felt, wad or combination thereof. 22. A method of making a catalyst comprising the steps of:selecting a porous support selected from the group consisting of honeycomb, foam, felt, and wad;vapor depositing a buffer layer on said porous support;wh erein the buffer layer comprises Al 2 O 3 , TiO 2 , SiO 2 , and ZrO 2 or combinations thereof;depositing an interfacial layer on said buffer layer; and depositing a catalytically active material on said inter facial layer. 23. The method of claim 22 wherein said buffer layer is titania. 24. The process of claim 22 wherein a catalytically active material is simultaneously deposited with the interfacial layer. 25. The method of claim 22 wherein the interfacial layer is deposited from solution. 26. The method of claim 22 wherein the step of vapor depositing comprises chemical vapor depositing. 27. The method of claim 26 wherein the support comprises a metal foam and wherein the chemical vapor deposition is conducted in a temperature range of 250 to 800° C. 28. The method of claim 26 wherein a precursor for the chemical vapor deposition is selected from the group consisting of: organometallic compounds, halides, carbonyls, acetonates, and acetates. 29. The method of claim 22 wherein the step of vapor depositing a buffer layer comprises the steps of: vapor depositing a TiO 2 layer; and vapor depositing a dense alumina layer over the TiO 2 layer; and wherein the step of depositing an interfacial layer comprises depositing a less dense, high surface area alumina layer over the dense alumina layer. 30. The method of claim 22 wherein the porous support comprises a metal foam and the catalyst has a surface area of greater than 2.0 g per cubic centimeter. 31. The method of claim 22 wherein the porous support comprises a metal foam and the metal foam is etched prior to vapor depositing the buffer layer. 32. The method of claim 22, wherein the support comprises a structure selected from the group consisting of honeycomb, foam, felt, and wad; and the catalyst possesses oxidation resistance such that, if it heated at 750° C. in air for 1500 minutes the catalyst increases in weight by less than 0.5%. 33. The method of claim 22 wherein the porous support has a porosity in the range of 70 to 98%. 34. The method of claim 22 wherein the porous support comprises a foam, felt, wad, or combination thereof. 35. The method of claim 34 wherein the step of vapor depositing comprises chemical vapor depositing. 36. The method of claim 22 wherein the porous support is a porous metal support and a catalytically active material is simultaneously deposited with the interfacial layer.