Methods to produce molecular sieves with LTA topology and compositions derived therefrom
US-9821297-B2 · Nov 21, 2017 · US
US2016288108A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016288108-A1 |
| Application number | US-201415035505-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 6, 2014 |
| Priority date | Nov 22, 2013 |
| Publication date | Oct 6, 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.
In an embodiment, a method for making a catalyst, comprises: forming a mixture comprising a germanium source, an alkali metal source, an aluminum source, and a silica source, wherein the mixture has a pH; adjusting the pH of the mixture to a value of greater than or equal to 9.5; crystallizing and calcining the mixture to form a zeolite; depositing platinum on the zeolite; and calcining the zeolite to form the final catalyst. The final catalyst is non-acidic and has an aluminum content of less than or equal to 0.75 wt % based on the total weight of the final catalyst excluding any binder and extrusion aide and a Si:Al2 mole ratio of greater than or equal to 125.
Opening claim text (preview).
I/We claim: 1 . A method for making a catalyst, comprising: forming a mixture comprising a germanium source, an alkali metal source, an aluminum source, and a silica source, wherein the mixture has a pH; adjusting the pH of the mixture to a value of greater than or equal to 9.5; crystallizing and calcining the mixture to form a zeolite; depositing platinum on the zeolite; and calcining the zeolite to form the final catalyst; wherein the final catalyst is non-acidic and has an aluminum content of less than or equal to 0.75 wt % based on the total weight of the final catalyst excluding any binder or extrusion aide, and a final Si:Al 2 mole ratio of greater than or equal to 125. 2 . The method of claim 1 , wherein the forming of the mixture comprises: forming a first aqueous solution, wherein the first solution comprises the germanium source and the alkali metal source; forming a second aqueous solution, wherein the second solution comprises the aluminum source; combining the first and second aqueous solutions to form a combined solution; and adding the silica source to the combined solution to form the mixture. 3 . The method of claim 1 , wherein the mixture has a mixture Si:Al 2 mole ratio of 175 to 290, a mixture Si:Ge mole ratio of 5 to 100, and a mixture Na:Al mole ratio of 10 to 60. 4 . The method of claim 1 , wherein the zeolite is a ZSM-5 zeolite. 5 . The method of claim 1 , wherein the final catalyst has one or both of a final Si:Ge mole ratio of 40 to 400 and a final Na:Al mole ratio of 0.9 to 2.5. 6 . The method of claim 1 , wherein the final catalyst comprises one or more of a Ge content of 0.1 to 3 wt %, an Na content of 0.5 to 2 wt %, and a Pt content of 0.05 to 3 wt %, wherein the wt % values are based on the total weight of the final catalyst excluding any binder and extrusion aide. 7 . The method of claim 1 , wherein the method does not include an ion-exchange step with an alkali metal. 8 . The method of claim 1 , wherein the final catalyst is free of cesium. 9 . The method of claim 1 , wherein the alkali metal source comprises at least one of a sodium source and a potassium source. 10 . The method of claim 1 , wherein the alkali metal source comprises at least one of NaOH and NaCl. 11 . The method of claim 1 , wherein the pH is 9.5 to 12.5. 12 . A catalyst comprising: a zeolite comprising Si, Al, and Ge in the framework with Pt deposited thereon; wherein the catalyst has an Si:Al 2 mole ratio of greater than or equal to 125, an Si:Ge mole ratio of 40 to 400, and an Na:Al mole ratio of 0.9 to 2.5, wherein the catalyst has an aluminum content of less than or equal to 0.75 wt %, wherein the catalyst is non-acidic. 13 . The catalyst of claim 12 , wherein the Ge is present in an amount of 0.3 to 3 wt %, and/or the Na is present in an amount of 0.5 to 2 wt % and/or the Pt is present in an amount of 0.05 to 3 wt %, wherein the wt % values are based on the total weight of the final catalyst excluding any binder and extrusion aide. 14 . A method for the aromatization of hydrocarbons comprising: contacting an alkane containing 6 to 12 carbon atoms per molecule with a catalyst comprising: a zeolite comprising Si, Al, and Ge in the framework with Pt deposited thereon; wherein the catalyst has an Si:Al 2 mole ratio of greater than or equal to 125, an Si:Ge mole ratio of 40 to 400, and an Na:Al mole ratio of 0.9 to 2.5, wherein the catalyst has an aluminum content of less than or equal to 0.75 wt % excluding any binder and extrusion aide. 15 . The method of claim 14 , wherein the Ge is present in an amount of 0.3 to 3 wt %, and/or the Na is present in an amount of 0.5 to 2 wt % and/or the Pt is present in an amount of 0.05 to 3 wt %, wherein the wt % values are based on the total weight of the final catalyst excluding any binder and extrusion aide. 16 . The method of claim 1 , wherein the final catalyst has a Ge content of 0.1 to 3 wt % based on the total weight of the final catalyst excluding any binder and extrusion aide. 17 . The method of claim 1 , wherein the final catalyst has a Ge content of 0.4 to 1.5 wt % based on the total weight of the final catalyst excluding any binder and extrusion aide. 18 . The method of claim 1 , wherein the final catalyst comprises Al in an amount of 0.45 to 0.7 wt % based on the total weight of the final catalyst excluding any binder and extrusion aide. 19 . The method of claim 1 , wherein the final catalyst has a Ge content of 0.1 to 3 wt %, an Na content of 0.5 to 2 wt %, and a Pt content of 0.05 to 3 wt %, wherein the wt % values are based on the total weight of the final catalyst excluding any binder and extrusion aide. 20 . The method of claim 1 , wherein the final catalyst has a final Si:Ge mole ratio of 40 to 400 and a final Na:Al mole ratio of 0.9 to 2.5.
by condensation of hydrocarbons with partial elimination of hydrogen · CPC title
Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title
Noble metals · CPC title
Noble metals · CPC title
containing platinum group metals or compounds thereof · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.