The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Oct. 16, 2018

Filed:

Dec. 16, 2015
Applicant:

King Abdullah University of Science and Technology, Thuwal, SA;

Inventors:

Rakan Sulaiman Bilaus, Thuwal, SA;

Ingo Pinnau, Thuwal, SA;

Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 5/27 (2006.01); B01J 19/24 (2006.01); B01J 31/06 (2006.01); B01J 8/02 (2006.01); B01J 31/10 (2006.01); B01J 35/06 (2006.01);
U.S. Cl.
CPC ...
C07C 5/2756 (2013.01); B01J 8/02 (2013.01); B01J 19/2475 (2013.01); B01J 31/06 (2013.01); B01J 31/10 (2013.01); C07C 5/2797 (2013.01); B01J 35/065 (2013.01); B01J 2219/0004 (2013.01); C07C 2531/10 (2013.01); Y02P 20/52 (2015.11);
Abstract

A process for producing xylenes, in particular para-xylene that is less energy intensive than conventional processes is provided. In an embodiment the process comprises contacting a feed mixture in an isomerization zone with a catalyst at isomerization conditions and producing an isomerized product comprising a higher proportion of p-xylene than in the feed mixture, wherein the catalyst comprises an acidic sulfonated catalytic membrane. Xylene isomerization can also be coupled with a p-xylene extraction process, where the raffinate (p-xylene deprived stream) from the extraction process is fed to an isomerization reactor to produce p-xylene. In an embodiment, the process can comprise: a) providing a feed stream comprising a mixture of xylene isomers including p-xylene; b) extracting p-xylene from the feed stream using a separator to separate the feed stream into a p-xylene rich stream and a p-xylene deprived stream; and c) delivering the p-xylene deprived stream to an isomerization unit, the isomerization unit including an acidic sulfonated catalytic membrane, and using the isomerization unit to produce an isomerized product comprising a higher proportion of p-xylene than in the p-xylene deprived stream delivered to the isomerization unit. In any one or more aspects, the isomerization unit can be operated at a temperature in the range of less than 350°, for example about 20° C. to about 200° C.


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