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:
Sep. 19, 2023

Filed:

Feb. 11, 2021
Applicant:

Exxonmobil Chemical Patents Inc., Baytown, TX (US);

Inventors:

Xiaoying Bao, Houston, TX (US);

John S. Coleman, Houston, TX (US);

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 5/333 (2006.01); B01J 21/10 (2006.01); C07C 5/41 (2006.01); C07C 5/367 (2006.01); B01J 38/10 (2006.01); B01J 38/32 (2006.01); B01J 35/00 (2006.01); B01J 23/62 (2006.01); B01J 23/10 (2006.01); B01J 21/04 (2006.01); B01J 21/06 (2006.01);
U.S. Cl.
CPC ...
C07C 5/3337 (2013.01); B01J 21/04 (2013.01); B01J 21/066 (2013.01); B01J 21/10 (2013.01); B01J 23/10 (2013.01); B01J 23/626 (2013.01); B01J 35/0026 (2013.01); B01J 38/10 (2013.01); B01J 38/32 (2013.01); C07C 5/367 (2013.01); C07C 5/417 (2013.01); C07C 2521/04 (2013.01); C07C 2521/06 (2013.01); C07C 2521/10 (2013.01); C07C 2523/10 (2013.01); C07C 2523/62 (2013.01);
Abstract

Processes for upgrading a hydrocarbon. The process can include contacting a hydrocarbon-containing feed with fluidized catalyst particles that can include a Group 8-10 element or a compound thereof disposed on a support to effect one or more of dehydrogenation, dehydroaromatization, and dehydrocyclization of at least a portion of the hydrocarbon-containing feed to produce a coked catalyst and an effluent. The process can also include contacting at least a portion of the coked catalyst particles with an oxidant to effect combustion of at least a portion of the coke to produce regenerated catalyst particles. The process can also include contacting an additional quantity of the hydrocarbon-containing feed with at least a portion of the regenerated catalyst particles to produce additional effluent and re-coked catalyst particles.


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