Zeolite-based SCR catalysts and their use in diesel engine emission treatment
US-9403156-B2 · Aug 2, 2016 · US
US2018057364A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2018057364-A1 |
| Application number | US-201715686235-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 25, 2017 |
| Priority date | Aug 29, 2016 |
| Publication date | Mar 1, 2018 |
| 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.
A process of producing a zeotype material having a zeolite-type framework. The process includes providing a zeolite having a framework, dealuminating the zeolite to remove aluminum atoms therefrom to produce a dealuminated framework comprising a plurality of vacancy sites, contacting the dealuminated framework with dichloromethane and a precursor comprising heteroatoms, and then heating the dealuminated framework, the dichloromethane, and the precursor under reflux conditions to incorporate the heteroatoms into at least some of the plurality of vacancy sites in the dealuminated framework to produce a zeotype material having a zeolite-type framework comprising the heteroatoms. In addition, a process is provided for producing a stannosilicate comprising a zeolite-type framework comprising Sn heteroatoms incorporated therein which form Sn sites in the zeolite-type framework each having an open configuration or a closed configuration. This process includes controlling relative amounts of Sn sites having open and closed configurations in the stannosilicate.
Opening claim text (preview).
1 . A process comprising: providing a zeolite having a framework; dealuminating the zeolite to remove aluminum atoms therefrom to produce a dealuminated framework comprising a plurality of vacancy sites; contacting the dealuminated framework with a polar aprotic solvent and a precursor comprising heteroatoms; and then heating the dealuminated framework, the solvent, and the precursor under reflux conditions to incorporate the heteroatoms into at least some of the plurality of vacancy sites in the dealuminated framework to produce a zeotype material having a zeolite-type framework comprising the heteroatoms. 2 . The process of claim 1 , wherein the solvent is dichloromethane. 3 . The process of claim 1 , wherein the heteroatoms are Sn or Ti. 4 . The process of claim 1 , wherein the framework of the zeolite has a Beta topology. 5 . The process of claim 1 , wherein the heteroatoms are incorporated into more than ninety percent of the plurality of vacancy sites in the dealuminated framework during the heating step. 6 . The process of claim 1 , wherein each of the plurality of vacancies that incorporates one of the heteroatoms is a heteroatom site having an open configuration or a closed configuration, and the process further comprising controlling relative amounts of heteroatoms sites having open and closed configurations in the zeotype material. 7 . The process of claim 6 , wherein the controlling step includes controlling a fraction of the vacancy sites to which the heteroatoms are incorporated into during the heating step in order to control the relative amounts of heteroatoms sites having open and closed configurations. 8 . The process of claim 6 , further comprising using the zeotype material as a catalyst in a reaction in which the overall number of heteroatom sites having an open or closed configuration affects the catalytic behavior. 9 . The process of claim 1 , controlling a fraction of the vacancy sites to which the heteroatoms are incorporated into during the heating step in order to control a desired Si-to-metal atom ratio of the zeotype material. 10 . The process of claim 1 , wherein the dealuminating step includes contacting the zeolite with nitric acid. 11 . The process of claim 1 , further comprising synthesizing the zeolite in a fluoride media to decrease the density of the vacancy sites in the zeotype material. 12 . The process of claim 1 , further comprising performing isomerization of glucose-to-fructose in the presence of the zeotype material. 13 . The process of claim 12 , further comprising controlling the heteroatom content in the zeotype material in order to improve a rate of isomerization. 14 . The process of claim 13 , wherein the heteroatom content is controlled by synthesizing the zeolite in a fluoride media to decrease the density of the vacancy sites in the zeotype material. 15 . The zeotype material produced by the process of claim 1 . 16 . A process of producing a stannosilicate comprising a zeolite-type framework comprising Sn heteroatoms incorporated therein, the Sn heteroatoms forming Sn sites in the zeolite-type framework each having an open configuration or a closed configuration, the process comprising: controlling relative amounts of Sn sites having open and closed configurations in the stannosilicate. 17 . The process of claim 16 , further comprising using the stannosilicate as a catalyst in a reaction in which the overall number of heteroatom sites having an open or closed configuration affects the catalytic behavior. 18 . The process of claim 16 , further comprising performing isomerization of glucose-to-fructose in the presence of the stannosilicate and controlling the heteroatom content in the stannosilicate in order to improve a rate of isomerization. 19 . The process of claim 16 , further comprising: dealuminating a zeolite to remove aluminum atoms therefrom to produce a zeolite-type framework comprising a plurality of vacancy sites; and then incorporating Sn atoms into at least some of the plurality of vacancy sites in the zeolite-type framework to produce the stannosilicate; wherein the controlling step includes controlling a fraction of the vacancy sites to which the heteroatoms are incorporated into during the heating step in order to control a desired Si-to-metal atom ratio of the stannosilicate. 20 . The stannosilicate produced by the process of claim 16 .
containing metallic elements added to the zeolite · CPC title
Germanosilicates; Aluminogermanosilicates (B01J29/005 takes precedence) · CPC title
Silicates, aluminosilicates or borosilicates of titanium, zirconium or hafnium {(B01J29/005 takes precedence)} · CPC title
Gallosilicates; Aluminogallosilicates; Galloborosilicates {(B01J29/005 takes precedence)} · CPC title
Zeolite Beta · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.