Catalyst with improved activity/selectivity for light naphtha aromatization

US10207255B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10207255-B2
Application numberUS-201415035505-A
CountryUS
Kind codeB2
Filing dateNov 6, 2014
Priority dateNov 22, 2013
Publication dateFeb 19, 2019
Grant dateFeb 19, 2019

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

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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.

First claim

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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 9.5 to less than 13; crystallizing and calcining the mixture to form a zeolite; a medium pore zeolite having an average pore size of 5 to 8 Å; 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 125 to 211; 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. 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 Ge content is 0.4 to 2.5 wt %, or wherein the final catalyst has an Na content of 0.5 to 2 wt %, or wherein the final catalyst has 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. 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. 13. 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. 14. The method of claim 1 , wherein the Ge content is 0.4 to 2.5 wt %, wherein the final catalyst has an Na content of 0.5 to 2 wt %, and wherein the final catalyst has 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. 15. The method of claim 1 , wherein the final Si:Al 2 mole ratio is 125 to 200.

Assignees

Inventors

Classifications

  • containing crystalline alumino-silicates, e.g. molecular sieves · CPC title

  • Platinum · CPC title

  • containing platinum group metals or compounds thereof · CPC title

  • by condensation of hydrocarbons with partial elimination of hydrogen · CPC title

  • of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11 · CPC title

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What does patent US10207255B2 cover?
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 zeo…
Who is the assignee on this patent?
Saudi Basic Ind Corp
What technology area does this patent fall under?
Primary CPC classification B01J29/047. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Feb 19 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 6 related publications on this page (citations in our corpus or others sharing the same primary CPC).