초록 ▼

A diesel exhaust treatment system and method of oxidizing NO to NO 2 at low temperatures are provided. The system utilizes a platinum catalyst on a zirconia-stabilized silica support which oxidizes NO in the exhaust gas to NO 2 and uses the NO 2 in an amount sufficient to oxidize particulate trap

A diesel exhaust treatment system and method of oxidizing NO to NO 2 at low temperatures are provided. The system utilizes a platinum catalyst on a zirconia-stabilized silica support which oxidizes NO in the exhaust gas to NO 2 and uses the NO 2 in an amount sufficient to oxidize particulate trapped on a particulate filter. The catalyst is preferably pre-treated at a temperature of between about 500 to 650° C. in a NO-oxygen-nitrogen mixture to increase conversion at low temperatures. The catalyst preferably includes an additional oxide component selected from the group consisting of TiO 2 , P 2 O 5 , WO 3 , B 2 O 3 , and Al 2 O 3. or a heteropolyacid component to further increase activity at low temperatures or to decrease platinum loading at the same level of performance.

대표청구항 ▼

1. A diesel exhaust gas treatment system comprising:an oxidation catalyst positioned in an exhaust gas passage of a diesel engine for converting at least a portion of NO contained in said exhaust gas to NO 2 at a temperature between about 175° C. to 250° C., said oxidation catalyst compri

1. A diesel exhaust gas treatment system comprising:an oxidation catalyst positioned in an exhaust gas passage of a diesel engine for converting at least a portion of NO contained in said exhaust gas to NO 2 at a temperature between about 175° C. to 250° C., said oxidation catalyst comprising platinum and a support material comprising zirconia-silica, said support material having strong acid sites; anda particulate filter for receiving said exhaust gas. 2. The system of claim 1 wherein said oxidation catalyst is positioned between said exhaust passage and said particulate filter. 3. The system of claim 1 wherein said oxidation catalyst is combined with said particulate filter. 4. The system according to claim 1 further including a second catalyst positioned downstream from said particulate filter. 5. The system according to claim 4 wherein said second catalyst comprises a selective reduction catalyst. 6. The system according to claim 1 further including a NOx trap positioned downstream from said oxidation catalyst. 7. The system of claim 1 wherein said oxidation catalyst comprises from about 1 to 5 wt. % platinum on a support containing from about 3 to 20 wt. % zirconia, and the balance silica. 8. The system of claim 1 wherein said support includes one or more oxides selected from the group consisting of TiO 2 , P 2 O 5 , WO 3 , B 2 O 3 , and Al 2 O 3 . 9. The system of claim 1 wherein said support has been prepared with the addition of a heteropolyacid selected from H 3 PW 12 O 40 and H 4 SiW 12 O 40 . 10. The diesel exhaust gas treatment system of claim 1 wherein said zirconia-silica support has been formed by impregnating silica gel with a zirconium citrate ammonium complex, drying said support, and calcinating said support at 800° C. 11. A method for treating diesel exhaust gases comprising:positioning an oxidation catalyst in an exhaust gas passage of a diesel engine, said oxidation catalyst comprising platinum and a support material comprising zirconia-stabilized silica, said support material having strong acid sites;providing a particulate filter downstream of said oxidation catalyst;exposing said oxidation catalyst to diesel exhaust gas containing NO such that at least a portion of said NO contained in said exhaust gas is converted to NO 2 at a temperature between about 175° C. to 250° C.; andpassing said NO 2 through said particulate filter in an amount sufficient to oxidize particulate matter trapped on said filter. 12. The method of claim 11 wherein said oxidation catalyst comprises from about 1 to 5 wt. % platinum on a support containing from about 3 to 20 wt. % zirconia and the balance silica. 13. The method of claim 11 including pretreating said oxidation catalyst in a gas mixture containing NO, O 2 and N 2 prior to positioning said catalyst in said exhaust stream. 14. The method of claim 13 wherein said gas mixture comprises about 500 ppm of NO, about 3% by volume O 2 , and the balance N 2 . 15. The method of claim 13 wherein said pretreatment is carried out a temperature of between about 500 to 650° C. 16. The method of claim 11 including adding one or more oxides to said support prior to positioning said oxidation catalyst in said exhaust stream, said one or more oxides being selected from the group consisting of TiO 2 , P 2 O 5 , WO 3 , B 2 O 3 , and Al 2 O 3 . 17. The method of claim 11 including adding a heteropolyacid selected from H 3 PW 12 O 40 and H 4 SiW 12 O 40 to said support prior to positioning said oxidation catalyst in said exhaust stream. 18. The method of claim 11 wherein about 60% to about 96% of NO contained in said exhaust gas is converted to NO 2 . 19. The method of claim 11 further including providing a second catalyst downstream of said particulate filter and passing said exhaust gas over said second catalyst. 20. The method of claim 19 wherein said second catalyst is a selective reduction catalyst. 21. The method of claim 11 further including a NOx trap positioned downstream of said oxidation catalyst. 22. The method of claim 11 wherein said conversion of NO to NO 2 occurs at a temperature of between about 200 to 250° C. 23. The method of claim 11 wherein said oxidation of particulate occurs at a temperature less than about 250° C. 24. A method for treating diesel exhaust gases comprising:positioning an oxidation catalyst in an exhaust gas passage of a diesel engine, said oxidation catalyst comprising platinum and a support material comprising zirconia-stabilized silica, said support material having strong acid sites;providing a particulate filter in combination with said oxidation catalyst;exposing said oxidation catalyst to diesel exhaust gas containing NO such that at least a portion of said NO contained in said exhaust gas is converted to NO 2 at a temperature between about 175° C. to 250° C.; andpassing said NO 2 through said particulate filter in an amount sufficient to oxidize particulate matter trapped on said filter. 25. A diesel exhaust gas treatment system comprising:a particulate filter for receiving diesel exhaust gas from a diesel engine;an oxidation catalyst for converting at least a portion of NO contained in said diesel exhaust gas to NO 2 at a temperature between about 175° C. to 250° C., said oxidation catalyst comprising platinum and a support material comprising zirconia-silica, said support material having strong acid sites; wherein said oxidation catalyst is impregnated in said particulate filter. 26. A diesel exhaust gas treatment system comprising:a first oxidation catalyst for converting at least a portion of NO contained in said diesel exhaust gas to NO 2 at a temperature of between about 175° C. to 250° C., said oxidation catalyst comprising platinum and a support material comprising zirconia-silica, said support material having strong acid sites; anda second oxidation catalyst different from said first oxidation catalyst; wherein said first and second oxidation catalyst are positioned in combination in the exhaust gas passage of a diesel engine.