Catalyst supports and catalyst systems and methods

US11577230B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11577230-B2
Application numberUS-202217815441-A
CountryUS
Kind codeB2
Filing dateJul 27, 2022
Priority dateAug 12, 2020
Publication dateFeb 14, 2023
Grant dateFeb 14, 2023

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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

Official abstract text for this publication.

Provided herein are catalyst supports, catalyst systems, and methods for making catalyst supports, catalyst systems, and performing chemical reactions with the catalyst systems. The catalyst supports include a zeolite and a binder including non-sodium counterions, such as ammonium counterions and/or potassium counterions. The catalyst systems include the catalyst supports and a catalytic material. The catalyst systems may be used to perform chemical reactions, including reactions of one or more hydrocarbons.

First claim

Opening claim text (preview).

I claim: 1. A catalyst system comprising: a dried and calcined catalyst support comprising a) one or more Group VIII metals and one or more halides, and b) a dimensioned mixture comprising a zeolite and a binder comprising a colloidal silica including potassium counterions, ammonium counterions, or a combination thereof, and substantially no sodium counterions. 2. The catalyst system of claim 1 , wherein the dimensioned mixture further comprises an extrusion aid. 3. The catalyst system of claim 2 , wherein the extrusion aid comprises a cellulose ether. 4. The catalyst system of claim 3 , wherein the cellulose ether comprises ethylcellulose, carboxymethylcellulose, ethylhydroxyethylcellulose, hydroxyethylcellulose, hydroxypropylcellulose, methylhydroxyethylcellulose, methylhydroxypropylcellulose, or a combination thereof. 5. The catalyst system of claim 1 , wherein the dimensioned mixture is formed by one or more of extruding, shaping, spray drying, pelletization, and agglomerization. 6. The catalyst system of claim 1 , wherein the zeolite comprises a large pore zeolite. 7. The catalyst system of claim 6 , wherein the large pore zeolite has an effective pore diameter of from about 6 Angstroms (Å) to about 15 Å. 8. The catalyst system of claim 1 , wherein the zeolite is selected from L-zeolite, X-zeolite, Y-zeolite, omega zeolite, beta zeolite, ZSM-3, ZSM-4, ZSM-5, ZSM-10, ZSM-11, ZSM-12, ZSM-20, ZSM-22, ZSM-23, ZSM-35, ZSM-48, ZSM-57, REY, USY, RE-USY, LZ-210, LZ-210-A, LZ-210-M, LZ-210-T, SSZ-23, SSZ-24, SSZ-25, SSZ-26, SSZ-28, SSZ-32, SSZ-36, SSZ-26, SSZ-31, SSZ-33, SSZ-35, SSZ-37, SSZ-41, SSZ-42, SSZ-44, MCM-58, SUZ-4, mordenite, faujasite, or a combination thereof. 9. The catalyst system of claim 1 , wherein the zeolite is an intermediate pore zeolite. 10. The catalyst system of claim 9 , wherein the intermediate pore zeolite has an effective pore diameter of from about 5 Angstroms (Å) to about 6 Å. 11. The catalyst system of claim 9 , wherein the intermediate pore zeolite is selected from ZSM-5, ZSM-11, ZSM-22, ZSM-23, ZSM-35; ZSM-48, ZSM-57, SUZ-4, SSZ-23, SSZ-25; SSZ-28, SSZ-32, SSZ-36, or a combination thereof. 12. The catalyst system of claim 1 , wherein the zeolite comprises a non-zeolitic molecular sieve with intermediate or large pores. 13. The catalyst system of claim 1 , wherein the one or more Group VIII metals are selected from platinum (Pt), palladium (Pd), rhodium (Rh), iridium (Ir), ruthenium (Ru), osmium (Os), or a combination thereof. 14. The catalyst system of claim 1 , wherein the catalyst support further comprises one or more metals selected from tin (Sn), gallium (Ga), thulium (Tm), indium (In), manganese (Mn), technetium (Tc), rhenium (Re), or a combination thereof. 15. The catalyst system of claim 1 , wherein the catalyst support is dried at a temperature in a range of about 100° F. to about 300° F. 16. The catalyst system of claim 1 , wherein the catalyst support is calcined at a temperature in a range of about 400° F. to about 900° F. 17. A reactor system comprising the catalyst system of claim 1 . 18. The reactor system of claim 17 , wherein the reactor system is an aromatization reactor system.

Assignees

Inventors

Classifications

  • Aromatics · CPC title

  • containing platinum group metals or compounds thereof · CPC title

  • containing crystalline zeolitic molecular sieves, other than aluminosilicates · CPC title

  • Halogenating · CPC title

  • Sulfiding · CPC title

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Frequently asked questions

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What does patent US11577230B2 cover?
Provided herein are catalyst supports, catalyst systems, and methods for making catalyst supports, catalyst systems, and performing chemical reactions with the catalyst systems. The catalyst supports include a zeolite and a binder including non-sodium counterions, such as ammonium counterions and/or potassium counterions. The catalyst systems include the catalyst supports and a catalytic materi…
Who is the assignee on this patent?
Chevron Phillips Chemical Co Lp
What technology area does this patent fall under?
Primary CPC classification B01J29/62. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Feb 14 2023 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 3 related publications on this page (citations in our corpus or others sharing the same primary CPC).