Disproportionation and transalkylation of heavy aromatic hydrocarbons

US10800718B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10800718-B2
Application numberUS-201716331999-A
CountryUS
Kind codeB2
Filing dateFeb 10, 2017
Priority dateOct 4, 2016
Publication dateOct 13, 2020
Grant dateOct 13, 2020

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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.

Disclosed herein is a process for producing para-xylene comprising the steps of: (a) contacting a feedstock comprising toluene with a first catalyst under effective vapor phase toluene disproportionation conditions to disproportionate said toluene and produce a first product comprising benzene, unreacted toluene and greater than equilibrium amounts of para-xylene; and (b) contacting a feedstock comprising C9+ aromatic hydrocarbons and benzene with a second catalyst in the presence of 0 wt. % or more of hydrogen having a 0 to 10 hydrogen/hydrocarbon molar ratio under effective C9+ transalkylation conditions to transalkylate said C9+ aromatic hydrocarbons and produce a second product comprising xylenes.

First claim

Opening claim text (preview).

What is claimed is: 1. A process for producing xylene from C 9+ aromatic hydrocarbons, the process comprising: (a) contacting toluene with a first catalyst in the presence of 0 wt. % or more of hydrogen under effective vapor phase toluene disproportionation conditions to disproportionate at least part of the toluene and produce a first product comprising para-xylene, benzene and remaining toluene; (b) contacting C 9+ aromatic hydrocarbons and at least part of the benzene and/or toluene from the first product with a second catalyst in the presence of 0 wt. % or more of hydrogen under effective C 9+ transalkylation conditions to transalkylate at least part of the C 9+ aromatic hydrocarbons and produce a second product comprising xylenes, wherein a portion of the first product is supplied to the contacting in (b) without intermediate separation; and (c) separating para-xylene from a portion of the first product. 2. The process of claim 1 , wherein the contacting in (b) is conducted under liquid phase C 9+ transalkylation conditions. 3. The process of claim 1 , further comprising separating benzene from a portion of the first product and supplying at least part of the separated benzene to the contacting in (b). 4. The process of claim 1 , further comprising: (d) separating the remaining toluene from a portion of the first product; and (e) supplying at least part of the separated toluene to the contacting in (b) or recycling the separated toluene to contacting in (a). 5. The process of claim 1 , further comprising separating para-xylene from a portion of the first product and the second product. 6. The process of claim 1 , wherein the first catalyst comprises selectivated ZSM-5. 7. The process of claim 6 , wherein the selectivated ZSM-5 is silicon selectivated ZSM-5 or carbon selectivated ZSM-5. 8. The process of claim 7 , wherein the first catalyst further comprises 0.01 wt. % to 5 wt. % of a metal selected from the group consisting of Pd, Pt, Ni, Rh, Sn, and a combination of two or more thereof. 9. The process of claim 1 , wherein the second catalyst comprises a molecular sieve having at least one of an MWW framework, a *BEA framework, a BEC framework, a FAU framework, or a MOR framework, or a mixture of two or more thereof. 10. The process of claim 9 , wherein the second catalyst comprises a molecular sieve having an MWW framework type selected from the group consisting of MCM-22, MCM-36, MCM-49, MCM-56, SSZ-25, MIT-1, EMM-10, EMM-10-P, EMM-12, EMM-13, ITQ-1, ITQ-2, ITQ-30, UZM-8, UZM-8HS, UZM-37, and mixtures of two or more thereof. 11. The process of claim 9 , wherein the second catalyst further comprises 0.01 wt. % to 5 wt. % of a metal selected from the group consisting of Pd, Pt, Ni, Rh, Sn, and a combination of two or more thereof.

Assignees

Inventors

Classifications

  • containing iron group metals, noble metals or copper · CPC title

  • C07C6/126Primary

    of more than one hydrocarbon · CPC title

  • containing arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium · CPC title

  • containing iron group metals, noble metals or copper · CPC title

  • Mixtures of different zeolites · CPC title

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What does patent US10800718B2 cover?
Disclosed herein is a process for producing para-xylene comprising the steps of: (a) contacting a feedstock comprising toluene with a first catalyst under effective vapor phase toluene disproportionation conditions to disproportionate said toluene and produce a first product comprising benzene, unreacted toluene and greater than equilibrium amounts of para-xylene; and (b) contacting a feedstock…
Who is the assignee on this patent?
Exxonmobil Chemical Patents Inc
What technology area does this patent fall under?
Primary CPC classification C07C6/126. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Oct 13 2020 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 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).