Catalytically active particle filter having a high degree of filtering efficiency
US-2024017213-A1 · Jan 18, 2024 · US
US10549265B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10549265-B2 |
| Application number | US-201514749222-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 24, 2015 |
| Priority date | Jun 27, 2014 |
| Publication date | Feb 4, 2020 |
| Grant date | Feb 4, 2020 |
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.
A highly effective catalyst for the preparation of diethyl oxalate using carbon monoxide using Pd/α-Al 2 O 3 and CeO 2 as a promoter. High conversion rates with greatly extended catalyst life is achieved with the CeO 2 -enhanced Pd catalysts. The catalysts can be used for the production of high-value diethyl oxalate, and eventually ethylene glycol, from coal-derived syngas.
Opening claim text (preview).
We claim: 1. A highly effective catalyst for the preparation of diethyl oxalate using carbon monoxide, comprising: an active component; a carrier; and a promoter agent, wherein: the active component is palladium present in the form of particles and the particles have an average surface area within the range of 2 m 2 /g and 12 m 2 /g; the carrier is α-alumina: the promoter agent is CeO 2 the loading of CeO 2 within 0.15 and 0.25 percent by weight; and the catalyst demonstrates a conversion rate of at least about 62 percent. 2. The catalyst of claim 1 , wherein the loading of active component is within the range of 0.1 and 1 percent by weight. 3. The catalyst of claim 2 , wherein the loading of CeO 2 is 0.2 percent by weight. 4. The catalyst of claim 1 , wherein the active component particles have an average size within the range of 2 and 80 nm and an average surface area within the range of 3 m 2 /g and 8 m 2 /g. 5. The catalyst of claim 1 wherein the carbon monoxide is from coal-derived syngas. 6. A method of improving the conversion rate of carbon monoxide to diethyl oxalate by at least fifty percent by catalysts comprising: an active component; a carrier; and a promoter agent, wherein: the active component is palladium present in the form of particles with an average surface area within the range of 3 m 2 /g and 8 m 2 /g; the carrier is α-alumina; and the promoter agent is CeO 2 , the loading of CeO 2 within 0.07 and 0.6 percent by weight. 7. The method of claim 6 , wherein the active component is present at about 0.8 to 0.9 percent by weight. 8. The method of claim 7 , wherein the active component particles have a size of between about 9 and 17 nm. 9. The method of claim 8 , wherein the carbon monoxide is from coal derived syngas. 10. The method of claim 4 , wherein the active component particles have a size of between about 9 and 17 nm. 11. The method of claim 10 , wherein the active component is present between about 0.7 and 1 percent by weight. 12. The method of claim 11 , wherein the active component is present at about 0.8 percent by weight and the promoter is present at about 0.2 percent by weight. 13. A method for producing diethyl oxalate comprising: providing carbon monoxide; providing ethyl nitrite; providing a catalyst, the catalyst comprising: a palladium active agent, wherein: the palladium is present in the form of particles; the particles have an average surface area between 2 m 2 /g; and 12 m 2 /g and the palladium loading is between 0.8 and 0.9% wt.; a CeO 2 promoter, the CeO 2 loading being between 0.15 and 0.25% wt.; and an α-alumina carrier; and reacting the carbon monoxide and ethyl nitrite in the presence of the catalyst, wherein the reaction has a carbon monoxide conversion rate greater than about 62% and an ethyl nitrite conversion rate of about 92%.
by reaction with carbon monoxide or formates (C07C67/02, C07C67/03, C07C67/10 take precedence) · CPC title
with rare earths or actinides · CPC title
Operations & Transport · mapped topic
Operations & Transport · mapped topic
Operations & Transport · mapped topic
Related publications grouped by family.
Answers are generated from the same data shown on this page.