Ceramic honeycomb structure and its production method
US-2016303500-A1 · Oct 20, 2016 · US
US9393522B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9393522-B2 |
| Application number | US-201314016795-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 3, 2013 |
| Priority date | May 29, 2008 |
| Publication date | Jul 19, 2016 |
| Grant date | Jul 19, 2016 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Provided is a particulate combustion catalyst including a carrier formed of monoclinic zirconium oxide particles, and metallic Ag or Ag oxide, which serves as a catalyst component and is supported on the carrier, wherein the amount of the catalyst component is 0.5 to 10 mass %, as reduced to metallic Ag, on the basis of the mass of the carrier, and preferably, the catalyst has a BET specific surface area of 8 to 21 m 2 /g. Also provided are a particulate filter coated with the particulate combustion catalyst; and an exhaust gas cleaning apparatus including a particulate filter coated with the particulate combustion catalyst.
Opening claim text (preview).
The invention claimed is: 1. A method for combusting an exhaust gas discharged from diesel, the method comprising: employing a particulate combustion catalyst comprising a carrier formed of monoclinic zirconium oxide particles, and a catalyst component and is supported on the carrier, wherein the catalyst component consists of metallic Ag or Ag oxide, and the amount of the catalyst component is 0.5 to 10 mass %, as reduced to metallic Ag, on the basis of the mass of the carrier, and removing soot being contained in the exhaust gas discharged from diesel through oxidation. 2. The method for combusting an exhaust gas discharged from diesel according to claim 1 , wherein the particulate combustion catalyst is produced through firing at 600 to 900° C. for 10 hours or longer. 3. The method for combusting an exhaust gas discharged from diesel according to claim 1 , wherein the catalyst particulate combustion has a BET specific surface area of 8 to 21 m 2 /g. 4. The method for combusting an exhaust gas discharged from diesel according to claim 1 , wherein the particulate combustion catalyst exhibits a combustion initiation temperature (Tig) of 300° C. or lower. 5. A method for combusting an exhaust gas discharged from diesel, the method comprising: employing catalyst comprising a carrier formed of monoclinic zirconium oxide particles, and a catalyst component and is supported on the carrier, wherein the catalyst component consists of metallic Ag or Ag oxide, and wherein the amount of the catalyst component is 1 to 9 mass %, as reduced to metallic Ag, on the basis of the mass of the carrier, and the catalyst has a BET specific surface area of 11 to 20 m 2 /g; and removing soot being contained in the exhaust gas discharged from diesel through oxidation. 6. The method for combusting an exhaust gas discharged from diesel according to claim 5 , wherein the catalyst exhibits a combustion initiation temperature (Tig) of 260° C. or lower. 7. The method for combusting an exhaust gas discharged from diesel according to claim 5 , wherein the catalyst is produced through firing at 730 to 870° C. for 10 hours or longer. 8. A method for combusting an exhaust gas discharged from diesel, the method comprising: employing a particulate filter comprising a base coated with a particulate combustion catalyst; and removing soot being contained in the exhaust gas discharged from diesel through oxidation, wherein the particulate combustion catalyst comprising a carrier formed of monoclinic zirconium oxide particles, and a catalyst component and is supported on the carrier, wherein the catalyst component consists of metallic Ag or Ag oxide, and the amount of the catalyst component is 0.5 to 10 mass %, as reduced to metallic Ag, on the basis of the mass of the carrier. 9. A method for combusting an exhaust gas discharged from diesel, the method comprising: employing a particulate filter comprising a base coated with a particulate combustion catalyst; and removing soot being contained in the exhaust gas discharged from diesel through oxidation, wherein the particulate combustion catalyst comprising a carrier formed of monoclinic zirconium oxide particles, and a catalyst component and is supported on the carrier, wherein the catalyst component consists of metallic Ag or Ag oxide, and the amount of the catalyst component is 1 to 9 mass %, as reduced to metallic Ag, on the basis of the mass of the carrier, and the catalyst has a BET specific surface area of 11 to 20 m 2 /g. 10. A method for combusting an exhaust gas discharged from diesel, the method comprising: employing an exhaust gas cleaning apparatus comprising a particulate filter coated with a particulate combustion catalyst; and removing soot being contained in the exhaust gas discharged from diesel through oxidation, wherein the particulate combustion catalyst comprising a carrier formed of monoclinic zirconium oxide particles, and a catalyst component and is supported on the carrier, wherein the catalyst component consists of metallic Ag or Ag oxide, and the amount of the catalyst component is 0.5 to 10 mass %, as reduced to metallic Ag, on the basis of the mass of the carrier. 11. A method for combusting an exhaust gas discharged from diesel, the method comprising: employing an exhaust gas cleaning apparatus comprising a particulate filter coated with a particulate combustion catalyst; and removing soot being contained in the exhaust gas discharged from diesel through oxidation, wherein the particulate combustion catalyst comprising a carrier formed of monoclinic zirconium oxide particles, and a catalyst component and is supported on the carrier, wherein the catalyst component consists of metallic Ag or Ag oxide, and the amount of the catalyst component is 1 to 9 mass %, as reduced to metallic Ag, on the basis of the mass of the carrier, and the catalyst has a BET specific surface area of 11 to 20 m 2 /g.
Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts (three-way-catalysts [TWC] B01D53/9445) · CPC title
Silver · CPC title
Other inorganic materials, e.g. ceramics · CPC title
Zirconium or hafnium; Oxides or hydroxides thereof · CPC title
with catalytic reactors · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.