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:
Jan. 02, 2024

Filed:

May. 16, 2022
Applicant:

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

Inventor:

Xiaoying Bao, Houston, TX (US);

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 5/333 (2006.01); C07C 5/41 (2006.01); B01J 38/10 (2006.01); B01J 21/10 (2006.01); C10G 29/04 (2006.01); C10G 25/00 (2006.01); C10G 31/06 (2006.01); B01J 35/00 (2006.01); B01J 21/04 (2006.01); B01J 23/10 (2006.01);
U.S. Cl.
CPC ...
C10G 29/04 (2013.01); B01J 21/04 (2013.01); B01J 21/10 (2013.01); B01J 23/10 (2013.01); B01J 35/0026 (2013.01); B01J 38/10 (2013.01); C07C 5/3337 (2013.01); C07C 5/417 (2013.01); C10G 25/003 (2013.01); C10G 31/06 (2013.01); C07C 2521/10 (2013.01);
Abstract

Processes for upgrading a hydrocarbon. The process can include (I) contacting a hydrocarbon-containing feed with a catalyst that can include a Group 8-10 element or a compound thereof disposed on a support to effect conversion of the hydrocarbon-containing feed to produce a coked catalyst and an effluent. The process can also include (II) contacting the coked catalyst with an oxidant to effect combustion the coke to produce a regenerated catalyst. The process can also include (IIa) contacting the regenerated catalyst with a reducing gas to produce a regenerated and reduced catalyst. The process can also include (III) contacting an additional quantity of the hydrocarbon-containing feed with the regenerated and reduced catalyst. A cycle time from the contacting the hydrocarbon-containing feed with the catalyst in step (I) to the contacting the additional hydrocarbon-containing feed with the regenerated and reduced catalyst in step (III) can be ≤1 hours.


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