초록 ▼

Catalysts are described in which an active catalyst is disposed on a low surface area, oxide support. Methods of forming catalysts are described in which a Cr-containing metal is oxidized to form a chromium oxide layer and an active catalyst is applied directly on the chromium oxide layer. Methods o

Catalysts are described in which an active catalyst is disposed on a low surface area, oxide support. Methods of forming catalysts are described in which a Cr-containing metal is oxidized to form a chromium oxide layer and an active catalyst is applied directly on the chromium oxide layer. Methods of making new catalysts are described in which the surface is sonicated prior to depositing the catalyst. Catalyst systems and methods of oxidation are also described. The inventive systems, catalysts and methods are, in some instances, characterized by surprisingly superior results.

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We claim: 1. A method of combusting a carbon-containing compound, comprising: providing a gas mixture comprising CO or a hydrocarbon and an oxidant; and passing the gas mixture through a reaction chamber at a GHSV of at least 100,000 h-1 and a temperature of 400 to 1100�� C.; wherein the reaction c

We claim: 1. A method of combusting a carbon-containing compound, comprising: providing a gas mixture comprising CO or a hydrocarbon and an oxidant; and passing the gas mixture through a reaction chamber at a GHSV of at least 100,000 h-1 and a temperature of 400 to 1100�� C.; wherein the reaction chamber has an internal dimension of 1 cm or less; wherein a combustion catalyst is disposed in the reaction chamber; and wherein at least 20% of the CO or the hydrocarbon in the gas mixture is converted to CO2; and wherein the combustion catalyst comprises a metal substrate; a chromium-containing oxide layer in direct contact with the metal substrate; an active catalyst on the chromium-containing oxide layer; wherein the combination of the metal substrate, the active catalyst and the chromium-containing oxide layer define a catalyst, and wherein the catalyst has a low surface area of no more than 0.5 m2/g and no more than 1 m2/inch2. 2. The method of claim 1 wherein the gas mixture further comprises H2. 3. The method of claim 1 wherein the gas mixture has a C:O atomic ratio of 1:1 or less, and wherein pressure drop through the reaction chamber is 20 psi or less. 4. A method of making a product from an endothermic reaction comprising passing an endothermic reaction composition into a reaction chamber that is adjacent to the reaction channel of claim 1 in which fuel is oxidized according to the method of claim 1, and using heat generated from the oxidizing of the fuel to add heat into the endothermic reaction. 5. The method of claim 1 wherein the reaction chamber and combustion catalyst define a catalyst system, and further wherein the catalyst system is characterizable by a combustion activity selected from the group consisting of: when a gas mixture containing 9 volume % CH4, 1.9 vol. % O2, and 89 vol. % N2 is passed through the reaction chamber at a GHSV of 1.6��106 h-1 and a temperature in the reaction chamber of 835�� C., there is a CH4 conversion of at least 9% and an O2 conversion of at least 50%; when a gas mixture containing 1.0 volume % CH4, 4.4 vol. % O2, 1.2 vol. % H2, 2.0 vol. % CO, and 91.4 vol. % N2 is passed through the reaction chamber at a GHSV of 1.1��106 h-1 and a temperature in the reaction chamber of 710�� C., there is a CO conversion of at least 80%; and when a gas mixture containing 1.0 volume % CH4, 4.4 vol. % O2, 1.2 vol. % H2, 2.0 vol. % CO, and 91.4 vol. % N2 is passed through the reaction chamber at a GHSV of 1.1��106 h-1 and a temperature in the reaction chamber of 910�� C., there is a CO conversion of at least 90%. 6. A method of oxidizing a carbon-containing compound, comprising: providing a gas mixture comprising CO or a hydrocarbon and an oxidant; and passing the gases through a reaction chamber at a GHSV of at least 10,000 h-1 and a temperature of 400 to 1100�� C.; wherein the reaction chamber has an internal dimension of 1 cm or less; wherein a combustion catalyst is disposed in the reaction chamber; wherein pressure drop through the reaction chamber is 20 psi or less, or wherein the pressure drop through the reaction chamber is 3.0 psi per inch or less; and wherein at least 20% of the hydrocarbon in the gas mixture is converted to CO2; and wherein the combustion catalyst has a low surface area of no more than 0.5 m2/g or no more than 1 m2/inch2. 7. The method of claim 6 wherein the combustion catalyst has a surface area of less than 0.2 m2/inch2 of the geometric surface area. 8. The method of claim 6 wherein the reaction chamber comprises a bulk flow path. 9. A method of making a product from an endothermic reaction comprising passing an endothermic reaction composition into a reaction chamber that is adjacent to the reaction chamber of claim 7 in which fuel is oxidized according to the method of claim 6, and using heat generated from the oxidizing of the fuel to add heat into the endothermic reaction. 10. The method of claim 9 wherein the reaction chamber containing the endothermic reaction composition is separated by a reaction wall from the reaction chamber of claim 7; and wherein the reaction wall has a thickness of 1 mm or less. 11. The method of claim 6 comprising passing the gas mixture through the reaction chamber at a GHSV of at least 100,000 h-1 and a temperature of 600 to 1000�� C.; and wherein at least 50% of the hydrocarbon in the gas mixture is converted to CO2. 12. The method of claim 6 wherein the oxidant enters the reaction chamber through holes along the length of the reaction chamber. 13. The method of claim 6 wherein the reaction chamber comprises a reaction chamber wall contains greater than 40% Ni. 14. The method of claim 6 wherein the combustion catalyst comprises Pt. 15. The method of claim 14 wherein the reaction chamber has a length of at least 1 cm. 16. The method of claim 15 wherein the reaction chamber has a cross-sectional area of 100 mm2 or less. 17. The method of claim 15 wherein the reaction chamber has at least one dimension of 2 mm or less. 18. The method of claim 6 wherein the at least one reaction chamber wall comprises a chromium-containing metal substrate; wherein a chromium-containing oxide layer is in direct contact with the metal substrate; an active catalyst is disposed on the chromium-containing oxide layer; wherein the combination of the metal substrate, the active catalyst and the chromium-containing oxide layer define the combustion catalyst. 19. The method of claim 18 wherein the chromium-containing oxide layer comprises at least 50% chromium oxide. 20. The method of claim 18 wherein the metal substrate contains less than 5% of aluminum plus zirconium. 21. The method of claim 18 wherein the chromium-containing oxide layer comprises 80 to 100% chromium oxide. 22. The method of claim 18 wherein the chromium-containing oxide layer has a surface that has a Ni:Cr atomic ratio of 0.05 or less.