Catalyst compositions and use in heavy aromatics conversion processes

US10058853B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10058853-B2
Application numberUS-201615004623-A
CountryUS
Kind codeB2
Filing dateJan 22, 2016
Priority dateFeb 4, 2015
Publication dateAug 28, 2018
Grant dateAug 28, 2018

How to read this patent

A practical reading order for non-experts. Skip the full description unless you need deep technical detail.

  1. Title

    What the patent document calls the invention.

  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

    Who owns or filed the patent and who is credited as inventor.

  4. Key dates

    Filing, priority, publication, and grant dates set the timeline.

  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

    Prior art links and similar publications in this corpus.

Abstract

Official abstract text for this publication.

Disclosed is a catalyst composition and its use in a process for the conversion of a feedstock containing C 8 + aromatic hydrocarbons to produce light aromatic products, comprising benzene, toluene and xylene. The catalyst composition comprises a mordenite zeolite synthesized from TEA or MTEA, optionally at least one first metal of Group 10 of the IUPAC Periodic Table, and optionally at least one second metal of Group 11 to 15 of the IUPAC Periodic Table, wherein said mordenite zeolite has a mesopore surface area of greater than 30 m 2 /g and said mordenite zeolite comprises agglomerates composed of primary crystallites, wherein said primary crystallites have an average primary crystal size as measured by TEM of less than 80 nm and an aspect ratio of less than 2.

First claim

Opening claim text (preview).

The invention claimed is: 1. A process, comprising: contacting a feedstock comprising toluene, C 8+ aromatic hydrocarbons and optionally hydrogen with a catalyst under suitable conversion conditions to transalkylate the C 8+ aromatic hydrocarbons with toluene; and producing an effluent stream comprising aromatic products that are lighter than at least some of the C 8+ aromatic hydrocarbons in the feedstock, wherein the aromatic products comprise xylenes, wherein the catalyst composition comprises a mordenite zeolite synthesized from TEA or MTEA, wherein the mordenite zeolite has a mesopore surface area of greater than 30 m 2 /g and the mordenite comprises agglomerates composed of primary crystallites, and wherein the primary crystallites have an average primary crystal size as measured by TEM of less than 80 nm and an aspect ratio of less than 2. 2. The process of claim 1 , wherein the catalyst further comprises (ii) 0.005 to 5.0 wt. % of at least one first metal of Group 10 of the IUPAC Periodic Table, based on the weight of the catalyst composition. 3. The process of claim 2 , wherein the catalyst further comprises (iii) 0.01 to 5.0 wt. % of at least one a second metal of Group 11 to 15 of the IUPAC Periodic Table, based on the weight of the catalyst composition. 4. The process of claim 1 , wherein the C 8+ aromatic hydrocarbons of the feedstock comprise aromatic compounds having nine or more carbon atoms. 5. The process of claim 1 , wherein the feedstock further comprises benzene. 6. The process of claim 1 , wherein the C 8+ aromatic hydrocarbons comprises aromatic compounds having a boiling point in the range of 135° C. to 260° C. at atmospheric pressure. 7. The process of claim 1 , wherein the effluent stream comprises at least one selected from the group consisting of benzene, and toluene. 8. The process of claim 1 , wherein the suitable conversion conditions comprise a temperature of 340° C. to 515° C., a pressure from 380 kPa (55 psia) to 4240 kPa (615 psia) and a weight hourly space velocity (WHSV) in the range of 1 to 100 hr −1 based on the weight of the feedstock. 9. The process of claim 1 , further comprising a reactor for contacting said feedstock with the catalyst composition under the suitable conversion conditions, wherein the reactor comprises at least one fixed catalyst bed of the catalyst composition. 10. The process of claim 1 , further comprising a reactor for contacting feedstock with the catalyst composition under the suitable conversion conditions, wherein the reactor comprises at least one fluid bed of the catalyst composition.

Assignees

Inventors

Classifications

  • Iron group metals or copper · CPC title

  • B01J29/44Primary

    Noble metals · CPC title

  • Noble metals · CPC title

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

  • MFS-type, e.g. ZSM-57 · CPC title

Patent family

Related publications grouped by family.

External sources

Frequently asked questions

Answers are generated from the same data shown on this page.

What does patent US10058853B2 cover?
Disclosed is a catalyst composition and its use in a process for the conversion of a feedstock containing C 8 + aromatic hydrocarbons to produce light aromatic products, comprising benzene, toluene and xylene. The catalyst composition comprises a mordenite zeolite synthesized from TEA or MTEA, optionally at least one first metal of Group 10 of the IUPAC Periodic Table, and optionally at least o…
Who is the assignee on this patent?
Exxonmobil Chemical Patents Inc
What technology area does this patent fall under?
Primary CPC classification B01J29/44. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Aug 28 2018 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 12 related publications on this page (citations in our corpus or others sharing the same primary CPC).