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:
Mar. 22, 2022

Filed:

Mar. 05, 2020
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Aadesh Harale, Dhahran, SA;

Ibrahim Abba, Dhahran, SA;

Ahmad Khowaiter, Dhahran, SA;

Abdennour Bourane, Dhahran, SA;

Aqil Jamal, Dhahran, SA;

Mourad Younes, Dhahran, SA;

Assignee:
Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
B01J 8/24 (2006.01); C01B 3/34 (2006.01); C10G 65/12 (2006.01); C10G 65/14 (2006.01); C10G 69/00 (2006.01); C01B 32/50 (2017.01); B01D 3/06 (2006.01); B01D 19/00 (2006.01); B01J 8/18 (2006.01); B01J 19/24 (2006.01); C01B 3/36 (2006.01); C01B 3/48 (2006.01); C07C 6/12 (2006.01); C07C 51/14 (2006.01); C10G 2/00 (2006.01);
U.S. Cl.
CPC ...
C10G 69/00 (2013.01); B01D 3/06 (2013.01); B01D 19/0057 (2013.01); B01J 8/1827 (2013.01); B01J 8/24 (2013.01); B01J 19/245 (2013.01); B01J 19/2445 (2013.01); C01B 3/34 (2013.01); C01B 3/36 (2013.01); C01B 3/48 (2013.01); C01B 32/50 (2017.08); C07C 6/126 (2013.01); C07C 51/14 (2013.01); C10G 2/32 (2013.01); C10G 2/344 (2013.01); B01J 2208/00893 (2013.01); B01J 2219/0004 (2013.01); B01J 2219/00038 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0244 (2013.01); C01B 2203/0255 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/1241 (2013.01); C10G 2300/1044 (2013.01); C10G 2300/1055 (2013.01); C10G 2400/20 (2013.01); C10G 2400/30 (2013.01);
Abstract

Systems and methods for direct crude oil upgrading to hydrogen and chemicals including separating an inlet hydrocarbon stream into a light fraction and a heavy fraction comprising diesel boiling point temperature range material; producing from the light fraction syngas comprising Hand CO; reacting the CO produced; producing from the heavy fraction and separating CO, polymer grade ethylene, polymer grade propylene, Ccompounds, cracking products, light cycle oils, and heavy cycle oils; collecting and purifying the COproduced from the heavy fraction; processing the Ccompounds to produce olefinic oligomerate and paraffinic raffinate; separating the cracking products; oligomerizing a light cut naphtha stream; hydrotreating an aromatic stream; hydrocracking the light cycle oils to produce a monoaromatics product stream; gasifying the heavy cycle oils; reacting the CO produced from gasifying the heavy cycle oils; collecting and purifying the CO; and processing and separating produced aromatic compounds into benzene and paraxylene.


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