Precipitated and calcined composition based on zirconium oxide and cerium oxide
US-2015375203-A1 · Dec 31, 2015 · US
US2016332118A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016332118-A1 |
| Application number | US-201515112986-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 21, 2015 |
| Priority date | Jan 21, 2014 |
| Publication date | Nov 17, 2016 |
| Grant date | — |
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.
Disclosed is a cheap and efficient non noble metal based catalyst for the oxidation of diesel or hydrocarbons, its synthesis and its application for diesel oxidation at low temperature. The catalyst comprises a mixed oxide of manganese and cerium, or manganese, cerium and zirconium. The catalyst has improved water and sulphur tolerance.
Opening claim text (preview).
We claim: 1 . A diesel oxidation catalyst comprising a mixed oxide of A and B, wherein A is Mn and B is Ce or a mixture of Ce and Zr, said catalyst comprises A in the range of 1-60% by weight of the catalyst and B in the range of 40-99% by weight of the catalyst, wherein the catalyst is devoid of noble-metal and is having Mn particle size of 50-70% particles <1 nm; said catalyst is prepared by a process comprising: a) mixing salt of A and salt of B in water or a mixture of water and an acid to obtain a solution; b) adjusting pH of the solution obtained in step (a) in the range of 7-12; c) heat treating the solution of (b) to a temperature in the range of 100-200° C. for 15-120 minutes to obtain a reaction mixture; di) cooling and filtering the reaction mixture to obtain a residue; and e) washing and calcinating the residue obtained in step (d) at a temperature in the range of 300-800° C. for 1-5 hours to obtain the diesel oxidation catalyst. 2 . The catalyst according to claim 1 , wherein the BET surface area of the catalysts is 100-160 m 2 /g with a pore volume of 0.200 to 0.381 cm 3 /g. 3 . The catalyst according to claim 1 , wherein the salt of A and B is selected from the group consisting of nitrate, acetate. 4 . The catalyst according to claim 1 , wherein the acid used is nitric acid. 5 . The catalyst according to claim 1 is useful in oxidation of hydrocarbons and carbon monoxide from diesel engine exhaust. 6 . The catalyst according to claim 1 , wherein the catalyst oxidizes carbon monoxide (50% conversion) at a temperature in the range of 30 to 250° C. 7 . The catalyst according to claim 1 , wherein the catalyst exhibits sulphur tolerance with oxidation of carbon monooxide (50% conversion) at a temperature in the range of 200 to 300° C. 8 . The catalyst according to claim 1 , wherein the catalyst exhibits water tolerance with oxidation of carbon monooxide (50% conversion) at a temperature in the range of 220 to 300° C.
Simultaneously removing carbon monoxide, hydrocarbons or carbon making use of oxidation catalysts (three-way-catalysts [TWC] B01D53/9445) · CPC title
Controlling the catalytic process · CPC title
Diesel engines and lean burn gasoline engines · CPC title
Specific surface · CPC title
Porosity · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.