Zeolite composite catalysts for conversion of heavy reformate to xylenes
US-2018361365-A1 · Dec 20, 2018 · US
US12098121B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12098121-B2 |
| Application number | US-202318165626-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 7, 2023 |
| Priority date | Feb 7, 2023 |
| Publication date | Sep 24, 2024 |
| Grant date | Sep 24, 2024 |
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A method for producing one or more of benzene, toluene, or xylene may include contacting a feed stream including C 9+ alkylaromatic hydrocarbons with a catalyst mixture to form one or more of benzene, toluene, or xylene. The catalyst mixture may include mesoporous zeolite Beta, ZSM-5 zeolite, one or more active metals, and binder material. The feed stream may include C 9+ alkylaromatic hydrocarbons in an amount of at least 10 wt. %. The weight ratio of mesoporous zeolite Beta to ZSM-5 zeolite may be from 2 to 4.
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What is claimed is: 1. A method for producing one or more of benzene, toluene, or xylene, the method comprising: contacting a feed stream comprising C 9+ alkylaromatic hydrocarbons with a catalyst mixture to form one or more of benzene, toluene, or xylene, the catalyst mixture comprising: mesoporous zeolite Beta; ZSM-5 zeolite; one or more active metals; and binder material; and wherein: the feed stream is a heavy reformate and comprises at least 20 wt. % toluene; the feed stream comprises C 9+ alkylaromatic hydrocarbons in an amount of at least 10 wt. %; the weight ratio of mesoporous zeolite Beta to ZSM-5 zeolite is from 2 to 4; a product stream is formed by the contacting of the feed stream with the catalyst mixture; and the product stream comprises less than or equal to 0.5 wt. % ethylbenzene. 2. The method of claim 1 , wherein the weight ratio of mesoporous zeolite Beta to ZSM-5 zeolite is from 3 to 4. 3. The method of claim 1 , wherein the amount of mesoporous zeolite Beta relative to the total weight of the catalyst mixture is from 40 wt. % to 60 wt. %. 4. The method of claim 1 , wherein the amount of ZSM-5 zeolite relative to the total weight of the catalyst mixture is from 5 wt. % to 25 wt. %. 5. The method of claim 1 , wherein the amount of binder material relative to the total weight of the catalyst mixture is from 20 wt. % to 45 wt. %. 6. The method of claim 1 , wherein the binder material comprises aluminum. 7. The method of claim 1 , wherein the binder material comprises aluminum in an amount of at least 50 wt. %. 8. The method of claim 1 , wherein the amount of active metals relative to the total weight of the catalyst mixture is from 1 wt. % to 10 wt. %. 9. The method of claim 1 , wherein the active metals comprise one or more of molybdenum, platinum, nickel, cobalt, or combinations thereof. 10. The method of claim 1 , wherein the feed stream is contacted by the catalyst mixture at a temperature of from 50° C. to 600° C. 11. The method of claim 1 , wherein the feed stream comprises one or more of propylbenzenes, ethylmethylbenzenes, tetramethylbenzenes, ethyldimethylbenzenes, trimethylbenzenes, or diethylbenzenes, methylpropylbenzenes. 12. The method of claim 1 , wherein: the amount of mesoporous zeolite Beta relative to the total weight of the catalyst mixture is from 40 wt. % to 60 wt. %; the amount of ZSM-5 zeolite relative to the total weight of the catalyst mixture is from 5 wt. % to 25 wt. %; the amount of binder material relative to the total weight of the catalyst mixture is from 20 wt. % to 45 wt. %; the binder material comprises aluminum in an amount of at least 50 wt. %; the amount of active metals relative to the total weight of the catalyst mixture is from 1 wt. % to 10 wt. %; and the active metals comprise one or more of molybdenum, platinum, nickel, cobalt, or combinations thereof.
Catalytic processes · CPC title
containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium · CPC title
Noble metals · CPC title
of only one hydrocarbon · CPC title
from hydrocarbons containing a six-membered aromatic ring, e.g. propyltoluene to vinyltoluene · CPC title
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