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:

Oct. 27, 2020
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Abdennour Bourane, Dhahran, SA;

Raed Abudawoud, Khobar, SA;

Ibrahim Abba, Dhahran, SA;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 8/18 (2006.01); B01J 8/20 (2006.01); B01J 8/08 (2006.01); C10G 11/18 (2006.01); C07C 4/06 (2006.01); C10G 51/06 (2006.01); C10G 55/08 (2006.01); B01J 8/26 (2006.01); B01J 8/00 (2006.01);
U.S. Cl.
CPC ...
C10G 51/06 (2013.01); B01J 8/003 (2013.01); B01J 8/0015 (2013.01); B01J 8/085 (2013.01); B01J 8/1827 (2013.01); B01J 8/20 (2013.01); B01J 8/26 (2013.01); C07C 4/06 (2013.01); C10G 11/182 (2013.01); C10G 11/185 (2013.01); C10G 11/187 (2013.01); C10G 55/08 (2013.01); B01J 2208/00752 (2013.01); B01J 2208/00761 (2013.01); C07C 2529/08 (2013.01); C07C 2529/40 (2013.01); C10G 2300/107 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/70 (2013.01); C10G 2400/20 (2013.01); C10G 2400/22 (2013.01);
Abstract

Systems and processes are disclosed for producing petrochemical products, such as ethylene, propene and other olefins from crude oil in high severity fluid catalytic cracking (HSFCC) units. Processes include separating a crude oil into a light fraction and a heavy fraction, cracking the light fraction and heavy fraction in separation separate cracking reaction zones, and regenerating the cracking catalysts in a two-zone having a first regeneration zone for the first catalyst (heavy fraction) and a second regeneration zone for the second catalyst (light fraction) separate from the first regeneration zone. Flue gas from the first catalyst regeneration zone is passed to the second regeneration zone to provide additional heat to raise the temperature of the second catalyst of the light fraction side. The disclosed systems and processes enable different catalysts and operating conditions to be utilized for the light fraction and the heavy fraction of a crude oil feed.


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