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. 23, 2020

Filed:

Jul. 16, 2018
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Kareemuddin Shaik, Dhahran, SA;

Lianhui Ding, Dhahran, SA;

Mazin Tamimi, Dhahran, SA;

Ibrahim Abba, Dhahran, SA;

Abdennour Bourane, Dhahran, SA;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 67/02 (2006.01); B01J 35/10 (2006.01); C10G 47/20 (2006.01); C10G 45/08 (2006.01); C10G 69/04 (2006.01); C10G 53/02 (2006.01); C10G 57/00 (2006.01); C10G 65/10 (2006.01); C10G 69/02 (2006.01); C10G 69/06 (2006.01); C10G 65/12 (2006.01);
U.S. Cl.
CPC ...
C10G 67/02 (2013.01); B01J 35/1061 (2013.01); C10G 45/08 (2013.01); C10G 47/20 (2013.01); C10G 53/02 (2013.01); C10G 57/00 (2013.01); C10G 65/10 (2013.01); C10G 65/12 (2013.01); C10G 69/02 (2013.01); C10G 69/04 (2013.01); C10G 69/06 (2013.01); C10G 2300/202 (2013.01); C10G 2300/205 (2013.01); C10G 2300/308 (2013.01); C10G 2400/02 (2013.01); C10G 2400/04 (2013.01);
Abstract

According to one embodiment, a heavy oil may be processed by a method that may include upgrading at least a portion of the heavy oil to form an upgraded oil, where the upgrading comprising contacting the heavy oil with a hydrodemetalization catalyst, a transition catalyst, a hydrodenitrogenation catalyst, a first hydrocracking catalyst, and a second hydrocracking catalyst downstream of the first hydrocracking catalyst to remove at least a portion of metals, nitrogen, or aromatics content from the heavy oil and form the upgraded oil. The final boiling point of the upgraded oil may be less than or equal to 540° C. The second hydrocracking catalyst cracks at least a portion of vacuum gas oil in the heavy oil. The first hydrocracking catalyst may comprise a greater average pore size than the second hydrocracking catalyst.


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