Catalyst supports and catalyst systems and methods

Patent metadata

Field	Value
Publication number	US-11529617-B2
Application number	US-202016991540-A
Country	US
Kind code	B2
Filing date	Aug 12, 2020
Priority date	Aug 12, 2020
Publication date	Dec 20, 2022
Grant date	Dec 20, 2022

Abstract

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

I claim:

1. A process for making a catalyst system, the process comprising:
contacting a zeolite and a binder to form a mixture, wherein the zeolite comprises a non-zeolitic molecular sieve with intermediate or large pores, and wherein the binder comprises a colloidal silica including potassium counterions, ammonium counterions, or a combination thereof, and substantially no sodium counterions;
extruding and/or shaping the mixture to form a dimensioned mixture;
drying the dimensioned mixture to form a substantially dried dimensioned mixture;
calcining the substantially dried dimensioned mixture to produce a catalyst support;
adding one or more Group VIII metals and one or more halides to the catalyst support to form a metalized and halided catalyst support; and
drying and calcining the metalized and halided catalyst support to form the catalyst system.

2. The process of claim 1 , wherein the mixture further comprises an extrusion aid.

3. The process of claim 2 , wherein the extrusion aid comprises a cellulose ether.

4. The process of claim 3 , wherein the cellulose ether comprises ethylcellulose, carboxymethylcellulose, ethylhydroxyethylcellulose, hydroxyethylcellulose, hydroxypropylcellulose, methylhydroxyethylcellulose, methylhydroxypropylcellulose, or a combination thereof.

5. The process of claim 1 , wherein the mixture further comprises water in an amount sufficient to permit the mixture to form the dimensioned mixture upon the extruding and/or shaping.

6. The process of claim 1 , wherein the zeolite has large pores.

7. The process of claim 6 , wherein the zeolite has an effective pore diameter of from about 6 Angstroms (Å) to about 15 Å.

8. The process of claim 1 , wherein the zeolite further comprises a material 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 process of claim 1 , wherein the zeolite has intermediate pores.

10. The process of claim 9 , wherein the zeolite has an effective pore diameter of from about 5 Angstroms (Å) to about 6 Å.

11. The process of claim 1 , wherein the zeolite further comprises an intermediate pore zeolite 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 process of claim 1 , wherein the adding of the one or more Group VIII metals and the one or more halides comprises adding the one or more Group VIII metals and the one or more halides via ion-exchange, incipient wetness, pore fill, impregnation, or a combination thereof.

13. The process of claim 1 , wherein the adding of the one or more Group VIII metals comprises impregnation with a metal-containing solution.

14. A process for converting a hydrocarbon feed to aromatics, the process comprising:
contacting the catalyst system of claim 1 with one or more hydrocarbons in a reaction zone under aromatization conditions;
recovering an aromatic product from the reaction zone; and
purifying the aromatic product to produce benzene, toluene, paraxylene, orthoxylene, metaxylene, or a combination thereof.

15. The process of claim 14 , wherein the catalyst system is reduced prior to the contacting of the catalyst system with the one or more hydrocarbons.

16. The process of claim 14 , wherein the one or more hydrocarbons comprises a naphtha feed.

17. The process of claim 14 , wherein the one or more hydrocarbons comprise acyclic paraffinic hydrocarbons, acyclic olefinic hydrocarbons, acetylenic hydrocarbons, cyclic paraffin hydrocarbons, cyclic olefin hydrocarbons, or a combination thereof.

18. The process of claim 1 , wherein the one or more Group VIII metals are selected from the group consisting of platinum, palladium, rhodium, iridium, ruthenium, and osmium.

19. The process of claim 1 , further comprising adding one or more non-platinum group metals to the catalyst support, wherein the one or more non-platinum group metals are selected from the group consisting of tin, gallium, thulium, indium, and a metal of Group VII.

Assignees

• Chevron Phillips Chemical Co Lp

Inventors

• Snell Ryan W

Classifications

• C10G35/065

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

• C10G2400/30

  Aromatics · CPC title

• B01J37/0236

  Drying, e.g. preparing a suspension, adding a soluble salt and drying · CPC title

• C10G35/085

  containing platinum group metals or compounds thereof · CPC title

• B01J37/0207

  Pretreatment of the support · CPC title