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. 22, 2026

Filed:

Apr. 23, 2024
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Aaron Chi Akah, Dhahran, SA;

Rashed Aleisa, Dhahran, SA;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 55/06 (2006.01); B01D 3/14 (2006.01); B01D 15/08 (2006.01); B01J 8/00 (2006.01); B01J 8/26 (2006.01); B01J 23/889 (2006.01); B01J 23/94 (2006.01); B01J 35/31 (2024.01); B01J 38/30 (2006.01);
U.S. Cl.
CPC ...
C10G 55/06 (2013.01); B01D 3/143 (2013.01); B01D 15/08 (2013.01); B01J 8/001 (2013.01); B01J 8/26 (2013.01); B01J 23/8892 (2013.01); B01J 23/94 (2013.01); B01J 35/31 (2024.01); B01J 38/30 (2013.01); B01J 2208/00548 (2013.01); B01J 2208/00628 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/1048 (2013.01); C10G 2300/706 (2013.01);
Abstract

A process for upgrading plastic derived oil includes contacting the plastic derived oil with a mixed catalyst in a first reactor, where the mixed catalyst includes a decontamination catalyst and a cracking catalyst different from the decontamination catalyst. The first reactor reduces concentrations of halogen-containing compounds in the plastic derived oil. The process includes passing the first reactor effluent to a second reactor and contacting the first reactor effluent with the cracking catalyst to produce a second effluent comprising light olefins and naphtha range hydrocarbons. The process includes separating used mixed catalyst from the first reactor to produce a used decontamination catalyst and a second used cracking catalyst, and regenerating the decontamination catalyst and cracking catalyst in separate regenerators to reduce exposure of the cracking catalyst to halogen-containing compounds produced during regeneration of the used decontamination catalyst.


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