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:
Jun. 07, 2022

Filed:

Oct. 29, 2020
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Sameer A. Al-Ghamdi, Dhahran, SA;

Saad Al-Bogami, Dammam, SA;

Abdennour Bourane, Ras Tanura, SA;

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 51/02 (2006.01); C10G 11/18 (2006.01); B01J 8/18 (2006.01); B01J 8/26 (2006.01); C10G 51/06 (2006.01); B01D 3/14 (2006.01); B01J 38/38 (2006.01); C10G 7/00 (2006.01); C10G 11/04 (2006.01);
U.S. Cl.
CPC ...
C10G 51/02 (2013.01); B01D 3/143 (2013.01); B01J 8/1809 (2013.01); B01J 8/26 (2013.01); B01J 38/38 (2013.01); C10G 7/00 (2013.01); C10G 11/04 (2013.01); C10G 11/182 (2013.01); C10G 11/187 (2013.01); C10G 51/06 (2013.01); B01J 2208/00628 (2013.01); C10G 2300/107 (2013.01); C10G 2300/1048 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/4081 (2013.01); C10G 2300/708 (2013.01); C10G 2400/16 (2013.01); C10G 2400/20 (2013.01); C10G 2400/22 (2013.01);
Abstract

Methods for operating a system having two downflow high-severity FCC units for producing products from a hydrocarbon feed includes introducing the hydrocarbon feed to a feed separator and separating it into a lesser boiling point fraction and a greater boiling point fraction. The greater boiling point fraction is passed to the first FCC unit and cracked in the presence of a first catalyst at 500° C. to 700° C. to produce a first cracking reaction product and a spent first catalyst. The lesser boiling point fraction is passed to the second FCC unit and cracked in the presence of a second catalyst at 500° C. to 700° C. to produce a second cracking reaction product and a spent second catalyst. At least a portion of the spent first catalyst or the spent second catalyst is passed back to the first FCC unit, the second FCC unit or both.


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