Precipitated and calcined composition based on zirconium oxide and cerium oxide
US-2015375203-A1 · Dec 31, 2015 · US
US10179324B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10179324-B2 |
| Application number | US-201615176405-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 8, 2016 |
| Priority date | Apr 4, 2014 |
| Publication date | Jan 15, 2019 |
| Grant date | Jan 15, 2019 |
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 field of control of nitrogen oxide pollution, and involves a high-efficient catalyst for denitration at low temperature and preparation method thereof, which comprises the steps: (1) preparing aqueous solution of cerium nitrate; (2) soaking mesoporous silica materials SBA-15 with aqueous solution from step (1), after stirring, filtrating, washing and drying; (3) calcining materials from step (2) to obtain evenly dispersed CeO 2 -SBA-15 materials; (4) preparing ethanol solution of manganese nitrate; (5) soaking CeO 2 -SBA-15 materials from step (3) with ethanol solution of manganese nitrate from step (4) and volatilizing ethanol, washing and drying; (6) calcining materials from step (5) to obtain evenly distributed Mn x O y /CeO 2 -SBA-15 catalyst for denitration; The preparation method has simple process with lower cost, and the obtained Mn x O y /CeO 2 -SBA-15 catalyst has uniform and ordered pores, large specific area, narrow pore size distribution, well dispersity of catalytic components, high catalytic activity, better effect of denitration at low temperature range and wider temperature range available for denitration.
Opening claim text (preview).
What is claimed: 1. A method for preparing catalyst for denitration, wherein the method comprises the following steps: (a) preparing an aqueous solution of cerium nitrate; (b) soaking mesoporous silica materials SBA-15 with the aqueous solution of cerium nitrate obtained from step (a), then stirring, filtrating, washing and drying; (c) calcining the materials obtained from step (b) to obtain CeO 2 -SBA-15 materials; (d) preparing an ethanol solution of manganese nitrate; (e) soaking the CeO 2 -SBA-15 materials from step (c) with the ethanol solution of manganese nitrate from step (d), then volatilizing ethanol, washing and drying; and (f) calcining the materials obtained from step (e) to obtain Mn x O y /CeO 2 -SBA-15 catalyst for denitration. 2. The method according to claim 1 , wherein in step (a) the concentration of the aqueous solution of cerium nitrateis 0.1 mol/L to 1 mol/L. 3. The method according to claim 1 , wherein in step (b) dosage of mesoporous silica materials SBA-15 is 10 g/L to 40 g/L. 4. The method according to claim 1 , wherein in step (b) soaking time is 4 to 8 hours. 5. The method according to claim 1 , wherein in step (c) calcining temperature is 300° C. to 500° C. and calcining time is 4 hours to 8 hours. 6. The method according to claim 1 , wherein in step (d) a mass of manganese in the ethanol solution of manganese nitrate accounts for 10% to 30% of dosage of the CeO 2 -SBA-15 materials. 7. The method according to claim 1 , wherein in step (e) soaking time is 1 hour to 3 hours. 8. The method according to claim 1 , wherein in step (f) calcining temperature is 300° C. to 500° C. and calcining time is 4 hours to 8 hours. 9. The method according to claim 1 , wherein and Mn x O y is MnO 2 and Mn 2 O 3 . 10. The method according to claim 1 , wherein pores of the catalyst have two-dimensional hexagonal structures, and sizes of the pores range from 6 nm to 7 nm, specific areas of the pores range from 300 m 2/g to 500 m 2/g, and volumes of the pores range from 0.3 cm 3/g to 0.5 cm 3/g.
Operations & Transport · mapped topic
Silica · CPC title
Processes characterised by a specific catalyst · CPC title
the impregnation liquid containing organic compounds · CPC title
Silicon · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.