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:
Jan. 18, 2022

Filed:

Jun. 25, 2020
Applicant:

Saudi Arabian Oil Company, Dhahran, SA;

Inventors:

Miao Sun, Dhahran, SA;

Qi Xu, Dhahran, SA;

Zhonglin Zhang, Dhahran, SA;

Sohel K. Shaikh, Dhahran, SA;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 53/10 (2006.01); B01J 19/24 (2006.01); B01J 27/19 (2006.01); B01J 27/188 (2006.01); B01J 23/30 (2006.01); B01J 23/28 (2006.01); B01J 19/00 (2006.01);
U.S. Cl.
CPC ...
C10G 53/10 (2013.01); B01J 19/0006 (2013.01); B01J 19/2445 (2013.01); B01J 23/28 (2013.01); B01J 23/30 (2013.01); B01J 27/188 (2013.01); B01J 27/19 (2013.01); B01J 2219/00033 (2013.01); B01J 2219/00038 (2013.01); C10G 2300/206 (2013.01);
Abstract

In accordance with one or more embodiments of the present disclosure, a continuous catalytic deasphalting process includes introducing a feed comprising crude oil and solvent to a first reactor to deasphalt the feed, producing polymerized asphaltene adsorbed to the catalyst and deasphalted oil; introducing solvent to a second reactor to regenerate catalyst in the second reactor while the deasphalting step is performed in the first reactor; introducing a wash solvent to the first reactor after deasphalting to remove the polymerized asphaltene, thereby regenerating the catalyst in the first reactor and producing a mixture comprising solvent and polymerized asphaltene; passing the mixture to a separator downstream of the reactor system to separate the wash solvent from the polymerized asphaltenes; and reintroducing at least a portion of the separated wash solvent to at least one of the first and second reactors.


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