Structured catalyst for oxidation for exhaust gas purification, method for producing same, automobile exhaust gas treatment device, catalytic molding, and gas purification method
US-2020114339-A1 · Apr 16, 2020 · US
US12508576B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12508576-B2 |
| Application number | US-202017636554-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 18, 2020 |
| Priority date | Aug 20, 2019 |
| Publication date | Dec 30, 2025 |
| Grant date | Dec 30, 2025 |
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.
The present invention relates to a composition comprising platinum supported on titanium oxide, the platinum particles having an average particle diameter of 50-200 nm. The composition has a surprisingly low light-off temperature for the ammonia oxidation and a high selectivity for oxidation to N2.
Opening claim text (preview).
The invention claimed is: 1 . Composition comprising platinum in the form of platinum particles supported on metal oxide A, characterized in that the platinum particles have an average particle diameter of 50-200 nm, wherein metal oxide A is titanium oxide. 2 . Composition according to claim 1 , characterized in that the platinum particles have an average particle diameter of 80-120 nm. 3 . Composition according to claim 1 , characterized in that the composition contains no further precious metal other than platinum. 4 . Composition according to claim 1 , characterized in that the titanium oxide comprises the crystalline phases anatase and rutile, and the anatase to rutile ratio is greater than 9:1. 5 . Composition according to claim 1 , characterized in that the platinum loading is 0.5-20% by weight based on the metal oxide A. 6 . Composition according to claim 1 , characterized in that the platinum loading is 3-8% by weight based on the metal oxide A. 7 . Composition according to claim 1 , characterized in that the metal oxide A contains silicon oxide, wherein the proportion of silicon oxide in the metal oxide A is 1 to 10% by weight. 8 . Composition, characterized in that it comprises a composition according to claim 1 and metal oxide B, wherein metal oxide B equals metal oxide A. 9 . Method for producing a composition according to claim 1 , characterized in that the platinum is deposited from a solution on the metal oxide A and the composition is subjected to a thermal treatment at 700° C. to 900° C. after drying. 10 . Catalyst comprising a composition according to claim 1 , characterized in that the composition is applied to a carrier substrate of length L. 11 . Catalyst according to claim 10 , characterized in that the composition is applied to a carrier substrate over at least 80% of the entire length L. 12 . Catalyst according to claim 10 , characterized in that the composition is applied to a carrier substrate over a length of 10% to 80% of the carrier substrate length L. 13 . Catalyst according to claim 10 , characterized in that the composition is applied to a carrier substrate together with another catalytically active composition that is active for SCR reaction. 14 . Catalyst according to claim 10 , characterized in that the composition and another catalytically active composition are arranged in different zones and/or layers. 15 . Catalyst according to claim 10 , characterized in that the carrier substrate is a ceramic or metallic substrate. 16 . Catalyst according to claim 10 , characterized in that the carrier substrate is a flowthrough substrate. 17 . Catalyst according to claim 16 , characterized in that the flowthrough substrate is a corrugated substrate. 18 . Catalyst according to claim 10 , characterized in that the carrier substrate is a filter substrate. 19 . Catalyst system, characterized in that it comprises a catalyst according to the invention in accordance with claim 10 . 20 . Method for reducing nitrogen oxides in exhaust gases of lean-burn internal combustion engines, wherein the exhaust gas is passed over an exhaust gas system that comprises a catalyst for the selective reduction of nitrogen oxides (SCR) and an ammonia slip catalyst (ASC) downstream of the exhaust gas stream, characterized in that the ASC is a catalyst according to the invention in accordance with claim 10 . 21 . Method according to claim 20 , characterized in that the SCR catalyst is a vanadium oxide-based catalyst or a zeolite-based catalyst of the Fe-zeolite or Cu-zeolite type.
zeolites · CPC title
for removing nitrogen oxides by NOx storage or reduction by cyclic switching between lean and rich exhaust gases (LNT, NSC, NSR) · CPC title
containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead · CPC title
combined with catalytic converters, e.g. NOx absorption/storage reduction catalysts · CPC title
of the platinum group metals · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.