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. 18, 2024

Filed:

Apr. 26, 2023
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Mourad Younes, Dhahran, SA;

Aqil Jamal, Dhahran, SA;

Aadesh Harale, Dhahran, SA;

Ibrahim Abba, Dhahran, SA;

Abdennour Bourane, Ras Tanura, SA;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F02C 3/20 (2006.01); B01D 53/047 (2006.01); B01J 7/00 (2006.01); B01J 19/24 (2006.01); C01B 3/02 (2006.01); C01B 3/12 (2006.01); C01B 3/34 (2006.01); C01B 3/56 (2006.01); C10G 2/00 (2006.01); C10G 69/00 (2006.01);
U.S. Cl.
CPC ...
F02C 3/20 (2013.01); B01D 53/047 (2013.01); B01J 7/00 (2013.01); B01J 19/245 (2013.01); C01B 3/02 (2013.01); C01B 3/12 (2013.01); C01B 3/34 (2013.01); C01B 3/56 (2013.01); C10G 2/50 (2013.01); C10G 69/00 (2013.01); B01D 2256/16 (2013.01); B01D 2257/502 (2013.01); B01D 2257/504 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/042 (2013.01); C01B 2203/047 (2013.01); C01B 2203/0475 (2013.01); C01B 2203/065 (2013.01); C10G 2300/205 (2013.01); C10G 2300/206 (2013.01); C10G 2300/42 (2013.01); C10G 2400/30 (2013.01); F05D 2220/32 (2013.01);
Abstract

A processing facility is provided. The processing facility includes an asphaltenes and metals (AM) removal system configured to process a feed stream to produce a power generation stream, a hydroprocessing feed stream, and an asphaltenes stream. A power generation system is fed by the power generation feed stream. A hydroprocessing system is configured to process the hydroprocessing feed stream to form a gas stream and a liquid stream. A hydrogen production system is configured to produce hydrogen, carbon monoxide and carbon dioxide from the gas feed stream. A carbon dioxide conversion system is configured to produce synthetic hydrocarbons from the carbon dioxide, and a cracking system is configured to process the liquid feed stream.


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