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. 10, 2025

Filed:

Jun. 23, 2021
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Omer Refa Koseoglu, Dhahran, SA;

Gerard De Nazelle, Dhahran, SA;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 65/06 (2006.01); C10G 1/10 (2006.01); C10G 7/06 (2006.01); C10G 35/00 (2006.01); C10G 45/08 (2006.01); C10G 45/36 (2006.01); C10G 65/16 (2006.01);
U.S. Cl.
CPC ...
C10G 65/16 (2013.01); C10G 1/10 (2013.01); C10G 7/06 (2013.01); C10G 35/00 (2013.01); C10G 45/08 (2013.01); C10G 45/36 (2013.01); C10G 65/06 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/301 (2013.01); C10G 2300/4006 (2013.01); C10G 2300/4056 (2013.01); C10G 2400/04 (2013.01); C10G 2400/06 (2013.01); C10G 2400/30 (2013.01);
Abstract

Method of producing pyrolysis products from mixed plastics along with an associated system for processing mixed plastics. The method includes conducting pyrolysis of a plastic feedstock to produce plastic pyrolysis oil; feeding the plastic pyrolysis oil to a first fractionator to separate the plastic pyrolysis oil into a distillate fraction including naphtha and diesel and a vacuum gas oil fraction; and feeding the distillate fraction to a three step hydrotreating operation. The three step hydrotreating operation includes feeding the distillate fraction to a first hydrotreating unit to remove di-olefins to produce a first product stream, feeding the first product stream to a second hydrotreating unit to remove mono-olefins to produce a second product stream; and feeding the second product stream to a third hydrotreating unit to remove sulfur and nitrogen by hydrodesulfurization and hydrodenitrogenation to produce a third product stream. Such system may be integrated with a conventional refinery.


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